Chapter 1
Thermal Degradation of Polymers C. DAVID
1. Introduction One of the main interests of the polymer chemist is to develop new polymers that have good mechanical properties at high temperature and to improve the thermal stability of existing polymers. Extensive studies of the mechanism of thermal degradation of the presently available macromolecules are very helpful in this field. Heat treatment of polymers may affect either the main chain linkages (often carbon-carbon bonds) or substituent atoms and side chains. Scission of the main chain often gives free radicals and can occur either at random in the chain or at weak links resulting from anomalous structures as in poly-a-methylstyrene and polyethylene. Also the chain ends often present labile structures suitable for initiation of thermal degradation. This is observed with polymethylmethacrylate chains terminated by double bonds. The macro-radicals formed by the rupture of the main chain can undergo depolymerization by a chain reaction the length of which varies according to the structure of the polymer and the temperature. They can also be involved in inter- or intramolecular transfer as in polystyrene and polyethylene heated at moderate temperature. A decrease in molecular weight is then often observed. Formation of crosslinks sometimes occurs if the main chain contains double bonds. An example of this is network formation in polyvinylchloride at unsaturated linkages formed under heat treatment. Reactions at the site of side chains or substituents of the main chain can also markedly affect the polymer properties. Elimination reactions of the type
have been identified with PVC. Radicals are not necessarily involved. If conjugated sequences of double bonds are formed, discolouration of the sample ensues. A free radical formed by side-chain breakage can also induce main-chain scission according to References p p . 165-1 73
2
4H-CH2-CH-CH2I I R R
+
-kH-CH2-CH-CH2-
I R
+ R'
-
-CH=CH2 +
::
H-cH2-
R
Volatile products are formed in the latter two reactions. The mechanism of degradation of condensation polymers is often complicated by the presence of traces of water which are difficult to eliminate from the samples. Hydrolysis then occurs at high temperature and competes with the pure thermal degradation. New chain ends are formed which may in some cases markedly affect the polymer stability. Cyclization is another frequent reaction of the side chain; a typical example is the heat-resistant cyclized structures formed in heated polyacry lonitrile
A diagram of the most probable reactions involved in thermal degradation of polymers is given in Scheme 1. It must be emphasized, however, that the instability of macromolecules under heat treatment is often due to the presence of anomalous weak links in the polymer. In these cases, low molecular weight models of the normal chain unit are much more stable than the polymer. The anomalous structure can be
'
r Breaking (1) Main chain reaction
r
Molecular weight decrease
1 Volatile formation
r Monomer
1n-Mers
Molecular weight increase
Crosslinking ---L
[ Gel formation
Side chain or substituent elimination (2) Side chain or substituent reaction I
L Cyclization Scheme 1. Simplified diagram of polymer degradation.
r
Volatile formation
r Main-chain scission
Main-chain crosslinking Unsaturation formation
3 situated in the chain or at the chain ends. The terminal double bonds in polymethylmethacrylate and -OH end structures in polyoxymethylene are the site of initiation of the depolymerization. Allylic chlorines in the polyvinylchloride chain are weak spots responsible for the dehydrochlorination reaction. The purpose of this review is to give insight into the experimental techniques, theories and present state of knowledge in the field of the thermal degradation of high polymers. Section 2 describes the techniques used for the characterization of volatile products and non-volatile polymeric residues, and for the determination of the rate of volatilization and heat evolved during pyrolysis. The measurement of the rate of weight loss and of the heat of reaction allow the evaluation of the kinetic and thermodynamic parameters of the reaction. The theoretical developments related to these methods are given in Sections 3 and 4. A review of some of the most significant results published in the literature for normal polymers is presented in Sections 5-12. One section is devoted to the basic principles leading to improvement of the thermal stability of high polymers. The main characteristics of some important thermostable polymers are given. Copolymers and polymer blends which are becoming more and more important in the elaboration of new materials are considered together. Their behaviour is related by a large number of common general principles. Various general monographs and articles have been published on the thermal degradation of high polymers [ 1-11] . More specialized studies are cited in the following Sections. 2. Experimental methods
The use of many different analytical techniques is necessary for the determination of a mechanism of thermal degradation. The main experimental data required are (i) (ii) (iii) (iv)
qualitative and quantitative analysis of the volatiles evolved, characterization of the non-volatile residue, measurement of the rate of volatilization, measurements of the heat evolved or absorbed.
2.1 QUALITATIVE AND QUANTITATIVE CHARACTERIZATION OF VOLATJLES AND RESIDUE
The analysis of volatile products can be performed by gas chromatography, mass spectrometry or a combination of both methods. Gas chromatography, which has become a normal laboratory technique can, in most cases, give complete qualitative and quantitative analysis of a complex mixture. Special techniques involve the breaking of a bulb containing the degraded polymer and the volatiles in the inlet system of References p p . 165--173
4
the chromatograph. This method is very rapid and renders the tedious collection of non-condensable gases with a Toppler pump unnecessary. Infrared spectroscopy can afford a method of qualitative and quantitative analysis in some special cases (analysis of C 0 2 , for instance). Complete characterization of the residue has also to be performed. The number average molecular weight has to be determined if main-chain scission occurs during the degradation. If crosslinks are formed, the weight average molecular weight has to be measured since it is related to the yield of crosslinking. The theory relating M, and the yield of crosslinks is developed in chapter 2, section 1.3. It has a wide range of applicability in the field of thermal degradation but has very seldom been applied to this type of results. Determination of molecular weight by viscometry may lead to important errors since this method is related to the hydrodynamic volume and does not separate branching and chain scission effects. If viscosity measurement is used as a rapid and convenient method to determine the decrease in molecular weight as a function of the conditions of pyrolysis, it is necessary to prove first that branching and crosslinking are not involved by measuring weight and number average M after a significant extent of degradation. Change in molecular weight distribution can be estimated by gel permeation chromatography (GPC). Such determinations have seldom been performed, however, with thermally degraded polymers. Structural modifications often appear in the polymer owing to the breaking or cyclization of the side chain. These can be observed and identified by IR and UV analysis of the degraded residue. Very accurate identifications of some structures can be obtained by fluorescence and phosphorescence emission and excitation spectra. This method has not found wide use in the field of thermal degradation, but it is nevertheless much more selective and sensitive than UV absorption spectroscopy and would yield very useful information when fluorescent or phosphorescent groups are formed. 2.2 MEASUREMENT OF THE VOLATILIZATION OF HEATED SAMPLES
The rate of volatilization can be obtained by different techniques. Either the weight of the sample or the amount of volatile products can be measured as a function of the time of degradation. The temperature may either be maintained constant (isothermal methods) or be varied, generally linearly, as a function of time (programmed temperature methods). The measurement of the weight of the sample at constant temperature is usually performed with an electronic thermobalance and is one of the oldest methods used to investigate the thermal degradation of polymers. The schematic diagram of a thermobalance is given in Fig. 1. Typical examples of diagrams representing weight loss as a function of time are
5
given in Figs. 33 and 34.These diagrams are often interpreted on the basis of the chain reaction kinetic theory which is developed in Section 3. In dynamic thermogravimetric analysis, the same type of thermobalance is used but the degradation temperature is changed as a function of time by means of a programmed heating rate. Typical diagrams are given in Figs. 15,19,39,41 and 42. This method has been reviewed [12]. It allows a very rapid and easy characterization of the thermal degradation of a polymer sample either under vacuum or in an inert atmosphere. The Pt-Pt 10% Rh thermOCOUple leads
-
To recorder
Gas inlet
Quartz chamber Sample crucible
Furnace
transformer
Demodulator
Fig. 1. Schematic diagram of Chevenard recording thermobalance
[lo].
effect of added stabilizers may be very easily checked. Kinetic equations applicable to these programmed degradations are summarized in section 4. Evaluation of the activation energy and order of reaction is possible by application of these methods. The direct determination of the rate of volatilization is possible using a method developed many years ago by Grassie and Melville [ 131. In the original device, the polymer was pyrolysed under vacuum in a glass molecular still. The sample was supported in a copper tray momted on a copper block containing a heating element. A standard Pirani gauge circuit, consisting of a simple Wheatstone bridge, is used for measuring pressure. The pressure is directly related to the amount of gas evolution from the sample. The response of the gauge depends on the nature of the volatiles formed and has to be calibrated before it can be used in degradation experiments. The kinetic equations developed in section 3 apply to the results obtained by this isothermal method. References p p . 165-1 73
6
'1F=@ IL
Tra
I
Receiver
To pumps
Trap
Fig. 2. Layout of TVA apparatus [14]. A, Pyrex glass degradation tube; B, chromel-alumel thermocouple; C, cold water jacket; D, removeable lid; E, F and G, attachment points for Pirani gauge heads.
The same principle of pressure measurement has been applied to programmed temperature degradation [ 141 . The volatilization system has been fitted with a differential condensation apparatus and cold traps in which collection of products is possible. The TVA oven, sample tube and calibration apparatus is represented in Fig. 2. Rather large samples (*25 mg) are used. Differential trapping of the degradation products according to their volatility is then realized according to the scheme given in Fig. 3;
1
.-
14
To pumps-
Fig. 3. Four-line differential condensation TVA system [15]. 1, heated sample; 2, 3, 4, 5 stopcocks (large bore, right-angle type); 6, 7, 8, 9,initial cold traps; 10, 11, 12, 13, Pirani gauge heads; 14, main cold trap; 15, exhaust Pirani gauge head; 16, 17, product collection points.
7
14 is the main cold trap maintained at liquid nitrogen temperature. Four condensation lines, each fitted with a Pirani gauge head, are arranged in parallel. If a cold trap, at some temperature below ambient and above liquid nitrogen temperature, is placed before a Pirani gauge, the system will respond only t o substances which are sufficiently volatile to pass through the trap. It has been found convenient for most applications t o maintain traps 6, 7, 8 and 9 a t O°C, -45OC, -75OC and -lOO°C, respectively. A further Pirani gauge is installed beyond the main trap in order to monitor the system for the passage of gases non-condensable in a liquid nitrogen trap. After completion of the degradation, the volatiles formed can be collected in 16 and 17. Detailed operation of this system has been described, and typical response curves obtained are illustrated in Figs. 29, 36,78, 79 and 80. Each of these methods offers advantages. Dynamic thermogravimetric analysis allows very rapid characterization of the volatilization of polymers but analysis of the evolved products is often difficult owing t o the small amount of pyrolysed sample. Thermal volatilization analysis at programmed temperature offers the possibility of using larger samples and collecting the degradation products according t o their volatility. Although the kinetic parameters can be derived from programmed temperature experiments, isothermal methods are much more appropriate t o detailed study of the degradation kinetics. 2.3 DETERMINATION O F HEAT EFFECTS
Measurement of the heat effect associated with the degradation can be performed by differential thermal analysis (DTA). The degraded sample x y recorder y
_
_
_
axis
~
+*:$ -
x
OXIS
+
v
P) - L
gs
FE
02
~
Sample temperature
Reference thermocouple
material
-Metal block
-
Sample ,/thermocouple
Block thermocouple 1
6 6
Fig. 4. A typical DTA apparatus and DTA curve [ 161. References p p . 165-1 73
8 and inert substance chosen as a reference are heated at a uniform rate. The temperature of the degraded sample is continuously compared with that of an inert sample and any difference in temperature, AT, is recorded. AT is related to the heat absorbed or evolved during the degradation. A schematic diagram is shown in Fig. 4. This method has been reviewed [16,17],and the theoretical aspects are outlined briefly below. Although DTA is more strictly applicable to stirred solutions, it finds most use in the case of solids. Consider a system of two cells in a heating bath at temperature T 3 (Fig. 5). One cell contains
I/
I
DTC
'#
i'.
Fig. 5. Principle of differential the] nal analysis [ 01.
reactants at temperature T, while the other is filled with pure solvent at temperature T2. The temperature of the bath is increased linearly with time. The heat balance in the reactant + solvent system is given by C, dT1 = dH + KT(T3 - Ti)dt
(1)
where C, is the total heat capacity of the reactants, K, is the heat transfer coefficient of the reactant cell, dH is the heat evolved by the reaction and dt is the time interval. In the solvent cell C, dT2 = K,(T3 - 7'2) d t
(2)
where s refers to solvent. If K, = K, = K and C, = C, = C, ,eqns. (1)and (2) give by subtraction dH=C, d(dT)+KATdt
(3)
where AT = T 2- T1. The total heat evolved by the reaction is obtained by integrating between t = 0 and t = 00.
I ATdt=KA, m
AH=C,(ATm - A T o ) + K
0
(4)
9 The first term is equal to zero since AT, = AT, = 0. Since AT as a function of t is recorded during the degradation, the area under the DTA curve is directly proportional to AH. If dH is a function of dWc the weight of the sample undergoing reaction,
where W o , c is the initial weight of active material; that is the weight of the sample at the beginning of the reaction minus the residue at the end of the pyrolysis. By inserting eqn. (3) in eqn. (5),
On integrating between t and 00, we have
If the K term is much larger than the C, term.and T is substituted for t
Equation (6) predicts that the maximum reaction rate should occur approximately at the differential thermal analysis peak if the C, term is omitted. This has been confirmed experimentally in several cases. 2.4 CONCLUSION
Characterization of the thermal stability of macromolecules implies the determination of the rate of volatilization and analysis of the volatile products formed, as well as the determination of the molecular weight of the residue. It must be stressed that main-chain scission involving deterioration of the physical properties of the polymer may occur in some cases without appreciable volatilization. In other cases, some volatilization does not critically limit the use of polymer systems.
3. Kinetics of isothermal depolymerization 3.1 INTRODUCTION
Main chain scission followed by depolymerization is a very frequently observed mechanism of thermal degradation. Kinetic treatments allowing References p p . 165-1 73
10
the determination of the rate parameters in isothermal experiments have therefore been published by several authors [18--211. All these tleatments lead to similar conclusions. One of these will be developed here [ 191. LIST OF SYMBOLS
parameter specifying type of termination. parameter specifying type of termination. r,r(x)reciprocal of the average zip length between initiation and termination or transfer, which is a function of x through R ( x ) in the presence of end group initiation. k I R / k E ,transfer parameter. sample density. rate coefficient for chain scission. rate coefficient for end group initiation. rate coefficient for intermolecular chain transfer. rate coefficient for propagation (unzipping). rate coefficient for termination. smallest degree of polymerization of molecules not volatile in sample. molecular weight of a repeat unit. total number of polymer molecules ZP, (zeroth moment of molecular weight distribution). total number of repeat units in sample ZnP, ; when multiplied by mo it is the sample weight; first moment of molecular weight distribution. number of polymer molecules of degree of polymerization n. number of polymer radicals of degree of polymerization n. R total number of radicals. x , x ( x ) total radical concentration which may be a function of x in the presence of end group initiation. V sample volume. X number-average degree of polymerization.
a,
P
Superscript zero ( O ) indicates initial values; that is, xo is the initial number average degree of polymerization. The experimental measurements of importance in determining the mechanism of depolymerization are the following. (i) The weight, M l m o , of the degraded sample as a function of the time degradation; from this d M ,/dt and M ,/My as a function of time can be obtained. M , and My are the total number of monomer units in the sample at time t and zero time. mo is the weight of a monomeric unit. The variation in the rate of volatilization d M ,/dM? as a function of conversion
11 [1 - ( M I/My) ] strongly depends on the mecnanism of depolymerization and has to be derived from the experimental data. (ii) The. degree of polymerization x, of the sample as a function of the time of degradation; from this, d.x/dt and x/xo as a function of time can be derived. ;yo is the degree of polymerization at t = 0. (iii) The rate of weight loss as a function of molecular weight. All these are related to the kinetic parameters of the reaction. The following are the most important considerations. (a) The type of initiation, at chain end or random. (b) The nature of chain termination, which can be first or second order. The second-order termination proceeds either by combination or disproportionation of the macro-radicals. (c) The zip length (see below). (d) The initial molecular weight. (e) The molecular weight distribution. (f) The possibility of chain transfer. The conclusions obtained by Wall [18] from the kinetic treatment for some extreme cases are given in Fig. 6. They illustrate the strong Extreme cases of chain depolymization theory
Monomer yield
Relative 3 p against conversion
Rate against conversion 1
Random initiation
Large zip
Large
Small ziD
Sma II
x=1OOo
0
100
End initiation
Large zip
Large
Small zip
Small
Fig. 6. Comparison of theoretical results for extreme cases of the depolymerization theory [18].Values of zip shown above curves. All curves for x = 1000 and L = 4. Rate scale for rate curves with zip = 0 multiplied by factor of 100 for random initiation and 50 for end initiation. No transfer. References p p . 165-1 73
12 dependence of the rate of volatilization and decrease of molecular weight on the mechanism of depolymerization. 3.2 BULK POLYMER DEGRADATION
3.2.1 Kinetic rate equations The general kinetic equations will now be developed, and solutions given for the most simple cases. They include all types of initiation and termination cited above for short [ ( l/yo) 4 x o ] and long [ ( l / y o) 9 x o ] zip length in the case of either uniform or random molecular weight distribution. Only the kinetic scheme and final equations will be given. For the complete mathematical development the reader is referred to the work of Boyd [19] and the other references cited. Similar kinetic equations have been suggested by Jellinek [ 201 and by Reich and Stivala r211. - The degradation of a number P , of polymer molecules of degree of polymerization n can be described by the combination of some of the following elementary steps. Initiation
Pn P,
kS
Rr + Rn-r
random scission
kE
R, +R ,
end initiation
-
(9) (10)
Propagation
Intramolecular chain transfer, which can be considered as a special case of reaction (1l), gives fragments larger than monomer.
-
P, + R s
ki
Pr + Rn-r + P s
Termination
R,
kT
Rr +R,
Rr + R s
p,
kT
Pr + Ps
kT
Pr+s
first order
(13)
second-order disproportionation
(14)
second-order combination
(15)
13 The rate of change in concentration of macromolecules P , is given by the difference between the rate of formation by steps (12)--(15) and the rate of disappearance by processes (9), (10) and (12); viz. @n -- - k s ( n - 1)P, - kEP, - k I ( R / V ) ( n- l ) P n
dt
This treatment is valid i f the monomer only is volatile.
The meanings of the various terms on the right-hand side of eqn. (16) are (1st) rate of disappearance by random scission initiation, eqn. (9); (2nd) rate of disappearance by end group initiation, eqn. (10); (3rd) rate of disappearance by transfer initiation, eqn. (12); (4th) rate of formation by transfer, P, in eqn. (12); (5th) rate of formation by termination of a radical by transfer P,, in eqn. (12); (6th) rate of formation by termination reactions, eqns. (13)-(15).
R is the total number of radicals, V is the sample volume, R / V = E,L is the degree of polymerization of the smallest molecule not volatile in the sample and if the termination is first-order,
.R / V if it is a second-order disproportionation, R i R j / Vif it is a second-order recombination. It can be shown that
kI
$ 3nPn n =i
d0
= k I R , -m0
where d o is the density of the sample. Equation (16) can be rearranged to give
+
(18)
kT(Yn
The rate of change of concentration of radicals, R , , is obtained in the same manner and is given by
(-
d-R n - ( 2 k s + k , R ) 2 Pj + k E P , + l .-- kId0 dt j=n+l m0 m
(19) References p p . 165-1 73
14 where
termination, (1for first-order for second-order termination.
P = R/V =
If a steady state concentration of radicals is assumed, then
or
where N is 1 for first-order termination and 2 for second-order termination. Some other useful relations can be derived from the kinetic treatment ~ 9 1 .
1 (a) The zip length - =
kPR 7 kTPR + kldOR/mO probability of propagation prob. of termination + prob. or transfer
(b) The variation in the total number of polymer molecules is
' OD
pn - dMo--( k s dt dt n=2
00
+ ~ I RC) ( n - l ) P n - k E n=2
m
2
n=2
Pn
where M o = ZPn and M I = ZnP,. This equation is valid only for firstorder termination and second-order disproportionation termination Adding eqns. (20) and ( 2 2 ) gives
15 The first two terms on the right-hand side represent the gain in molecules by initiation or transfer, and the second, the loss of molecules by evaporation of P I . (c) The rate of weight loss is obtained in a similar way by multiplying eqn. (18) by n and summing, t o give
The first term represents weight loss due t o termination by R and the second, loss by unzipping. (d) The rate of weight loss as a function of zip length can be obtained if R - R and R in eqn. (24) are eliminated with the aid of eqns. (20) and (23). Then
d"'- - (I-dt
5 ) To __-
[(I + : ) k s + kI,]M1 - (1 + : ) k E M o
(25)
(e) The rate of weight loss as a function of molecular weight is obtained by introducing x = M ,/ M o into eqn. (25). This gives
-1
1 dM1 -]MI dt
+(:
--I
1d.X
--)x'dt
- [(++l)ks
(::)
-+I -
+klfi]=O
These equations must now be simplified according t o the type of initiation and termination, zip length and distribution of molecular weight; the radical concentration will be considered for the same conditions. The various cases are considered separately and the results are summarized in Table 1.
3.2.2 Random chain scission initiation; first-order and disproportionation term inat ion (a) Short zip length ( l / y Q x) In this case R is small, and from eqns (23) and (25)
(28) References p p . 165-1 73
16 TABLE 1 SUMMARY OF DEPOLYMERIZATION BEHAVIOUR AT LONG AND SHORT ZIP LENGTHS 1. Random initiation Zip length
TermiMtion
First-order
Short 1/70 < x o
Initial molecular weight distribution
Weight loss rate
Insensitive to initial dist.
-- = -
Disproportionation
Insensitive to initial dist.
Recombination
Most probable
Mono
Order
Dependence
o f initial mte
on molecular weight
First-order only until
2kS ( : ) M I ;
x no longer 3
dt Early stages
dM1 dl = - 2kS ) (:
First-order only until
MI
x no longer % l / y
(early stages only)
Early stages
_MI _
--4ks($)M1 dt Over fairlv wide range
M_I -d = dt
117
(early stages only)
ksxoMi
First-order, until
x no longer %
117;
fairly wide range
Independent
Independent
Independent
First-order
Proportional to xo
First-order Most probable
!!3-2kSXMI
x changes slowly, not
dt
quite first-order
Proportional to xo
Initial molecular weight distribution
Weight loss rate
Order
Dependence of initial rate on molecular weight
2.
End initiation ~-
Zip length
Termination
_ Mono
dM1
kE1
dt
x 7
_
_
~
MI
Zero-order until x no longer 3 117
MI
First-order
First-order Most probable Short 1/70 e x o
Disproportionation
Recombination
%=-!!EL dt
xo 7
Inversely proportional t o xo Inversely proportional to xo
Inversely
Mono
dMI=-"E'
MI dt x 7 Until x no longer 3 117
x changes, not
Most probable
dM!=-!%L MI dt xO
First-order
Inversely proportional to
First-order (short-zip is maintained, x increases)
Independent
First-order
Independent
1
M
I
- -k E / 2
Most probable
M I dt
Insensitive to initial dist.
5 =dt kEMl
first-order
0
17
Rate constant for initial weight loss
4kS
A = 4kp Y
Molecular weight against time
In x/xo = - 2kS - t Y
x = xo
2ksx0
---=
Rate constant for initial weight loss
Molecular weight against time
MI dt
Introduction of chain transfer
Drops rapidly until x = 1/y
Fig. 9
Drops rapidly until x = 1/y
Fig. 9
1
%do
ksxo
1
('3)
Molcular weight us. co nuersion
1 xo
Relative d.p. always greater than rel. wt Stays constant
Falls slowly
kSt
Molecular weight us. conversion
Introduction of chain transfer
r=o
x - xo = - kE
x=xo
1
-t Y
Fig. 1 2 while l / y < x
Stays constant
Fig. 1 3
_x = - M I
while x
> l/y
Fig. 1 2
xo MY' while 1/y < x
x=xo
Stays constant
Fig. 13
In x/xo = 4kEt
>=(i)
x = xo
Stays constant
x increases rapidly
kE
Mo
R e f e r e n c e s pp. 165-1 73
18 The rate of weight loss is proportional to M , as long as the degree of polymerization is larger than the zip length. From eqns. (28)and (26) dx __ = -(ks + klE)x2 dt
which gives in the integrated form, in the absence of transfer,
1 1 - - kst x x: This equation is not valid in the limiting case l / y = 0. ( b ) Long zip length (l/yS x )
In the case of long zip length, R, is very small and the two last terms in eqn. (16)can be neglected. In the absence of transfer @n = - (n - l ) k s P ,
dt
since kE = 0. Integration of eqn. (31)gives
For an initially monodisperse polymer
dx
-=
dt
0 since
1
-
Y
S x
(33)
and
x = xo.
(34)
Chains depolymerize up to the end and the instantaneous degree of polymerization is equal to the initial degree of polymerization x o . Also it can be shown [2]that
for the most probable distribution. This gives
19 The rate of volatilization is related to the initial molecular distribution through eqn. ( 2 6 ) ;namely,
for monodisperse samples, and
-dt
= -2 k s ~ M 1
(38)
for the most probable distribution. Curves showing x/xo as a function of conversion, and Ml/Mo as a function of x o k , t are given in Figs. 7 and 8 for short and long zip lengths. Data for intermediate zip lengths have been obtained by other methods which will not be discussed here, and are also given in these figures.
Conversion, 1-
M~IMP
xoks t
Fig. 7. Random chain scission initiation, initial “most probable” distribution [ 191. The effect of different ratios of zip length to average degree of polymerization (d.p.), ( l/y)/xo,on the relative d.p., x/xo,plotted against conversion, l-M, IMP.
Fig. 8. Random chain scission, initial “most probable” distribution [ 191. The relative weight remaining, M IIMP, plotted logarithmically against time for a number of ratios of zip length to initial d.p., (1/y)/x0. References p p . 165-1 73
20 Kinetics including transfer and the effect of molecular weight will not be discussed. Some of the conclusions are summarized in Fig. 9*.
xO(ks
+
k * R )t
Fig. 9. Random chain scission initiation, initial “most probable” distribution [ 191. The effect of chain transfer on weight remaining against time. The relative weight remaining, Ml/M:, is plotted logarithmically for three ratios of zip length to initial d.p., (l/y)Ixo. At each zip length ratio, curves forJhree-values of the fraction of the initial weight loss rate due to chain transfer, F = k I R / ( k l R + k s ) , are plotted.
3.2.3 Random chain scission initiation; combination termination
The degradation behaviour in this case cannot be obtained from the preceding equations, which are restricted to first-order termination or second-order disproportionation termination. Another method [ 21 restricted to a “most probable type” initial distribution has shown that in this case, in the absence of transfer
1d.X 1 ---ks+ks( x2 dt 1 + 11x7
)
2
(40)
By integration, eqns. (39)and (40) give
* Many other useful calculated curves are given in Ref [ 21. Attention must, however, be paid to the system of units used.
21 and
s=(;) 2
M,
These equations simplify for limiting behaviour. In the short-zip case (l/y-4 x o ) , we have dx 2ks X (431 dt Y
w, -
4ks M1 Y
at
(44)
In the long-zip case ( l / y % x o ), we have
dx
- =-ksx
dt
2
(45)
_w _1 - - 2ks x M ,
(46)
dt
The variation of M I /My as a function of time is given in Fig. 10.
0
1
2
3 Xokst
4
5
6
Fig. 10. Random chain scission initiation, initial “most probable” distribution [ 191. Weight loss curves for recombination termination. The relative weight remaining, hf~/My, is plotted logarithmically against time for several ratios of zip length to initial d.p., ( l / W x o .
3.2.4 End-group initiation; first-order and disproportionation termination; narrow distribution
(a) Short zip; no transfer There is no decrease in the number of molecules since only the References p p . 165-1 73
22
fragments R , produced by end initiation are evolved from the system after the termination step. Thus W O --0
(47)
dt
and, if M o = M , /x, eqn. (25) becomes
-d M 1 - - kEMl (1+ dt
i)/x
then from eqn. (26)
This solution does not hold for a wide distribution, since complete loss of the shorter molecules may occur even for low zip length and eqn. (47)is not valid.
( b ) Long zip; no transfer
R, molecules are rare and the last two terms of eqn. (16) disappear.
Then
The degree of polymerization x at time t is independent of the initial distribution in all cases since m
From eqn. (51)
dx _ -0 dt
and from eqns. (52) and (26)
1 MI --- -kE Mi dt
23 Generalized treatment for all zip lengths indicates that the molecular weight is constant and the weight loss rate d M ,/dt is first-order with respect t o M , but dependent on the initial mean molecular weight and zip length. If chain transfer is present, the molecular weight decreases rapidly during the early stage of depolymerization, while the rate of weight loss increases, passes through a maximum and then decreases with increasing
't
Convenlon
Conversion
(a)
(b)
Fig. 11. End-group initiation, initial "most probable" distribution [ 191. The effect of chain transfer on (a) the relative rate of weight loss, (dM1/dt)/(dMl /dt)o, against conversion, and on (b) the relative d.p., x/xo, against conversion. Curves are plotted at one value of the ratio of initial zip length to initial d.p., ( l/ro)/xo = 0.01, for several values of the initial transfer parameter times initial d.p., UOX' = ((klz/kg)xo.
Conversion
Fig. 12. End-group initiation, initial monodisperse distribution [19]. The effect of chain transfer on the relative rate of weight loss, (dMl/dt)/ (dM1ldt)o. Curves are plotted at one value of the initial zip length, ll'f = 5 [(l/rO)/xO= 0.00791, for several values of t_he transfer parameter times initial d.p., u0xo = ( k , R / k E ) x o . References p p . 165-1 73
24
2 boxo=
1
x/x"
1
'0
02
06
04
08
1
'0
0.2
04
0.6
Conversion
Conversion
(a)
(b)
08
Fig. 13. End-group initiation, initial "most probable" distribution [ 191. The effect of chain transfer on (a) the relative rate of weight loss, (dM1/dt)/(dM, /dt)o, against conversion, and on (b) the relative d.p., x/xo, against conversion. Curves are plotted at one value of u0xo = ( k l E / k & ) x o = 1 for several values of the ratio o f the initial zip length to initial d.p., (l/To)/x .
conversion. Typical curves are given in Figs. 11-13. The importance of chain transfer is given by
a=
k,R kE
(54)
( c ) Recombination termination For recombination termination, other methods have been used [19]. The results obtained for short zip length are
1dx 1 x dt - 4 k E m _ _l -
-_ _k E 2 M1 dt
25 and for long zip length
1 dx @Yo )@Or0) = kE x dt 4
- --
-- =
0
x = xo
3.3 DEGRADATION OF POLYMER SOLUTIONS
The elementary steps, eqns. ( 9 ) - ( 1 5 ) , and the global kinetic eqn. (16) are of course valid for the degradation of polymer solutions. In this case V is the volume of the solution which does not change with degradation time. For bulk polymer, V is the volume of the polymer sample which usually decreases as degradation proceeds. Therefore, in the preceding discussion
was considered t o be equal t o d o h , . This assumption is not valid in the case of solutions and eqn. (21), for instance, has t o be written as
The same change has to be made in all the kinetic equations in section 3.2 and Table 1 in order to obtain correct expressions for the degradation of polymers in solution. 3.4 DIFFUSION CONTROLLED REACTIONS IN POLYMER DEGRADATION
Diffusion processes often control the rate of elementary steps in polymerization processes. I t is thus not surprising that diffusion plays an important role in the degradation of bulk polymers or even of polymer solutions. This aspect of the kinetics of polymer degradation has been surveyed by Jellinek and Luh [22]. Three types of diffusion controlled reaction have been discussed. (a) A t high temperature the rate of monomer formation from bulk polymer may become so rapid that the rate of diffusion of the monomer from the sample may become rate determining. This has been observed by Jellinek and Kachi [ 231 with polymethylmethacrylate films. In this case References p p . 165-1 73
26 the fraction of the polymer transformed to monomer after a given time is not proportional to the initial weight of the polymer sample. (b) Bimolecular termination may be diffusion controlled. This is observed in photodegradation of bulk polymethylmethacrylate between 160 and 200°C [ 241. An activation energy of 20.5 kcal mole-' was in fact determined by Melville and Cowley for the termination step. The same value was also found by Jellinek and Wang [25], who studied the photolysis of the same polymer in solution. In this case, the concentration of the macroradicals is not necessarily stationary and the rate of monomer formation can be shown to be
where m l is the moles of monomer formed per unit volume at time t. The corresponding equation if the steady-state treatment is applied is
Both equations are identical if the tanh term tends to one. Numerical evaluation has shown that this is usually the case. (c) The random initiation is diffusion controlled. The first step in the degradation is the formation of polymer radicals in solvent cages. Recombination of these radicals is very probable. Escape from the cages is diffusion controlled and is a rare event. The mechanism in these conditions can be formulated as Chain scission
P,,,
kl
( R , .R , )
Depropagation
(R, .Rn)
k2
cage
P,,,
27 Termination k
R+ml A P k
Rm + R,
&=
(Rm. Rn)
&
k3
first-order
(Rm. R , ) Pm
second-order
+Pn
For short zip lengths (l/y< x )
where m l ( t o t a l ) is the moles of monomer formed at time t. For long zip lengths ( l / y > x ) dml (total) ____dt
- k 3 [cagelx
The zip length and the total number of caged radicals have now to be obtained. If the steady-state method can be applied t o radicals in the cage, then
and
If monomer is not eliminated from the system, Jellinek and Kachi [6] assume that after the very early stages k, [ R ] is negligible compared with k, [R] ml(total).Then, if eqns. ( 6 6 ) and (67) are introduced into eqn. (64), for short zip length we have dt where m, is the initial amount of monomeric units bound in the sample and ml(total)the moles of monomer produced at time t. If a steady-state concentration is assumed for R , then for short zip length and bimolecular termination, at the beginning of the reaction
References p p . 165-1 7 3
28
The decrease in molecular weight is given by [ 231
1 x
1 - k,k,
xo
k2
t
For a high zip length, eqn. (66) is substituted into eqn. (65) and
k 3 can be expressed in terms of diffusion coefficients. Diffusion controlled initiation is operative in the degradation of poly-a-methylstyrene solution [ 231 , and occurs probably in most bulk and solution degradation. 4. Determination of kinetic parameters by temperature programmed methods 4.1 THERMOGRAVIMETRIC ANALYSIS
Isothermal methods have generally been used for the study of thermal degradation mechanisms and the determination of kinetic parameters. In recent years, however, dynamic thermogravimetric analysis (TGA) has been developed. In this case, polymer samples are weighed in a
-z
100%
E
c0
::
c L
r
50
1.35
lA0
lo? T P K -'1 145
150
1.55
p
0
Fig. 14. Graph of A, the first derivative of the thermogravimetric curve dwldt, and 0, the weight of reactant W, as a function of reciprocal absolute temperature for the degradation of polythene in vacuum [ 27 I .
29 thermobalance while the temperature is continuously increased at a programmed rate. This method has been reviewed by Reich et al. [21, 261. Dynamic thermogravimetric methods offer many advantages when compared with the usual isothermal methods. The thermal behaviour of a polymer can be characterized rapidly over a wide range of temperature in one experiment using a small amount of sample. When the rate of heating is kept constant, the TGA trace is a simple sigmoidal curve for many polymers (Fig. 14). This of course implies that the degradation mechanism does not change with temperature. If concurrent reactions are occurring, the traces may be very complicated and impossible to analyse. However, if the activation energies of the rate controlling steps are sufficiently different, a sequence of sigmoidal paths may be observed. Each of them can be analysed according to the various methods given below. In favourable cases, determination of reaction order, global activation energy and frequency factor is rapid and easy. Thus, for reactions of the tY Pe A(so1id)
-
B(so1id) + C(gas)
the variation of weight per unit temperature depends on the rate of heating, weight and temperature according t o dW R T = - - - - ( A / R H )e-EIRT W" dT where W is the weight of active material, RH is the rate of heating, T is the temperature, A is the frequency factor, E is the activation energy and n is the reaction order. Some of the various methods developed to analyse the weight loss curve will now be outlined. 4.1.1 Method of Freeman et al. [27, 281
From the experimentally determined curve giving the weight of polymer as a function of 1/T,the reaction rate as a function of 1/T can readily bederived (Fig. 14). If eqn. (72) is applied at two temperatures and the resulting expressions in the logarithmic form are subtracted from each other,
d log R T = n d log W -(E/2.303R)d(l/T)
(73)
A log RT thus varies linearly with d log W for constant intervals d ( l / T ) . The reaction order n is the slope of the line and E can be calculated from the intercept. References p p . 165-1 73
30 4.1.2 Methods using the inflexion point o f the primary trace [ 2 9 , 3 0 ]
An expression for n can be obtained by differentiating eqn. ( 7 2 ) with respect to T . dRT/dT has a zero value at the inflexion point of the primary trace, where
n = ( E / R )(WM/RMT h )
(74)
the subscript M refering t o the value of the various parameters at inflexion. The logarithmic form of eqn. ( 7 2 ) is log Rr = logA + ( E / R )[(WM/RMT&)log W - (1/2.303T)]
(75)
where R , = RH ( R T )and n has been replaced by the expression in eqn. (74). Plotting log R , as a function of ( W M / R M P M log ) W - (1/2303T) gives values for A and E . n is then readily calculated from eqn. ( 7 2 ) . 4.1.3 Method involving more than one thermogram at different heating rates [ 31-33] If the constant rate of heating is changed from run to run and the other conditions are maintained constant, different thermograms are obtained (Fig. 15). From eqn. ( 7 2 ) In R , = In A - E/RT + n ln W
(76)
E and In A + n In W can thus be calculated from a plot of In R , against 1/T, for constant W. Furthermore, at In R , = 0, E/RTo = l n A + n l n
W
(77)
and one can get a value for n. 0-
60-
TemperaturePC)
Fig. 15. Primary thermograms for rn-phenylenediamine-curedhalogenated epoxides at various heating rates [ 261.
31 4.1.4 Graphical estimation of reaction order [ 341
If two thermograms at different heating rates are obtained for the same material, the results can be treated according to the following procedure. From eqn. (72) one can readily derive T2
T2
In RiTX dT
j l n R,TXdTT,
1
TI
T*
= n [ r In WTX dTTI
j In W'TX dT TI
The temperature limits T, and T, are identical for both thermograms, and
x is an arbitrary constant. If x is taken as zero,
n=
T,
(1nWdT-
=,[ l n W ' d T
--
(79)
AW
A R and A are obtained by measuring the shaded areas in Figs. 16 and 17, respectively. Once n is known, A and E are calculated from eqn. (76) by plotting In R, - n In W against 1/T.
rt'
C
i I
1
825
I
850
wo
875
Temperature
I
925
(OK)
Fig. 16. Curves for graphical estimation of A R for Teflon. Heating rates of 6OC min-' and 18OC min-I [ 341. References p p . 165-1 73
32 I
I
I
875
900
I
5
4
3
3
C
2
1
0 I 800 825 850
Temperature
925
(OK)
Fig. 17. Curves for graphical estimation of A w for Teflon. Heating rates of 6OC min-' and 18OC min-' [ 341.
Various other methods have been described and discussed by Reich and Levi [26],and a comparative study of some methods has been published by MacCallum and Tanner [ 351 . 4.2 DIFFERENTIAL THERMAL ANALYSIS
The fundamental equations for differential thermal analysis have been derived in section 2; namely,
w
W o ,C
=---(? AT
T
These equations are based on the assumptions that the heat evolved in a small temperature interval is directly proportional t o the weight of polymer reacting during that temperature interval (eqn. ( 5 ) , p. 9) and that the heat capacity terms are negligible compared with the other terms (eqns. (7) and (S), p. 9). If eqns. ( S O ) and (81) are substituted into eqn. (72), it is possible to convert the expressions used in thermogravimetric analysis into those for differential thermal analysis [ 36, 371 . The activation energy and order of reaction can then be obtained by similar methods.
33 4.2.1 Method of Freeman and Carroll [ 281
If eqns. (80) and (81) are substituted into eqn. (73),
A log(dT) = n A log 6 - (E/2.3R) A ( l / T )
(82)
If A (1/T)is maintained constant, a plot of A log (d 2') against d log 6 should give a straight line. The slope of this line is n and its intercept gives the value of E . 4.2.2 Other methods It can be shown [ 361 that
and at the maximum value of d W,/dT
n = ( i / A T ) , (l/T&)E/R = K(E/R)
(84)
Once n is known, E is calculated from the plot of log ( A 2') against ( K log a" - 1/2.3T) + K log ( W,,,/AT). Other methods have been reviewed by Reich [36]. 5. Polyolefins and natural rubber 5.1 POLYETHYLENE AND POLYPROPYLENE
Early work on polyethylene and polypropylene has been reviewed by Madorsky [ 381 and Winslow and Hawkins [ 391. Initiation by random scission or at weak links has been proposed. Since little monomer is evolved, chain depolymerization seems to be of minimal importance. The low molecular weight products formed are the result of inter- or intramolecular free radical transfer. The effect of structure on the mechanism of thermal decomposition of saturated hydrocarbon polymers has been studied more recently by Wall and Straus [ 401 . Linear and branched polyethylene, polypropylene and various copolymers have been investigated and the rates of volatilization compared. The linear materials behaved according to the theory of random degradation (Fig. 18) for l / y + 0, while the branched materials did not. The greater the branching, the greater was the rate of decomposition and References p p . 165-1 73
34
o Branched polyethylene
12
0
Linear polyethylene
lheory - Random theory
B Q
! a2 S
n 0
20
40 volatilization (%)
60
00
Fig. 18. Comparison of the rates of volatilization at 4OO0C for linear and for branched polyethylenes with random theory [ 4 0 J .
the more it was at variance with random theory. (The branches have, however, to be longer than one carbon atom.) No quantitative theory could be presented by the authors at that time. They proposed, however, that polymer branching enhances intramolecular transfer at the expense of intermolecular transfer. The decrease in thermal stability with branching is illustrated in Fig. 19, which shows the rate of weight loss as a function of temperature in temperature programmed experiments [ 391.
0 320
--
CJ
d o . 340
a 360
A
360
0 ;
I
0
400 420 Temperature ( O C )
I
I
1
440
460
480
500
Fig. 19. Effect of branching on the thermal stability of various polyolefins [39].
35
0
100
200
300
Temperature
400
500
("C)
Fig. 20. Differential thermal analysis curves for low-pressure polyethylene Hizex 5000 [41]. Upper curve, in air; lower curve, in a nitrogen atmosphere.
Low and high pressure polyethylene were recently compared by thermal and thermogravimetric analysis [41]. The differential thermal analysis curve for low pressure polyethylene is given in Fig. 20. The first endotherm corresponds t o melting and the second to thermal decomposition. The two small exotherms correspond to oxidation. Thermogravimetric analysis (Fig. 21) shows that with high pressure polyethylene, decomposition begins at a higher temperature (2OoC) than with low pressure polyethylene. Activation energies of 61-74 kcal mole- were derived.
Temperature
("C)
Fig. 21. Thermogravimetric analysis curves for polyethylenes in a nitrogen atmosphere 0 , Sumikathene F-70-6. [41]. 0 , Hizex 7000;@, Sumikathene MF-40; References p p . 165-1 73
36 The volatile products formed during degradation of polyethylene have been analysed by mass spectrometry by Madorsky [ 381 . Gas chromatographic analysis of the low molecular weight volatilization products was performed later by Moisev et al. [42, 431, and still more recently by Tsuchiya and Sumi [44]. The very efficient separation and quantitative determination performed by these authors is shown in Fig. 22.
Pyrolysis temperature
("C)
. 22. Decomposition products of polyethylene [ 4 4 ] .
The formation of products is explained on the basis of a free radical mechanism. Initiation consists of preferential scission of weak bonds or ordinary C-C bonds. The weak bonds may include oxygen atoms; carbon-carbon bonds in the 0 position to double bonds or adjacent to tertiary carbons may also be involved. The mechanism proposed is Initiation
R-R
__+
-
2FC
Propagation
R
R,. + CH,=CH,
37
Intramolecular transfer followed by a decomposition reaction Ri
-----*
R24H-CH2-R3
R; + CH2=CH-CH2-R, R2-CH=CH2 + R;
(87) (88)
Intermolecular transfer followed by a decomposition reaction
-
R4-CH2-RS
R4--C'H-RS Termination R,* + R; R;+R,
+R'
+
R4-6H-R5
+RH
R4-CH=CH2 + R i
(89) (90)
R-CH=CH2 + R,H
(91)
R,-R,
(92)
Propagation competes with transfer and their relative importance depends on temperature. The relative amounts of different hydrocarbons produced can be discussed in terms of +,hedifferent possibilities for intramolecular transfer. Isomerization of a free valency on a primary carbon t o the fifth carbon should be very favourable for geometrical reasons; namely,
This explains why propane and 1-hexene are among the most abundant decomposition products. Propene can be produced by two different routes: intramolecular transfer t o the second carbon, and scission of the C-C bond in the 0 position t o one of the terminal double bonds formed during heating, eqn. ( 9 1 ) . Isobutene can be produced at the sites of unsaturation of the type
which are present in polyethylene due to scission of the C-C bonds in the fl position to the double bond. It can also be produced by abstraction of a hydrogen atom at branch sites, followed by scission of the C-C bonds in the position. The authors conclude that the predominant process for the formation of volatiles is intramolecular transfer in radicals in which local coiling plays an important part in determining the relative quantities of each product.
References p p . 165-1 73
38 The changes in molecular weight during pyrolysis were first studied by Oakes and Richards [ 4 5 ] . They found that the molecular weight of branched polyethylene decreased above 290°C whereas weight loss was negligible up t o 370°C. This was confirmed by Wall et al. [46]. These observations are in agreement with rupture at weak links. These authors also demonstrated that hydrogen transfer during pyrolysis of branched polyethylene occurs by three different routes, leading t o three types of unsaturation which were identified by infrared analysis:
R-&CH,+R' I R
-
R-C=CH2 I R
+&
/ R-CH,--CH=CH-R giCH2-CH'-CH-R -'*' R R
CH,=CH-CH-R
-
I
+R
+ li'
R RCH=CH,
+ RCHi
Vinyl-type double bonds are indeed more numerous in polymers containing few branches in agreement with this mechanism. A broad range of activation energies [ 391 depending on the conversion, initial molecular weight and the method used to measure the extent of 99 I
Z
70 -
$
60-
0,
!j 505 40 30V
20 10 -
Chain length, I
Fig. 23. Comparison of the experimental and theoretical chain length distributions for ) theoretical the degraded polymer for various degrees of degradation [47 1. (curves.
39 TABLE 2 THERMAL DECOMPOSITION PRODUCTS O F POLYPROPYLENE [ 50 1 36OoC
4OO0C
Wt. %
Mole%
Wt.%
Mole%
Wt. %
Mole%
of
of
of
of
of
of
polymer
Methane Ethane Propane Propene Isobutene Butane 2-Meth yl-l-butene 1-Pentene Pentane 2-Pentene,cis and trans 2-Meth ylpentane 2-Methyl-l- pentene Peak h 2,4-Dimethylpentane 2,4-Dimethyl-l-pentene 4-Methylheptane 2,4-Dimethyl-l-heptene Peak m Peak n Peak o 4,6-Dimethylnonane, threo form 4,6-Dimethylnonane, erythro form 2,4,6-Trimethyl-lnonene, threo form 2,4,6-Trimethyl-1nonene, erythro form Total volatiles analysed 100 residue wt. %
38OoC
volatiles polymer
0.0055 0.0057 0.0021 0.0296 0.0083
7.7 4.2 1.1 15.7 3.3
0.102
31.6
0.0066 0.079
1.7 20.9
volatiles polymer
0.021 0.030
7.0 5.4
0.131 0.069 0.001 0.002
13.2 6.6 0.09 0.14
0.421 0.002 0.017 0.249 0.003 0.004 0.013 0.052 0.26 0.005 0.007 0.006
volatiles
31.5 0.12 1.1 16.0 0.2 0.22 0.72 2.5 11.2 0.20 0.25 0.23
0.057 0.13 0.078 0.83 0.16 0.004 0.010 0.008 1.62 0.015 0.074 1.19 0.029 0.032 0.089 0.24 2.20 0.059 0.098 0.044
3.9 4.8 1.9 21.4 3.0 0.07 0.15 0.12 24.3 0.23 0.93 15.4 0.4 0.34 0.98 2.3 18.9 0.5 0.75 0.35
0.0019 0.013 0.040
0.43 2.6 7.1
0.0039
0.55
0.011
0.38
0.042
0.29
0.0046
0.66
0.014
0.49
0.052
0.36
0.0130
1.73
0.040
1.3
0.055
0.36
0.0134 0.326 2.7
1.78 100
0.045 1.41 4.4
1.4 100
0.066 7.05 19.8
0.44 100
degradation (weight loss or molecular weight measurements) were reported [39]. Early work on polypropylene has also been reviewed by Madorsky [ 381 and Winslow and Hawkins [39]. Its pyrolysis also involves random chain scission. A reduction in molecular weight and a change in mechanical properties appear in the range 230-250°C, but volatilization is unimportant below 300°C. The changes in molecular weight during pyrolysis have been thoroughly studied by Davis et al. [ 471. A decrease in the mean degree of polymerization and a narrowing of the distribution are observed. The results are given in Fig. 23. They are in good agreement with a mechanism of degradation involving random scission and transfer. References p p . 165-1 73
40
s
vI X Sy-u
s vI I
zs u-u
+
u
s
It
z u-
zf s y-u
.s u
/
U
.p
I
s ‘Y zs 1
p-u
T
I
N
t
Z’
' y-u
7
Scheme 1. The thermal decomposition of polypropylene [ 50 1.
41 The broad initial distribution characterized by a high value of M , / M n tends to become random [(M, / M n ) = 21 as the degradation proceeds. Analysis of the volatile degradation products has been performed by Moiseev [42], Bailey and Lieske [48] and van Schooten and Evenhuis [49] . Later, very comprehensive analytical data, including separation of saturated and unsaturated hydrocarbons, were published by Tsuchiya and Sumi [50]. The results obtained are summarized in Table 2. The kinetic scheme proposed by the authors is presented in Scheme 1. The decomposition products resulting from intramolecular transfer in radicals I and I1 from this scheme are given in Table 3. The experimental results indicate that radical transfer takes place mainly at the tertiary carbons. TABLE 3 DECOMPOSITION PRODUCTS RESULTING FROM INTRAMOLECULAR RADICAL TRANSFER AT 4OO0C [ 5 0 ] From
Transfer to nth carbon
Secondary radical
-cH-cH,--CH I
CH3
I
CH3
Primary radical
-CH-CH,
I
CH3
H-CH,
-C
I
CH3
n
Decomposition product
Amount of product, mole % o f vola t iles
3 3
Ethane 2-Methyl-1-pentene
4.8 15.4
5
Pentane
24.3
5
7 7 9
2,4-Dimethyl-l-heptene 18.9 4-Methylheptane 2.3 2,4,6-Trimethyl-l-nonene 0.80 4,6-Dimethylnonane 0.65
4 4
Propane 2,4 -Dimethyl-1-pentene
6 6
2-Methylpentane 0.93 2,4,6-Trimethyl-l-heptene a 2,4-Dimethylheptane <0.1
8
1.9 0.98
Not determined. 5.2 POLYISOBUTENE
In this polymer, every alternate carbon of the chain is quaternary and no reactive hydrogen atoms are present. Formation of radicals by scission of the main chain results in monomer formation by a chain depolymerization [51,52, 54, 551, but the polymer is not quantitatively converted into monomer as happens with polymethylmethacrylate. A range of products from C4 t o C2, is also evolved 152, 531. References p p . 165-1 7 3
42 McIntyre et al. [ 541 have examined the rate versus percentage degradation curves for series of polyisobutene fractions. All the samples gave the same behaviour (the rate decreasing with increasing conversion), except the highest molecular weight fractions for which a maximum is observed in the curve. This was, however, not confirmed by later thermal volatilization analysis [55]. All the samples show a decrease in the rate of volatilization as a function of percent degradation, and no indication of any dependence on the initial molecular weight could be found. Random initiation followed by depropagation competing with inter- and intramolecular transfer was proposed by these authors. This intramolecular transfer was further investigated by Tsuchiya and Sumi [ 561 by means of a careful analysis of the volatile products formed. These authors have shown that the amount of products formed by radical transfer to primary carbon atoms was much greater than that formed by transfer to secondary carbon atoms. It is suggested that the low reactivity of the hydrogen atoms attached to secondary carbons is due to the steric effect of the methyl groups.
5.3 POLY-4-METHYLPENTENE-1
A comprehensive study of the thermal degradation of poly-4-methylpentene-1 has been reported by Reginato [57]. It includes the determination of the nature of the volatile products, their rate of evolution and the variation of the molecular weight of the polymer residue with the extent of volatilization. The volatiles formed are isobutene, propane, isobutane, 4-methyl pentene-1, isopentane, 2-3-dimethylbutane, n-pentane and propene. The heavy fraction contains mainly branched saturated hydrocarbons of the general formula C, H, and C, 3HZ and branched unsaturated hydrocarbons C12Hz4, C14Hz8, C , , H , , and C 1 8 H J 6 . Isobutene and propane are the main components of the volatile products. According to the author inter- and intramolecular transfer of radicals to tertiary hydrogen dominates the degradation of this polymer and explains the formation of most of the compounds evolved (Scheme 2). If the tertiary hydrogen is abstracted from the backbone, scission of a C - C bond in a 0 position to the radical will occur. This will lead to a decrease in molecular weight if the C - C bond is situated in the main chain. The reactions subsequent to the abstraction of a tertiary hydrogen on the substituent chain are given in Scheme 3. Radical VII could also undergo a scission. The activation energy for the loss of weight was found to be 53.5 kcal mole-’. The molecular weight of the polymer decreases sharply at the beginning of the reaction, and then more slowly. The rapid decrease is assigned to the breaking of abnormal “weak” structures distributed at random dong
* * *
-CH-CH2-CH-CH2-CHI I I CH2 I (732 y 2 CH CH CH /\
/ \
/\
H3C CH3 H3C CH3 H3C CH3
-
*
- -R.
*
43 (2) (2) -CH~CH2~-CH2-CH-
I I ‘ CH2 I (1)--t-CH2 CH
/\
CH
/\
I
--
*
+ RH
YH2 CH
/\
H3C CH3 H3C CH3 H3C CH3
Scheme 2 [Ref. 571.
Scheme 3 [Ref. 57 I.
References p p . 165-1 73
44 the chain. Its importance vanes according t o the previous history of the polymer sample. 5.4 NATURAL RUBBER AND POLYBUTADIENE
Reviews on the degradation of these polymers have been presented by Madorsky [ 381 and Bevilacqua [ 581 . Yields of volatile products reported by different workers differ very much since such yields often strongly depend on the experimental techniques used to isolate the products. In fact diffusion of these gaseous products and heat transfer rates are often determining factors and are influenced by sample size and purity. Up to 200°C, solid rubber is stable; volatilization is negligeable. Above 300"C, degradation is very rapid; complete volatilization occurs in 30 min at 400°C. In the interval 200-3OO0C, low molecular weight materials are formed and the residual rubber becomes progressively insoluble and intractable. Its structure has not been studied in detail but could involve condensed polycyclic structures formed by cyclization. If rubber is preheated in the region 200-300°C, the yield of monomer obtained by pyrolysis at higher temperatures becomes lower and lower. Since an appreciable fraction of molecular weight about 600 is obtained by slow distillation after pyrolysis in the temperature range 260-4OO0C, random scission and intermolecular transfer are also operative. Polybutadiene was shown to behave in rather a similar manner. 6. Polystyrenes and polyvinylpyridine 6.1 POLYSTYRENE
6.1.1 Molecular weight decrease and volatile formation above 3OO0C
Early work on the degradation of polystyrene has been reviewed by Madorsky [ 5 9 ] . When polystyrene is heated above 300°C, volatile products are formed. They consist mainly of monomer (about 45%) and decreasing amounts of dimer, trimer, tetramer and traces of pentamer. A sharp decrease in the molecular weight followed by a much slower degradation reaction is observed. The mechanism of formation of volatiles has been clearly demonstrated. Jellinek and Spencer [60] have proved the radical nature of the production of volatiles by studying the degradation of polystyrene in naphthalene and tetralin solutions. The formation of volatiles is, in fact, completely inhibited in the last solvent which contains a-methylenic hydrogen atoms which are able t o deactivate free radicals. The rate of volatilization has also been shown t o be proportional t o the number of chain ends [61(a)], a result confirmed by Cameron [61(b)]. The
45 formation of volatile products is thus a free radical process initiated at chain ends; the dimers, trimers and tetramers are formed by intramolecular transfer. The importance of transfer is shown by experiments on poly-a-deuterostyrene [62]. The monomer yield for this polymer is 70% by weight of total volatiles, while it is only 42%for the undeuterated polymer. This can be accoimted for by an isotope effect in intramolecular transfer. The relative importance of inter- and intramolecular transfer has been discussed recently by Cameron and McWalter [63, 641. A theoretical treatment was developed which showed that a propagation mechanism comprising only intermolecular transfer, along with unzipping, would give a monomer/non-monomer ratio which is at least a hundred times larger than that observed, and would vary, contrary t o observation, with the extent of degradation. Intramolecular transfer is thus the main source of volatile low polymer, but it has only a small effect on molecular weight. Intermolecular transfer, however, produces little volatile material but causes a decrease in molecular weight of the residue. If it is thus assumed that volatiles are formed only by intramolecular transfer, a total zip length of 3.3 is calculated. The nature of the chain termination has also been discussed; it is assumed to be unimolecular by some authors and bimolecular by others [65]. The mechanism of main chain scission has, on the contrary, led to much controversy. The rapid initial decrease in molecular weight was assigned by Jellinek [66] t o the scission of a limited number of weak links distributed at random in the polymer. According t o this author, a plot of the inverse of molecular weight as a function of time, which would have to be linear in the case of random degradation, shows strong departure from linearity. Also, the molecular weight distribution of the degraded material was narrower than that produced by a random degradation. Similar results were obtained by Grassie and Kerr [ 671 , but a different interpretation was given. When the molecular weight changes are plotted against the extent of volatilization at various temperatures, the curves obtained are almost superimposable [67]. From this, Grassie and Kerr deduced that weak links are present in the polymer; their decomposition corresponds to the initial steep decrease in molecular weight. The later part of degradation is due t o chain end initiation followed by unzipping, with a zip length of the order of the molecular chain length. After the initial decrease in molecular weight, the curves are almost linear and appear to lie between the horizontal and the diagonal running to zero molecular weight. A third, unified mechanism for volatile formation and molecular weight decrease was proposed by Gordon [ 681 . Assuming chain end initiation, intermolecular transfer, and bimolecular termination, mathematical expressions were derived for the molecular weight and relative rate of volatilization as a function of percent volatilization. These expressions fit the experimental results obtained by Grassie and References p p . 165-1 7 3
46
20
40 % Volatilization
60
80
Fig. 24. Application of Gordon’s theory (continuous line) to Grassie and Kerr’s experimental points for the molecular weight changes during depolymerization of polystyrene [69].
K e n [67] very well (Figs. 24 and 25). Madorsky and co-workers have also made an extensive study of polystyrene degradation (see Ref. 59)’ and agree with Gordon’s degradation mechanism. A further argument against the weak link theory of Jellinek can be deduced from the results of Wall [70] on deuteropolystyrene. They, in fact, show that the initial molecular weight decrease is reduced fifty percent by deuterium substitution. This can be explained if transfer is
I
1
20
I
40
60
I
80
% Volatilization
Fig. 25. Application of Gordon’s theory (continuous line) to Grassie and Kerr’s experimental points for rate changes during depolymerization of polystyrene [ 691.
47 responsible for part or all of the molecular weight decrease. Since such different mechanisms were proposed on the basis of the earlier experimental results, later work has been mainly devoted to obtaining data t o test one of the above mechanisms for molecular weight decrease, that is scission at weak links, random scission with intermolecular transfer or a combination of both. The best evidence against the mechanism suggested by Gordon came from a comparison of the degradation of polystyrene in bulk and in naphthalene or tetralin solution [71, 721. It was found that tetralin inhibits volatile formation, whereas the initial steep decrease in molecular weight remains unchanged. It is clear that a unique mechanism, involving chain transfer t o explain volatilization and main chain scission, is not in agreement with these observations. The results obtained with tetralin solution can, however, be interpreted by both weak-link theory and random scission for molecular weight decrease. Further evidence will be discussed in section 6.12. 6.1.2 Degradation o f polystyrene without volatile formation (below 300°C) In order t o obtain further evidence on the mechanism of thermal degradation of polystyrene, several workers have recently studied the decrease in molecular weight occumng below 300°C. In this temperature range, in fact, volatile formation is negligible and it was hoped that the degradation kinetics would be easier t o interpret. If no volatiles are evolved, the variation in the number average degree of polymerization for random initiation is given by [ 731 (y
1
1
x
xo
= - - -- = k t
(93)
where x and xo are the number average degrees of polymerization at time t and zero time, respectively, and k is a first-order rate coefficient. If the polymer contains weak links which break rapidly at the beginning of degradation, eqn. (93)becomes
1 1 a=---- - @ + k t x
xo
(94)
The degradation of samples of non-radical polystyrene has been studied by different workers [73-761, all of whom reported linear plots passing through the origin of a as a function of t. This proves that weak links are absent in this polymer. The molecular weight distribution at various stages in the degradation was determined by Nakajima et al. [76]. The initial polymer was shown t o have a logarithmic normal molecular weight distribution. The molecular weight distribution of the degraded polymer could be explained on the basis of a mechanism of random References pp. 165-1 73
48 scission. On the contrary, conventional (radical) polystyrene, on degradation gave values of 01 which showed an appreciable ordinate intercept when plotted according t o eqn. (94)(Fig. 26). Degradation of these polymers is thus due t o the superposition of two mechanisms: one, very rapid, involves scission at weak links, and the other, much slower, is characterized by the rate coefficient k. The scissions per chain link for a intercept 0 corresponds to about 5 x polymer having an initial molecular weight of 515,000. This number of
I
0
I
20
I
4.0 6.0 Tirne(h)
0.0
1
l0.0
Fig. 26. Degree of degradation, a, against time of heating at 287OC for TPS polymers [73]. 0 , TPS/1; x TPS/2; +, TPS/3; A, TPS/4; D, TPS/5.
weak links is sufficient t o cause an initial drop in molecular weight from 515,000 to 341,000 in that polymer sample. The results have demonstrated that weak links are absent in isotactic polystyrene but present in free-radical produced polystyrene. Two problems remain. What is the nature of the weak links and what is the mechanism of chain breaking corresponding either t o the intercept or t o the normal scission process ( k t ) ? The second problem has been partly solved by performing the degradation in the presence of a large excess of 1,4-diaminoanthraquinone(DAA) [741 . The molecular weight decrease is not affected by this inhibitor; the values of h and /3 are both unchanged. If the intercept /3 was due to chain end initiated rupture, followed by random transfer reaction, and subsequent scission at a new radical centre, 0 would be decreased by the addition of DAA. It thus seems most
49 probable that the weak links are distributed at random along the polymer chain. The absence of any effect of DAA on the slower phase of the degradation shows that, in this also, the scission of bonds occurs at random and is not due t o chain end initiation followed by transfer. The rate of bond scission, however, exhibits a direct dependence on the initial molecular weight. An inverse dependence would be expected in the case of chain end initiation followed by transfer, but a direct proportionality is not consistent with random scission. The effect of molecular weight on the rate of main chain scission has not been explained. The structure of weak links has been discussed [ 741 . Three possibilities have been considered: head-to-head bonds, branch points and intramolecular unsaturation. (a) Head-to-head bonds may be formed during the polymerization, either by combination of the radicals or by abnormal addition during polymerization. Copolymers of styrene and stilbene contain such links: -CH2
Ph Ph Ph I l l +H-CH--CH-CH
2-
and have been synthetized and degraded [74]. The parameter /3 in eqn. (94)is the same for the homo- and copolymers, but the slower phase of the degradation is markedly increased with the copolymer. Copolymers containing -CH2 --CHPh-CHPh-CH, - were prepared by Richards and Salter [ 771 by anionic polymerization. According to these workers, the thermal rupture of the CHPh-CHPh links below 300°C produces radicals which depropagate to give monomer. The zip length was calculated to be about 1.4 monomers per initiation step. Decrease in molecular weight corresponding t o the number of weak links contained in the polymer was also observed. The importance of chain transfer was demonstrated by the same authors by degrading below 300°C a mixture of anionic polystyrene containing weak head-to-head links and “normal” C-14 labelled polystyrene [78]. A t a temperature at which only the polystyrene containing weak links degrades, inactive styrene will be produced in the absence of chain transfer. If, however, chain transfer is appreciable, both types of polymer molecules will be susceptible to random attack and radioactive monomer will be produced. Measurement of the activity of the monomer in the distillate showed that, with a kinetic chain length of about 3 monomer units, 1.2 chain transfers occur per radical. (b) It is suspected that branch points are formed at high extents of free radical polymerization. The value of /3 is, however, the same for polystyrene obtained at 12.5% and 60% conversion [74]. In this case also, the slower stage of degradation is faster with the branched polymer. (c) Intramolecular unsaturation has been determined by McNeill and Makhdumi [79] t o be approximately 1.5 double bonds per 1000 References p p . 165-1 7 3
50 monomer units in polystyrenes prepared at 100°C with benzoylperoxide as initiator. This is ten times larger than the concentration of weak links determined by use of eqn. (94) [ 7 4 ] . The intercept 0 is thus not associated with main chain unsaturation. This can, however, contribute to the slow stage of the degradation. In view of the preceding results, it seemed reasonable t o Cameron and Kerr [74] t o assign the weak links to peroxy structures incorporated in the chain during the polymerization. 6.1.3 Conclusion
The preceding discussion shows that, despite the large number of experiments that have been performed t o elucidate the mechanism of the thermal degradation of polystyrene, many aspects of the problem are not definitively resolved. It seems clearly established that volatilization is a free radical process initiated at chain ends; transfer is responsible for the formation of dimer, trimer, etc. The mechanism of main chain scission is less clear. It seems nevertheless probable that weak links associated with peroxy structures in the chain are present in the polymers prepared by free radical mechanism. They would break very rapidly at the onset of heating. Further chain scission is probably due t o random breaking of the chain. This random breaking is accelerated if head-to-head, branch chains or main chain unsaturation are present. Transfer occurs but is not very important. 6.2
POLYa-METHYLSTYRENE
Polya-methylstyrene and polymethylmethacrylate degradations show strong similarities. Thus, both polymers depolymerize at relatively low temperatures. Almost pure monomer is obtained as volatile product. Depolymerization of polymethylmethacrylate, however, is initiated at unsaturated chain ends below 250°C, whereas polya-methylstyrene undergoes mainly random-chain scission. Degradation of solid polya-methylstyrene was studied by Brown and Wall [80] and Jellinek and Kachi [81]. Depolymerization in solution was investigated by Bywater et al. [82,83] and Jellinek and Luh [84]. For solutions, the rate of monomer production, expressed in monomer concentration per unit time, is first-order in polymer concentration and directly proportional t o the molecular weight up t o an initial molecular weight of 6.5 x l o 5 . The sharp molecular weight distribution of anionic polymers was retained after 9% conversion [85]. These results could be accounted for by assuming random initiation, no transfer and a kinetic chain length high compared with the molecular chain length of the polymer. The degradation of polya-methylstyrene in solution was reinvestigated by Jellinek and Luh [84] with special emphasis on the effect of solvent
51 viscosity on the kinetics of depolymerization. The rate of monomer formation was, in fact, shown to be diffusion controlled. The rate determining step after a potential chain scission has taken place to form an encounter pair in a cage is the diffusion of polymer radicals out of cages. Kinetic equations including this diffusion controlled step have been developed in section 3.3. However, this cage effect does not change the formal kinetics nor the reaction order. Only some of the rate coefficients
Fig. 27. Degree of degradation, l/mn,t - 1/FPn,oas a function of time at 24OoC ~341.
have a different meaning and include the solvent viscosity. A monodisperse polymer with an initial number average molecular weight of 7.81 x 10' was studied. The molecular weight was found to vary according to the relation (l/x) - (l/xo)= k s t a t the beginning of the degradation and then to remain constant (Fig. 27). For the first stage the results are in agreement with random initiation, kinetic chain length less than the molecular chain length, and termination by disproportionation. Since the monomer concentration in solution becomes appreciable, termination readily occurs between radical and monomer. This elementary step is thus first order in macro-radicals and in residual monomer. The rate of monomer production expressed in total number of moles is then proportional to M ,/(My- M I ). When the polymerization degree x becomes less than the kinetic chain length, the molecular weight remains References p p . 165-1 73
52
constant and the rate of total monomer produced is proportional to M I (Fig. 27). The rate of monomer production is, however, strongly dependent on the viscosity of the medium (Fig. 28). The rate is in fact, directly proportional t o the reciprocal of the solvent viscosity, indicating that the over-all reaction is diffusion controlled. All the data are thus in agreement with the kinetics developed in section 3.
Fig. 28. Rate of monomer formation against moles of monomer produced at 24OoC ~ 4 1 .
The same mechanism was shown to be operative for films: random initiation and depolymerization with l/y > x or l / y < x [80,811. The kinetic chain length is, however, greater for solutions than for films at the same temperature. In view of the data obtained with solutions, diffusion of polymer radicals from cages has also t o be considered for polymers in the bulk phase [84]. 6.3 POLYVINYLPYRIDINE AND ITS COPPER CHELATE
A rapid initial drop in molecular weight followed by a slower decrease is observed when polyvinylpyridine is heated at 250°C [ 851 . This behaviour is qualitatively similar to that of polystyrene. Scission of weak links may be involved in the fast decay of molecular weight, but random scission may also explain the shape of the curve. As in the case of polystyrene, the mechanistic problem is very complex and many more experiments are needed t o solve it. Chelation of 2- and 4-polyvinylpyridine makes those polymers less heat-resistant; chain scissions already occur at 100°C while the uncomplexed polymer suffers no damage at this temperature. On heating, a change in the absorption spectrum of 2-polyvinylpyridine copper chelate dissolved in 1M HC1 is observed; a new peak is formed at
53 420 nm, the absorbance of which increases linearly with heating time. Most probably a redox reaction is responsible for the initiation of this degradation. Such a redox reaction has been identified in the polymerization of vinylpyridine in the presence of cupric acetate. A one-electron transfer from Cuz ion t o vinylpyridine in a comple-: including two monomers per metal ion has been shown to initiate the polymerization [861* +
7. Polymethacrylates and polyacrylates 7.1 POLYMETHYLMETHACRYLATE
The degradation behaviour of polymethylmethacrylate is easily characterized by thermal volatilization analysis [87] (Fig. 29). Monomer is obtained in very high yield in all cases. A polymer sample prepared by a free radical reaction undergoes a rapid depolymerization at about 275°C as indicated by the first peak. The second peak, situated between 350 and 4OO0C, corresponds t o a second mode of initiation of chain depolymerization. For samples prepared by anionic polymerization, the first peak is not observed. Depolymerization of the whole sample occurs above 350°C. The thermal degradation of polymethylmethacrylate was investigated many years ago by isothermal methods [ 8 8 , 891. The two mechanisms of chain depolymerization were already identified at that time and analysed. At temperatures below 27OoC, the reaction is initiated at the double bonds situated at chain ends and formed by radical disproportionation
Fig. 29. Comparison of TVA thermograms for high and low molecular weight polymethylmethacrylate samples prepared by an anionic mechanism with the thermogram for a low molecular weight free radical sample [ 871.Dotted line, polymer = 1,500,000;full line, polymer E, M, = 60,000; dashed line, free radical polymer C, Mn = 20,000.
D,Fn
References p p . 165-1 7 3
54 during the polymerization. This type of chain end is not produced during )anionic polymerization and therefore the first peak is absent in the thermogram of anionic polymers (Fig. 29). End initiation and a long zip length characterize the degradation below 270°C. This has been proved by different methods. If the molecular weight of the polymer residue is plotted as a function of the percentage degradation to monomer (Fig. 30) it is found to be
% Degradation
to nwnomer
Fig. 30. Effect of degradation on the molecular weight of polymethylmethacrylate of various initial molecular weights. 0, 44,000;8 94,000;8, 179,000;a, 650,000;0, 725,000 [ 891.
independent of the percentage degradation for low molecular weight polymers; this means that the zip length is larger than the mean degree of polymerization (see Table 1,pp. 16-17). For polymers of higher molecular weight, the experimental points lie on the diagonal. This diagonal describes a situation in which each molecule that has been affected by degradation is represented in the residue by one involatile fragment. The dependence of the initial rate of degradation on molecular weight ia another proof of end initiation. If initiation is random, the number of possible initiation sites is independent of molecular weight; if the zip length l/-y is larger than the degree of polymerization x the over-all rate of volatilization is thus proportional t o x and, according t o Table 1
55 In the case of chain end initiation the number of possible initiation sites per unit weight is inversely proportional t o x and, if the zip length l / y is larger than x, the amount of monomer formed per break is proportional to x. The over-all rate must thus be independent of x, and
Figure 31 shows that the reaction is initiated at chain ends for the low molecular weight samples. At higher degrees of polymerization, when the zip length is smaller than x, the rate of monomer production d M ,/dt is given by
according t o the general kinetic treatment as outlined in section 3. This is experimentally verified as shown in Fig. 31.
Fig. 31. Dependence of the initial rate of thermal degradation of polymethylmethacrylate on molecular weight [ 89 1.
Above 270°C, end initiation and random initiation occur simultaneously. If the temperature is raised above 300°C, the molecules with labile chain ends are rapidly removed and the random-initiated degradation process can be studied independently [go]. In this case also the kinetic relationship deduced from weight loss experiments depends on the relative values of the degree of polymerization x and the zip length l/r.It has been shown by Cameron and Kerr [go] that when the zip length is less References p p . 165-1 73
TABLE 4 ARRHENIUS EQUATIONS FOR ISOTACTIC AND SYNDIOTACTIC PMMA (MONOMER FORMATION)a [ 931. (a) Isotactic PMMA (Unfractionated) 4.5% conversion
k = (1.19 f 0.14) x lOZ3e-
Medium range
k = (2.83 f 0.38 x l o z z e -
Final range
k = (5.64 f 1.18
X I. o Z ' e -
(68410 f 1958) cal mole-'
RT (66900 f 3180) cal mole-'
RT (65570 f 1870) cal mole-'
RT
min-' min-' min-'
(b) Isotactic PMMA (Fractionated) (64150 f 577) cal mole-'
Medium range
h = (5.08 x 0.18 x 10"e-
Final range
k = (1.13 f 0.36 x 10Zoe-
RT
(61480
* 4793) cal mole-' RT
min-' min-'
(c) Syndiotactic PMMA Initial range (corresponding to medium range of isotactic PMMA)
k = (8.36 f 0.41) x 10"e
Final range
k = (2.93 f 0.38) x 10*'e -
a
The f values are standard deviations from straight lines obtained by the least-squares method.
-
(65760 f 830) cal mole-'
RT
min-'
(64940 f 2004) cal mole-' - min-'
RT
57 than the mean molecular chain length, an element of chain end initiation must be included in the kinetics to fully describe the rate of monomer formation. More recent work [ 91-96] has confirmed these mechanisms and further shown that termination is bimolecular at low temperatures and changes to unimolecular at high temperatures. The influence of tacticity on the rate of polymethylmethacrylate degradation has been studied using a closed system over a range of temperature from 300-400°C in the absence of air [93]. The degradation proceeds by random initiation, depropagation and radical disproportionation. The global Arrhenius equations for monomer formation in these polymers are given in Table 4. The activation energies are similar for all polymers. The elementary rate coefficients for random scission and the kinetic chain lengths, however, show some dependence on the stereospecificity. 7.2 OTHER METHACRYLATES
In the early stages of degradation, polymethyl-a-phenylacrylate [ 97, 981 decomposes by random initiation and unzipping t o monomer, as d o poly-a-methylstyrene and anionic polymethylmethacrylate. Later in the reaction, chain-end initiation becomes important and predominates beyond about 45% conversion. Poly-n-butylmethacrylate yields appreciable amounts of monomer but the reaction is not quantitative [99]. Monomer production ceases at 30-50% conversion at 25OoC, and at
I
40
I
L
80
Time(min)
120
Fig. 32. Decomposition curve for poly(t-butyl methacrylate heated to 2OO0C and maintained at that temperature [ 1001. References p p . 165-1 73
higher temperatures a complex series of reactions occurs in which there is evidence of decomposition of the ester group to give butene, methacrylic acid and anhydride. Grassie and McCallum [99] report that polyethylmethacrylate shows thermal degradation behaviour closely similar t o that of the n-butylester. Poly-t-butylmethacrylate behaves in a very different way. If the pressure of the evolved gas is measured as a function of time [loo] (Fig. 32) three maxima are observed. They correspond to three different stages in the degradation. The volatiles produced during each stage were analysed and the results obtained are shown in Table 5 . These data can be TABLE 5 PRODUCT YIELDS ASSOCIATED WITH MAXIMA C, D AND E (FIG. 32) IN THE THERMAL DEGRADATION OF POLY-t-BUTYLMETHACRYLATE - _ _ _ -
Maximum
Percentage of products
C D E
Total
Single stage
Is0 butene
Monomer
Water
10 35 47.4
10 25 12.4
6 22.3 6.5
3.4 0.1 0
0.6 2.6 5.5
interpreted in terms of three distinct reactions: (i) depolymerization in which monomer is formed, (ii) ester decomposition to yield isobutene and polymethacrylic acid, and (iii) anhydride formation between neighbouring polymethacrylic acid groups and water elimination. The reaction is autocatalytic in nature. The proposed mechanism is
CH3 I -C- I
CH2-C-
I Scheme 4.
CH3 I I
CH,\--H
59 Matsuzaki et al. [ 1011 have found that isotactic poly-t-butylmethacrylate decomposes more rapidly into isobutene and polyanhydride than the corresponding syndiotactic polymer. This is in agreement with the above mechanism.
7.2.1 Conclusion Monomer production is a general reaction of the methacrylates. Ester decomposition yielding methacrylic acid and the corresponding olefin is possible when the alcohol residue has 0 hydrogen atoms; it becomes the most important mechanism in the case of tertiary esters like poly-t-butylmethacrylate but is competitive with monomer formation in ethyl- and n-butylmethacrylates. 7.3 POLYMETHACRYLIC ACID
Thermal degradation of polymethacrylic acid at 2OO0C was first studied by Grant and Grassie [102]. The major reaction is the formation of anhydrides of the glutaric type due t o elimination of water between neighbouring carboxyl groups. Matsuzaki et al. [ 1031 investigated the effect of tacticity on the rate of water elimination. Examination of the infrared spectra of isotactic and atactic polymethacrylic acid heated for 10 min at 17OoC shows that the isotactic sample dehydrates more quickly than the syndiotactic. Thermogravimetric analysis of the rate of water loss between 190 and 21OoC was recently performed by Geuskens et al. [lo41 for atactic and isotactic polymethacrylic acid. Three distinct parts can be observed in the curves (Figs. 33 and 34).
OL
I
50
100
150
200
Time (min)
Fig. 33. Weight loss curves of atactic polymethacrylic acid. 205OC; 0 , 21OoC [ 1041.
0,
190°C;
*, 20OoC; X ,
References p p . 165-1 7 3
60
.--.-.-.-.-. ,.~.-:~-.:.:~~=~~~-~~=~-~--~~=~ .,yL-++
15 -
--
i
/.OM
/y ,:A
!/f
10-
dn
8
5 P
.-I-.-.
.
.P'O
/.,."Q ,O ,OR'
5l / 0
I
50
I
100
L
150
200
Fig. 34. Weight loss curves of isotactic polymethacrylic acid. 0,190°C; A, 20OoC; x , 205OC; 0, 21OoC [ 1041.
(a) A rapid drop corresponding t o about 5% weight loss occurs during the temperature rise time. The rate of weight loss in this region is independent of the polymer tacticity and the degradation temperature, and is due t o water absorbed in the polymer. (b) There is a second range characterized by a slower weight loss that is temperature dependent and higher for the isotactic than for the atactic polymer. (c) There is a limiting weight loss which varies between 13 and 16% depending on the sample. For the atactic polymethacrylic acid degraded at 190 and 2OO0C, a short heating period at 275OC was necessary to obtain the limiting loss within a reasonable time. Only water was detected in the volatile products. No carbon dioxide or monomer was formed. Anhydride formation in the heated polymer results in a decrease in absorption in the region 2500- .3000 ern-.' and at 1700 cm-' , and the appearance of strong absorption at 1022, 1760 and 1810 cm-I. The dehydration of acid groups obeys first-order kinetics at least up t o 80% reaction with both isotactic and atactic samples. Such a result is expected for a reaction occurring in a solid in which each carboxyl group has a neighbouring group available for the formation of an anhydride without any migration or diffusion of the reactants. It is important t o point out that the anhydride is more readily formed from the isotactic than the atactic polymethacrylic acid although the activation energies are almost identical (42 k 1 kcal mole-' ). The influence of the tacticity of polymers on chemical reactivity has been studied by many workers in recent years. Differences are usually observed for intramolecular reactions between two neighbouring groups, leading to ring formation; in such reactions, the isotactic polymer is always the more reactive, in agreement with the results for the dehydration of polymethacrylic acid.
61 7 . 4 POLYMETHYLACRYLATE
This polymer was first studied by Madorsky [105, 1061 and later by Cameron and Kane [ 1071 . The experimental results can be summarized as follows. (a) A rapid decrease in the molecular weight with increasing time of degradation is observed (Fig. 35). I
“i,,
,
,
,
30
40
50
20
10
20
% volatilization
Fig. 35. Molecular weight of residue as a function of percentage volatilization for PMA [107].Temperature of heating: x , 286;0, 290; m, 30OoC.
(b) If the rate of weight loss is plotted against percentage volatilization, the curves show a maximum in the range 10-2076 volatilization, the rate then decreasing linearly. (c) Volatiles are formed but, in contrast to polymethylmethacrylate degradation, very little monomer is evolved [ 105, 1081. (d) Gels are formed in some cases [107,109, 1101. All these data can be interpreted by a free radical mechanism including random initiation and inter- and intramolecular transfer [ l l l ] . The shape of the curve of rate of volatilization plotted as a function of percentage volatilization is in agreement with this kinetic scheme. Theoretical calculations (section 3) have in fact shown that, for polymers undergoing random degradation, the maximum rate of weight loss has to correspond to 26% conversion and not to the 10-20% observed for polymethylacrylate. The position of the maximum is, however, sensitive t o chain transfer. The very little monomer evolved is also in agreement with this mechanism. The products of pyrolysis obtained by different workers are References p p . 1 6 5 - - 1 7 3
62
given in Table 6 [go]. The short zip length is shown by the small amount of monomer evolved, whereas the presence of large fragments is evidence of chain transfer. The observed rapid decrease in molecular wiight also results from random initiation in the case of short zip length when transfer is operative. This has been demonstrated in section 3. The mechanism proposed by Cameron and Kane [ill] for the thermal degradation of polymethylacrylate is HI
'+CH2q+CH2d*
-CH,--C--CH,--C
I
C0,Me
I
C0,Me
H
I
C0,Me
I
C02Me
Inter- o r intramolecular transfer
H - C H 2 -II C - - C I H 2 - k ~ C H 2 ~ ~ C H 2 - C IH 2 C0,Me
CO,Me
C02Me
I
H
I -CH2-C- I + CH2=C+CH2q+CH2-CH2 C0,Me
C0,Me
C0,Me
C0,Me
I
C02Me
Scheme 5.
Terminal double bonds have been identified by NMR [ill]. The initiation step is not known [ 1111. It could arise from random main chain scission or from random side chain breaking. The decrease in molecular weight and the formation of volatile products are both inhibited by dimethylanthraquinone [ 108, 1111. The most reasonable explanation for this effect is that the additive interferes with transfer reactions. The mechanism of formation of volatile products is somewhat speculative. Different possibilities have been discussed by Cameron and Kane [108]. Gel formation occurs with some samples after variable irradiation times [ 107, 109, 1101, probably due to recombination of two radicals of the type
-6
I
-CH2
COOMe
63 TABLE 6 PRODUCTS OF PYROLYSIS OF POLY(METHYL ACRYLATE) BETWEEN 250 AND 40OoC [lo81 ~~
Fmct.
Yield ( w t . %)
Polymer
Residue
Polymer
Residue
- (ii) - (i) - (ii)
(Bn
Low polymer 704)a Low polymer (M, 633)
-90 73
I11
Condensable volatiles
-9.0
Condensable volatiles
26.7 f 3.2
Condensable volatiles
27.4 b
Non-condensable gases Non-condensable gases
Components
-
I1
IV
~
Nature
NO.
I
~
<0.5
Monomer
Oxy -compounds
Monomer CO, COZ, CH4
Yield ( wt. %)
3.4 ( i ) 4.8 trace 14.6 (ii) 7.4 0.7 3.9 16.2 (iii) 4.5 6.7
-(i) - (ii)
Degradation temperatures ("(3): (i) 290, (ii) 250-400; (iii) room to 400 at 2.5OC min-'. Analyses from ( i ) refer to 50% conversion to volatiles. a Using Mechrolab vapour pressure osmometer. From experiments in all-glass apparatus.
The gel content of the degraded polymer residue depends on the method of polymerization used in producing the polymer sample. It is affected by the degree of branching of the initial sample, the degree of conversion during polymerization and possibly the initial molecular weight [ 1091 . The ratio p o / q o , where p o and q o are the densities of chain scission and of crosslinking per unit time of heating, has been determined [ 1101 , according to the theory of Charlesby-Pinner (Chap. 2), for polymer samplesdegraded at 243 and 210°C. This ratio was found to decrease when the temperature of pyrolysis increased. 7.5 OTHER POLYACRYLATES
Polybenzylacrylate [ 1121 appears t o pyrolyse according to a mechanism similar t o that of polymethylacrylate. The main chain polymer backbone decomposes in a random manner. The main products of degradation are carbon dioxide, benzylalcohol and low polymers. The behaviour of polyalkylacrylates on degradation is strongly dependent on the nature of the ester group; primary esters are different in References p p . 165-1 73
64
Fig. 36. TVA thermogram of poly( n-propyl acrylate) at various trap temperatures: ) 0 and -45OC; (--) -75 and -lOO°C [ 1131.
(-
behaviour from secondary and tertiary esters. Ethyl, n-propyl, n-butyl and 2-ethylhexylpolyacrylate degradations have been studied by thermogravimetry and thermal volatilization analysis [113, 1141. They all degrade at approximately the same temperature in a one-stage process, and the general pattern of volatile products is similar. A typical thermogram is given in Fig. 36. In all cases, C O , , and the olefin and the alcohol corresponding to the ester group, are evolved. The number of moles of these volatiles is given in Fig. 37 as a function of the time of degradation for poly( n-propylacrylate). Similar curves are obtained for the other polymers. Insolubility develops in ethyl-, n-propyl- and nbutylesters. No gel was ever formed in degraded poly-2-ethylhexylacrylate.
Time ( h )
Fig. 3 7 . Production of A carbon dioxide, degradation of poly(n-propyl acrylate) [ 1141.
propene and
n-propanol during
65
Since carbon dioxide and olefin are evolved in a molar ratio close to unity, the mechanism that has been proposed is
Scheme 6. I
Temperature ( ' C )
Fig. 38. T V A themogram of poly(isopropy1 acrxlate) at various trap temperatures [ 1 1 3 ] : () 0, -45 and -100°C; (- - -) -75 C.
References p p . 165-1 73
66
Various possible mechanisms for alcohol and network formation have also been discussed. The volatilization of isopropylacrylate [ 113-1151 is a two-stage process as indicated by the thennogram in Fig. 38. No alcohol is formed and the ratio of CO, t o propene is lower than unity. The polymer becomes insoluble and brittle and a yellow colouration appears. The volatilization occurs at a lower temperature for this polymer than for the n-propyl isomer described earlier (Fig. 36). Anhydride structures and water were detected by means of infrared spectra. The data show that a different mechanism is operating in the case of polyisopropylacrylate. In fact, three were proposed to occur simultaneously. The first involves elimination of propene and formation of an acid residue on the chain; this will catalyse further decomposition of the ester group. Such a mechanism has also been proposed t o account for the thermal degradation of poly-t-butylacrylate (see later). It may occur either by a molecular or by a radical process. The molecular reaction may be written as
-C
H, H/C\H I
CI
C=O
F=O + CH,-CH=CH,
0-R
OH
I
CH3 Scheme 7.
The second is the simultaneous elimination of olefin and water; namely,
Scheme 8.
The third is the simultaneous elimination of carbon dioxide and propene according t o Scheme 6 above. The thermal decomposition of poly-t-butylacrylate was studied by Schaefgm and Sarasohn [116] and Grant and Grassie [117]. A t temperatures above 160°C, isobutene was formed quantitatively. A t
67 180"C, isobutene, water and carbon dioxide were identified in the volatile The polymeric residue was found to products in mole ratios of 1/0.4/0.05. be polyacrylic anhydride. The mechanism proposed included the equivalent of Scheme 7 followed by
I
H\? H-C-C-CH, H' I CH3
Scheme 9.
to take into account the autocatalytic character of the process which is most likely due to neighbouring group participation of the carboxylic acid. 8. Polyacrylonitrile and related polymers 8.1 POLYACRYLONITRILE
When polyacrylonitrile is heated in vacuo or in an inert atmosphere, weight loss is observed between 250 and 350°C. Ammonia and hydrogen cyanide are the main volatile products. In the same temperature range,
L
a
01
200
303
400
Temperature ("C)
Fig. 39. DTA and TG curves for PAN 53,slurry polymer, redox-initiated [ 1181. References p p . 165-1 73
68
discolouration appears in the polymer and a strong exotherm has been identified. Typical thermogravimetric and differential thermal analysis curves are given in Fig. 39. The manufacture or carbon fibres by pyrolysis of polyacrylonitrile at high temperature prompted numerous studies to elucidate the mechanism of thermal degradation of this polymer. The main problems t o be solved were: what is the nature of the chromophores responsible for the discolouration of polyacrylonitrile?; what is the mechanism of their formation and the sites where this reaction is initiated? Low molecular weight models of polyacrylonitrile are in fact known t o be thermally stable. Two reviews have been published on the subject [119, 1201.
8.1.1 The structure of the chromophore in discoloured polyacrylonitrile A completely aromatic naphthyridine structure has been proposed by Houtz [121] :
and an azomethine structure was later proposed by Schurz [122, 1231 :
-CH--CH2--CH-CH*-CH-
I
CN
C=NH
I
CN
-CH-CH2-CkH*-CHI I I CN CN CN
on the basis of the UV and IR absorption spectrum of substituted pyridines and naphthyridines. However, these absorb at frequencies of 30,000-33,000 cm- and 43,000-46,000 cm- , compared with 37,000 cm-' for heated polyacrylonitrile. Furthermore, substituted pyridines and naphthyridine have strong infrared absorption at wavelengths of 10-15 pm, where the degraded polymer does not absorb.
'
'
69 Partially hydrogenated ring structures
were proposed by McCartney [124], Burlant and Parsons [125] and Grassie and McNeill [126], whereas Berlin et al. [127] and Fester [128] assumed a structure of the type
Since it is difficult t o resolve this structural problem on the basis of spectroscopic data alone, further studies including chemical methods were undertaken. Peebles and Brandrup [129] prepared (-C=N-), systems by the polymerization of saturated nitrile compounds using either base (with succinonitrile) or heat (with isobutyronitrile and 2,4dicyanopentane). Conjugated (-C=C-), systems were obtained by heating polyvinylchloride or p-carotene. It was found that treatment with basic hydrogen peroxide bleaches and destroys a (--C=N-), system but not a (-C=C-), system, while palladium on charcoal catalyses the hydrogenation of a conjugated (-C=C-), system but not a (--C=N-), system. They further showed that polyacrylonitrile degraded by heat or base always behaves like a (-C=N-), system. Structure (111) was thus proposed as the most probable. However, discrepancies are always found in the C, H, N analysis of degraded polyacrylonitrile, and Peebles and Brandrup [ 1291 demonstrated that oxygen is incorporated into the degraded polymer. Conjugation is not destroyed by the presence of this oxygen and the carbon skeleton remains unchanged as shown by NMR studies. The formation of some nitrone groups in heat-treated polyacrylonitrile was thus suggested:
0
0
0
It was also found that small amounts of the polyimine-type chromophores are sufficient t o produce strong coloration in degraded polymers [129,130]. References p p . 1 6 5 - - 1 7 3
70 8.1.2 Abnormal structures in polyacrylonitrile and their relation to the mechanism of cyclization The action of many nucleophiles in initiating colour production is well known. The action of amines was reported by La Combe [131], the action of bases by McCartney [124], Schurz et al. [122, 1231, Beaman [132] and Overberger et al. [133]. Acids were found, by Grassie and McNeill [ 1341 to accelerate the colouration process. The catalytic effect of acids was studied with polyacrylonitrile containing a small amount of copolymerized acrylic acid units; the mechanism proposed was
Since even carefully purified polyacrylonitrile discoloured on heating, it was suggested by Grassie and Hay [135] that the tertiary hydrogen adjacent t o the nitrile group can act as initiator according t o
This reaction, even if it exists in polymers, is improbable since low molecular weight model compounds were found to be very stable at
71 145°C under nitrogen. Another mechanism was recently proposed by Peebles et al. [120]. Since model compounds are stable, initiators are needed to start the cyclization of nitrile groups. These initiating species are introduced into the PAN molecules in different ways according to Path C, minor
Path B, major
oxygen
oxygen
Path D, minor hydrolysis
/ 1 \
Path A, major /3-ketonitrile defects produced during polymerization
I
Path E, major nucleophilic agents Path A: the incorporation of enamine units occurs by addition of the growing chain radical t o a --C=N substituent of a macromolecular chain. Reaction then occurs with H,O+ to give 6-ketonitrile defects:
-CH2
I
+ -CH2+H-
CN
I
CN I
+=N* -CH*--CH
-
--CHz=CH
I CN
I
I
CN
The ketonitrile group is a weak acid and can- be titrated. The enamine structure has a strong absorption at 2 6 5 nm. References p p . 165-1 73
72 Path B: is the main route of thermal oxidative degradation:
CN
CN OOH I -CH-CH-CHI I CN CN
-Hz 0
0
I1
-CH-C-CHI I CN CN
The 0-ketonitrile content is determined by absorption spectroscopy, and the hydroperoxide iodometrically . Preferential attack of oxygen on the 0-hydrogen was demonstrated by oxidation studies using model compounds
CH3-CH-(CH2),-CH-CH3 I I CN CN with n = 0, 1, 2. The compound with the highest number of -CH2groups (n = 2) is the least stable. Path C: involves attack of oxygen at the tertiary hydrogen atom but is of minor importance in the case of polyacrylonitrile. The oxidation of isobutyronitrile proceeds according to
CH,-CH-CH, I CN
-
CH,--CH--CH, I C H2NI \ 0
OOH I CH,-C-CH, I CN
+
-
CH3-CH2 I + C
NH/ \b
/
Intermediates
CH3 I
c
/B NH, 0
+
-
CH,-CH-CH,
I
COOH
CH3 In the case of the polymer the products are incorporated in the chain and cannot be separated. Path D: hydrolysis of the nitrile group by acids or bases results in the formation of amide and carboxyl groups which initiate the discolouration process. Path E: includes nucleophilic attack on the nitrile group. The nucleophiles are produced by paths A-D. Polymerization of the nitrile groups
73 propagates according to
The nucleophilic character of the P-ketonitrile groups formed in paths A-C was demonstrated by Peebles et id. [120]. Cyclization in this case can be written as
8.1.3 The nature of the exotherm in temperature programmed degmdation of polyacrylonitrile. A new mechanism for chromophore formation
The behaviour of polyacrylonitrile samples heated in vacuo or in an inert atmosphere may be summarized as follows [136]. Below 350°C, short chain molecules containing conjugated carbon-nitrogen sequences are formed. The more volatile are removed from the system. The gaseous products are mainly ammonia and hydrogen cyanide. Between 350 aid References RP. 165-1 73
74 700°C, hydrogen is evolved from the cyclized structures which become aromatic. Above 700°C, intermolecular condensation of aromatic structures occurs and hydrogen is formed. Finally, at about 900°C, nitrogen is evolved; it results from the breakdown of the heterocyclic rings and the rearrangement of these to give pure carbon. Additional data are provided by differential thermal analysis, which has shown that an intense exotherm occurs in the range 250-300°C (Fig. 39). Reich [137] has suggested that the exotherm is caused by nitrile-group polymerization. Hay [138], on the contrary, concludes, on the basis of differential scanning calorimetry, that the exotherm is associated with the formation of ammonia. This problem was reinvestigated by Grassie and McGuchan [136]. They confirmed that the exotherm which is observed during the temperature-programmed degradation of polyacrylonitrile in an inert atmosphere occurs in the same temperature range as colouration and weight loss. Conditions such that the exotherm is separated from weight loss can, however, be found [139]. If isothermal ageing of the sample is performed below 200°C, the exotherm is completely removed during further programmed heating at higher temperature. It must also be noted that volatilization is not observed during the thermal ageing below 200°C, while colour appears gradually. The exotherm is thus associated with cyclization of the nitrile groups as revealed by the IR spectrum (Fig. 40) and not with the formation of volatile products. Ammonia is probably formed from terminal imine structures, and hydrogen cyanide is eliminated from units which have not undergone cyclization. A systematic study of the influence of sample preparation on the differential thermal analysis and thermogravimetric behaviour was then undertaken. The results were shown to be very sensitive t o the method of polymerization and residual traces of catalyst. Initiation of cyclization at
Fig. 40. IR spectra of ( i ) polyacrylonitrile as 1%KBr disc, and (ii) PAN heated for 7 h at 22OoC in Nz, 0.5% KBr disc [ 1391.
75 enamine structures according to Peebles' theory is in agreement with the experimental results for the bulk polymers obtained by a free radical process. Polymers prepared in dimethylformamide with AIBN as initiator incorporate ketonitrile-structures by transfer t o the solvent. These structures also act as initiating sites for the cyclization. The behaviour of redox-initiated slurry polymers depends on end-groups in low molecular weight samples and on the presence of catalyst residues. In anionic polymers, random attack of the strongly basic catalyst on the nitrile groups would also produce abnormal structures of the type -C<
NH
and
-C<
0
NHR NHR The weight loss corresponding to NH, and HCN is very large in some cases (up to 65%) and this is, as discussed by Grassie and McGuchan [139], not consistent with the concept of a small concentration of initiating sites and Initiation Abnormal structures End structures Impurities
-
Cyclization
H
n = 0,1 , 2 . . . m = 0,1, 2.
transfer
NH CN
I
End group reactions
NH,, HCN
I Chain scission
CN
I
Fragments
Scheme ,lo[ 139 1. References p p . 165-1 73
76 long zip length in the nitrile group polymerization. Furthermore, it has been shown by infrared spectroscopy that 80% of the nitrile groups participate in the reaction. Therefore, a mechanism including initiation at abnormal structures, short kinetic chain length and marked chain transfer has been proposed [ 1391 . The general reaction mechanism is given in Scheme 10. Cyclization is initiated by active radicals resulting from the decomposition of defect structures in the polymer. The propagating imino radical will then either attack the next nitrile group or abstract the next tertiary hydrogen. The number of successive cyclized sequences obtained in this manner by competition between addition and hydrogen abstraction lies between 0 and 5. After a transfer step, cyclization is reinitiated according to
The nature of the exotherm produced by the cyclization of the nitrile groups in a sample prepared by a free radical process was shown to be very
0 0
200
400
600
800
1000
Temperature ('C)
Fig. 41. TG curves in N () and vacuum (- - -) of PAN-KCN. 10.7 mg sample heated at 10 degC min-'. DTA curve included [ 1401.
77 sensitive to the presence of additives [140]. Marked reduction in the exotherm is observed in the presence of a free radical inhibitor DPPH. This confirms the free radical nature of the cyclization. It is initiated at much lower temperatures by acidic and basic compounds. Broad exotherms with much reduced differential temperatures are then observed (Fig. 41). Inorganic salts such as KCN, NaSCN and Na,S have the same effect. An ionic or concerted mechanism characterized by a slow propagation is proposed to occur in the presence of these additives. This is in agreement with the mechanism suggested a long time ago by Grassie for polyacrylonitrile containing a small number of copolymerized acrylic acid units. 8.2 POLYMETHACRYLONITRILE, POLY-(U-PHENYLACRYLONITRILE, POLYGCHLOROACRYLONITRILE AND POLYVINYLIDENE CYANIDE [ 1411
8.2.1 Polymethacrylonitrile
The differential thermal analysis curves do not show any exotherm (Fig. 42). Small endotherms corresponding to weight loss are visible. Monomer is the major volatile product. Since low molecular weight
L
200
300
Temperature ( O C )
400
Fig. 42. DTA and TG curves for polymethacrylonitrile [ 141 J . PMAN-A (PMAN-B (- - -).
) and
samples are characterized by a lower stability, chain end initiated depolymerization has been proposed for the first degradation step. A small amount of cyclization is produced in additive-free polymer. Deep colourations are obtained in the presence of acid structures but the concentration of -CZN groups is not reduced by more than 10%.It must References p p . 165-1 73
78
be remembered that in polyacrylonitrile about 80% of the initial G groups have disappeared in the discoloured polymer.
N
8.2.2 Poly-a-phenylacrylonitrile The behaviour of pure poly-a-phenylacrylonitrile is similar to that of polymethacrylonitrile. A strong exotherm which suggests a rapid cyclization is nevertheless observed in the presence of 9%KCN as additive.
8.2.3 Polyvinylidene cyanide The main degradation process in pure polymers is depolymerization. Polymers containing impurities degrade t o a lesser extent and some cyclization of the nitrile groups occurs.
8.2.4 Poly-a-chloroacrylonitrile Dehydrochlorination is the main reaction but a limited amount of nitrile cyclization is indicated by the observed exotherm. 9. Polyvinylchloride 9.1 INTRODUCTION
When polyvinylchloride (PVC) is pyrolysed in a nitrogen atmosphere with the temperature increasing at a rate of 100 deg C h-' (Fig. 43) [142], a rapid loss of weight is observed in the range of about 225-275OC. Analysis of the gas has shown that this loss is primarily due to the evolution of HC1. A second rapid loss of weight is observed between 425 and 475OC. It corresponds t o carbonization of the dehydrochlorinated residue. The maximum loss of weight in the first and second temperature range are about 63 and 86%, respectively. Corresponding to the HC1 loss, unsaturation formation resulting in discolouration of the polymer has been observed. Increase in molecular weight and gel formation in that temperature range have also been reported. The crosslinking of PVC and the pyrolysis at temperatures higher than 4OO0C have not widely been studied, whereas the loss of HCl and the discolouration of the polymer have received much attention. These are indeed very important problems in the industrial processing of PVC. Very efficient stabilizers have been discovered and the practical problem of PVC manufacture is satisfactorily resolved. The mechanism of the degradation is, however, far from being definitively resolved, in spite of the large amount of research being done. This is mainly due to the complexity of the problem: the rate of dehydrochlorination depends on many parameters, such as the size of samples, HC1 partial pressure, molecular weight, branching, crystallinity and the presence of 0,. There is
79 still controversy about the free radical or molecular character of the elimination. An attempt will be made t o review some of the significant data on PVC thermal degradation in the literature. Special reference will be made t o the behaviour of model compounds; reviews of that field have been published j143-1461.
'"I
pyrolysis temperature("C1
Fig. 43. Pyrolysis of ( i ) polyvinylchloride and ( i i ) poly(viny1idine chloride) in a nitrogen atmosphere [ 1421. 9.2 RATE OF HCI ELIMINATION
When 100-200 mg samples of PVC of high purity, prepared without promoters, are heated in nitrogen, the percentage loss in weight as a function of temperature that occurs is given in Fig. 43. As mentioned earlier the rapid loss of weight in the range 200-275OC is due primarily to the evolution of HC1. HC1 evolution was later shown by many workers to begin at temperatures as low as 100°C. S-shaped curves have been reported by Druesdow and Gibbs [147] for the evolution of HC1 with time in a nitrogen atmosphere between 150 and 20OoC. The induction period becomes shorter as the temperature increases. According to these workers, it corresponds to activation of weak links in the polymer. The rate of HCl elimination and the shape of the curve was more recently shown to be very sensitive t o numerous parameters. The presence of plasticizers and other additives may be very critical. Therefore for kinetic study, carefully purified specimens have t o be used in order to avoid complications. References p p . 165-1 73
80
The rate of HC1 elimination in PVC will now be discussed as a function of: the sample size and morphology the presence of oxygen the polymerization conditions and molecular weight of the polymer the temperature of degradation the presence of various additives.
9.2.1 Effect o f sample size and morphology Geddes [ 1481 reports that HCl elimination is linear with time at 182OC for powder samples of less than 400 mg but that S-shaped curves result with larger samples. Acceleration effects are also observed for large agglomerates when compared with powder samples. Identical effects are reported by Geddes for films of different thickness and powders of various particle size. A catalytic effect of the HC1 produced seems to be responsible for the acceleration observed, although Druesdow and Gibbs [147] did not observe any increase in the rate of HC1 evolution when the flow of nitrogen was stopped and a stagnant system produced. An acceleration effect of HC1 has also been reported by Luther and Kruger [ 1491, Troitskaya et al. [150] and Van der Ven and de Wit [151]. As shown in Fig. 44, the catalytic effect of HC1 is more pronounced when more
Fig. 44. Dehydrochlorination of PVC: ( i ) at 190°C 2nd -lo-' Torr. With HCl (150 Torr) addition to the polymer; degraded at 190°C in vacuo (%lo-' Torr) for (ii) 0 min, (iii) 330 min and (iv) 570 min [152].
polyene is formed [152]. The experiment involves the thermal d e p dation of PVC performed with continuous freezing out of HC1; then 150 tom pressure of HC1 is introduced into the system at definite times, indicated by arrows on the figure, and degradation is then continued without removal of HC1. After longer degradation in vacuo, and thus higher polyene content, there is a higher initial dehydrochlorination rate in the presence of HC1.
81 9.2.2 Degradation in the presence of oxygen
HC1 elimination is faster in the presence of oxygen than in pure nitrogen (Fig. 45), but no permanent increase in rate is observed when oxygen is admitted temporarily to the system.
I
Time(min)
Fig. 45. The dehydrochlorination of 448 powder at 182.5OC in ( i ) nitrogen and ( i i ) oxygen [ 148 1.
9.2.3 E f f e c t o f polymerization conditions and molecular weight
The rate of dehydrochlorination was found to be about four times lower for PVC prepared by bulk polymerization at -50°C than for that prepared by conventional suspension polymerization [ 1531. Guyot et al. [154] reported that the crystallinity of low molecular weight PVC fractions induces thermal stability in a nitrogen atmosphere. This is observed as long as the temperature is below the melting point. A significant dependence of heat resistance on stereoregularity was also demonstrated by Millan and Nino [155] by thermogravimetric analysis. Low molecular weight components (25,00O-50,000) favour HC1 elimination in PVC. The stability of a polymer sample is, in fact, improved when they are eliminated by extraction. The presence of oxygen during polymerization results in a polymer with a high oxygen content. Berticat and Vallet [156] and Popova et al. References pp. 165-1 73
82 [ 1571 have shown that the rate of dehydrochlorination is proportional to the oxygen content. They do not specify, however, how the peroxide is incorporated chemically. The influence of molecular weight has been given a great deal of attention. Armaldi et al. [ 1581, Bengough and Varma [ 1591 and Sat0 and Asahina [160] have independently reported that there is no linear relationship between the rate of HC1 evolution and the inverse of molecular weight. Other workers [ 161,1621, on the contrary, find that the rate is dependent on the reciprocal of the degree of polymerization. It can thus be concluded that only part, if any, of the dehydrochlorination is initiated at the chain ends. Therefore a detailed study of fractionatedpolymers has been carried out by Sat0 and Asahina [ 1631. Of three fractions with viscosities ranging from 0.028 to 0.122 1 . g-' ,the intermediate one was shown to be the most stable with respect to HC1 loss and decrease of transmittance. The initiation of HC1 loss must thus be related to the presence of more than one weak link in the polymer. This view is substantiated by the fact that model compounds of the polymer, having secondary chlorine such as 2-4dichloropentane, are stable below 200°C. The identification of the weak links can be made in two different ways: by the study of thermal stability of model compounds and by the synthesis and degradation of polymers or copolymers containing potentially weak links. Both methods have been used and the results obtained will be outlined briefly in sections 9.4 and 9.5.
9.2.4 Effect of the temperature o f degradation The effect of temperature on the rate of dehydrochlorination has been studied by many workers. The activation energies for films and solutions usually lie between 22 and 30 kcal mole-'. Some of the reported data are given in Table 7. 9.2.5 E f f e c t o f additives Hydroquinone-type inhibitors of radical chain reactions were shown by Bengough and Sharpe [161] t o have no effect on the rate of HC1 elimination. Free radical sources like peroxides or AIBN have been incorporated during the thermal treatment. According to Bengough and Sharpe [161] and Braun and Bender [169], they d o not modify the rate of dehydrochlorination. If a concentration of 4% initiator in solution is used, a two-fold increase in rate is observed [161]. Geddes [173], however, reports a strong acceleration effect due t o peroxides and related substances. Polyenes and other conjugated substances [1741 inhibit the evolution of HC1. The same effect was reported with gaseous nitric oxide [ 1731. Very efficient stabilizers are used during the processing of PVC; the mechanism of their action has become somewhat controversial. Extensive tabulation of these additives has been given [175]. Some of the most
83 TABLE 7 ACTIVATION ENERGIES FOR THE DEHYDROCHLORINATION OF POLYVINYLCHLORIDE E (kcal mole-' )
Temperature range
Physical state of the sample
Ref.
22.8 to 24 5 26 to 32 34 24 29.5 30 20 25 27 0 28
178 t o 212 130 to 190 235 t o 260
solution solid solid solid and solution solid solid solution
161 164 165 166 167 168 169
solution
170
films
171
films
172
("C
-
186 t o 250 150 to 220 160 t o 200 175 to 210 210 to 260 126 to 155 78 t o 126 90 to 130
I
efficient are zinc, cadmium, lead, calcium and barium soaps. Synergetic action is observed when some combinations of soaps are used. It is often assumed that metal soaps scavenge the evolved hydrogen chloride. Frye and Horst [176] have proposed that metal soaps displace the labile chlorine by the more stable ester group. The esterification of the allylic chlorine of model compounds for PVC was performed by Bengough and Onozuka [177]. The thermal stability of the compounds was improved. The chlorine atoms of 2,4-dichloropentane could not be exchanged using ester metal soaps. Organotin stabilizers also have a widespread use; some examples are dialkyltin dicarboxylate, dialkyltin bis(maleate ester), dialkyltin bis(alky1mercaptan), dialkyltin( S,S'-mercaptoacid ester) and dialkyltin P-mercaptopropionate. The last one is supposed t o exist in the solid state as a kind of telomer -CI1 0
References p p . 165-1 7 3
84
,
The mechanism of action of stabilizers of the type Bu, SnY involves a displacement reaction between the 7 group of the organotin compound and the labile chlorine of PVC [178, 1791. This was confirmed in the case of model compounds by Onozuka and Asahina 11441 and more recently by Suzuki et al. [ 1801. Neutralization of the evolved hydrogen chloride occurs. The reactivity of organotin additives with respect t o hydrogen chloride has been shown to be a measure of their efficiency in stabilizing polyvinylchloride [ 1811. Organotin derivatives containing maleate are particularly good colour inhibitors because they interrupt the formation of double-bond sequences by taking part in a Diels-Alder reaction. Labile chlorine can also be displaced by alkyl aluminium compounds of the type R, AlCl [ 1821 or by organic phosphites. Various other classes of stabilizers are currently used. Their mechanism of action has been discussed recently by Rasuvaev et al. [152] and by Nass [183]. An extensive review of the properties of these additives is given by the latter. wavelength ( 8 )
3000
4000
5000 600( 115
1.0-
0.8-
35000
Xi000
25XO
2QO00
Wavenumber (cml)
Fig. 46. Absorption spectra of suspension-polymerized PVC ( 5 8 5 ) heated at 15OoC in nitrogen for 15, 35, 60, 85, and 115 min [ 1 4 8 ] .
85 9.3 DISCOLOURATION OF PVC
When PVC is heated, new absorption bands appear in the UV and visible spectra (Fig. 46). The absorption maxima have been related to polyene structures by Braun and Thallmaier [184] and many other authors. Convincing agreement exists between the absorption maxima shown by the polymer and those reported by Bohlmann and Mannhard [ 1851 for dimethylpolyene. Y
I
20
L-
250
I:' :: 1 1
(cm-')
.. "
I
I .
PVC- IBu-Cop 190 I Id
300
400
-1
500
600
700
A (nm)
Fig. 47. Absorption spectrum of thermally degraded polyvinylchloride (Vestolit S K 55), polyvinylbromide and a copolymer vinyl chloride-isobutene in tetrahydrofuran. The absorption maxima correspond to polyene sequences with n = 4, 5, 6, etc. [ 1841.
The absorption spectra of a heated PVC foil are identical if the oil is obtained direct from the solid sample or from a solution. The absorption spectrum of a polyvinylbromide sample however, is quite different (Fig. 47). A broad absorption without structure has been assigned to a mixture of polyene sequences much longer than those observed in PVC. Figure 48 gives the frequency of polyene sequences in decomposed PVC and polyvinylbromide when the fraction of evolved HC1 is 0.16 x The frequency decreases with increasing number of conjugated double bonds, while in decomposed PVBr, mean sequencies consisting of about 12-13 double bonds occur more often than either shorter or longer ones. With increasing time of degradation, a deficit in polyene concentration was found compared t o the liberated hydrogen chloride [168]. The References p p . 165-1 73
86
n
Fig. 48. Frequency of polyene sequences for a polyvinylchloride samqle degraded at 17OoC in nitrogen and a polyvinylbromide sample degraded at 100 C in nitrogen [ 1841; conversion x 0.16 x lo-*.
Ol
2
6
4
10
8
12
14
n
Fig. 49. Sequence distribution of polyene in degraded polyvinylchloride [ 1681 (see text). Vestolit SK 55: time of degradation (h) (a) 0.5, (b) 1, (c) 2.1, ( d ) 4.4, (e) 11.1; conversion x l O z (a) 0.063, (b) 0.165, (c) 0.383, (d) 0.797, (e) 2.29. Vestolit S 55: time (h) ( f ) 0.5, (g) 1.1, (h) 2.1; conversion x l O z ( f ) 0.057, (9) 0.155, (h) 0.351.
seauence distribution at the same time shifts noticeably towards shorter sequences for PVC powders. This is attributed to secondary reactions of the longer sequences; these may be network or aromatic structure formation. A parameter Vn which is defined as
vn
xn =-n-
c
n=1
xn
87 (where x , is the fraction of the double bonds formed which are involved in sequencies of length n ) is a measure of the sequence distribution. It is given in Fig. 49 as a function of n for various degradation yields from PVC powders and illustrates the preceding considerations. Another conclusion that may be drawn from these data is that the formation of long polyene
r
loo
L
l-
' d
ot Wavelength (nm)
Fig. 50. Ultraviolet spectra of model compounds and charge-transfer complex measured in 0.1 mm liquid cell. (a), 4-chlorohexene-2; (b), 4-chlorohexene-2 heated for 1 0 min a t 18OoC in vacuo (measured after 24 h); (c), sample ( b ) after bubbling of nitrogen; ( d ) 4-acetoxyhexene-2 and decomposed 4-acetoxyhexene-2; (e), mixture of 2,4-hexadiene and trichloroacetic acid; ( f ) , the mixture of 2,4-hexadiene and sulphuric acid. (b), (e) and ( f ) are charge-transfer complexes [144].
sequences takes place very rapidly once the initial step of dehydrochlorination has occurred. Apart from the above-mentioned consecutive reactions, only the number, not the average length, of polyene sequences changes significantly with increasing time of degradation. A different interpretation of the absorption spectra involving chargetransfer complex formation was proposed by Schlimper [186] and later by Onozuka and Asahina [ 1441 . Discolouration of the polymer would be due partly to charge-transfer complexes between HC1 and double bonds. These complexes are destroyed in the presence of ammonia. Arguments in References p p . 165-1 73
88 favour of the complexes arise from the behaviour of model compounds [144]. 4-Chlorohexene-2 shows an amber colour when it is heated in vacuo, the reaction being
C1 colourless [CH3--CH=CH--CH=CH--CH,]'
C1-
yellow This colour fades rapidly on bubbling nitrogen or washing with aqueousalkali. The yellow colour reappears on passing HC1, but the product remains colourless in the presence of acetic acid. The absorption spectra of 4-chlorohexene-2 and its charge-transfer complex are given in Fig. 50. 9.4 THERMAL STABILITY OF MODEL COMPOUNDS
Dehydrochlorination of low molecular weight organic compounds has been investigated by Baum and Wartman [164], by Asahina and Onozuka [187] and by Barton and Howlett [188, 1891. Some lose hydrogen chloride by a free radical chain mechanism and others by molecular elimination. The free radical chain mechanism in unambiguously shown by strong inhibition of the dehydrochlorination by added propene. Free radical and molecular elimination are both first-order reactions. The following compounds degrade by a free radical mechanism: 1,2-dichloroethane, 1,1,2,2-tetrachloroethanne,1,1,1,2-tetrachloroethane, 1,1,2-trichloroethane, 1,4dichlorobutane. Others decompose by molecular elimination: ethylchloride, l,ldichloropropane, 4-chlorohexene TABLE 8 DATA FOR HCI-ELIMINATION O F ALKYL-HALOGEN COMPOUNDS [ 1441 Compound
Decomp. temp. ("C)
2-Chloropro pane 340 2,4-Dichloropentane 360 2-Methyl-2chloropropane 230 3-Ethyl-3chloropentane 180 4-Chlorohexene-1 3 25 3-Chloropentene-1 280 3-Chloropentene-2 >400 4-Chlorohexene-2 160
ASS (eu mole-')
Ea (kcal m o l e - ' )
AG-f (kcal m o l e - ' )
- 11.5 + 29.2
42.4 69.9
48.2 50.2
- 2.6
41.6
41.9
- 15.4 - 16.5 - 19.8
31.0 38.0 34.0
37.1 47.0 43.9
- 20.9
28.5
36.7
89 and other hydrocarbons having one primary, secondary or tertiary chlorine. The activation energy E, entropy AS*, free energy AG' and the temperature of decomposition are given in Table 8 for some of these compounds. These results shown that the thermal stability of saturated compounds having secondary chlorines is very high, whereas compounds with tertiary of allylic chlorine are much less stable. The order of stability is
72H5
CH,-CH,--C--CH2-CH, I c1
> CH,--CH=CH--CH+H,
1,2-Dichloride structures were studied by Erbe et al. [190] and are thought to be more stable than 2,4dichloropentane which represents the normal structure of the polymer. 9.5 WEAK LINKS IN PVC
The results given in the preceding section 9.4 on model compounds would seem to suggest that the normal structure of PVC is very stable. Anomalous weak links are thus probably responsible for the degradation of the polymer. The potential weak links in PVC are (i) 1,adichloride structures -CH2-CH-CH--CH2-
I
I
c1 c1 (ii) vinyl chlorine at chain ends
-cH=YH c1
(iii) primary chlorine at chain ends --CH2-CH2-C1 (iv) allylic chlorine in the chain --CH2-CH-CH=CH-CH2-
I c1
References p p . 165-1 7 3
90
(v) allylic chlorine at chain ends -CH2-CH-CH=CH2
I
c1 I
CH2 I (vi) tertiary chlorine -CH2-C-CH2-
I
c1 These structures are formed during preparation of PVC in the following ways. Structure (i) is formed by combination termination or tail-to-tail addition. Structures (ii) and (iii) are formed by disproportionation termination. Structure (iv) results from HC1 elimination. Structure (v) results from termination transfer to the monomer by C1abstraction and reinitiation by the radical formed. Structure (vi) results from termination transfer to the polymer by hydrogen abstraction and reinitiation at the radical site in the macroradical. From the considerations in the preceding section 9.4, it may be inferred that the order of increasing stability of these chain structures is (a) 0-chloro-unsaturated structures in the chain, (b) tertiary chlorine, (c) P-chloro-unsaturated structures (allylic chlorine) at chain ends; (d) tertiary hydrogen and normal head-to-tail structures; (e) vinyl chlorine at chain ends; (f) head-to-head structures. In order to verify these assumptions experimentally Gupta and St Pierre [191] prepared PVC containing the structures
Q
-CH,-CHCl-&CHCl-CH,-
I
and
CH3
(C) and (D) were obtained by copolymerizing vinyl chloride and, respectively, l-chloropropene and 2-chloropropene. The mole ratio of vinyl chloride t o the second monomers were, respectively, 4.33/1.08 and 7.40/1.06 in the copolymers.
91
200
240
200
320
Tern pemtu r e ("C)
Fig. 51. Relative thermal stability of polyvinylchloride samples by dynamic thermogravimetry. 0, PVC(A);0, PVC(E);A, PVC(C);V,PVC(D)[191].
The relative thermal stabilities obtained by dynamic thermogravimetry above 200°C and by isothermal methods at 220°C are given in Figs. 51 and 52. (A) is a slightly branched polymer sample produced using benzoyl peroxide. Polymer (B) is a linear syndiotactic sample prepared at low temperature. The figures show that copolymers (C) and (D) are both much less stable than (A) and (B). Tertiary hydrogen and tertiary chlorine are
Time (min)
Fig. 52. HCl evolution at 224OC.0, PVC(A);0, PVC(B); A, PVC(C);V,PVC(D) [191]. References p p . 165-1 73
92 thus weak spots for the initiation of dehydrochlorination. The distribution of polyene length is not given. The relative stabilities deduced from the study of model compounds are thus in agreement with these results obtained by Gupta and St. Pierre on polymers. PVC containing allylic chlorine has not been synthesized as yet. The study of its stability would give valuable information concerning the behaviour of the links that are supposed to be the weakest in PVC. It has, however, been shown in section 9.2.5 that if allylic chlorines are esterified by reaction with organometallic compounds, stabilization of the polymer occurs. 9.6 MECHANISM OF DEHYDROCHLORINATION OF THE POLYMER
Both free radical and molecular mechanisms have been proposed. 9.6.1 Free radical mechanisms
Free radical processes were first postulated by Arlman [ 1661, Winkler [192] and Stromberg et al. [165]. The rate of dehydrochlorination of PVC was reported t o be a 3/2 order reaction by Stromberg et al. [165] and the mechanism suggested was the following. Initiation
H H H H ( I l l
-c-c-c-cI l l
1
c 1 H c1 H
kl
H H H H I I I I
-c-c-q-c-++1 I I I C1 H
(95)
H
Propagation
H H H H I I I I
-C-C-C-C!-
I
I
I
I
+.C1
H C1 H C1 H H H H 1 1 1 1
-c-c-q--cI
I
H c1 Termination
I
C1
-
k3
k2
H H H I I I -C<-C-C1 1 . H C1
H H H H 1 1 1 1
-c-c-c=cI
I
H C1
H I 1 C1
+ c1*
+HCl
(97)
93 A 3/2 order reaction was also observed by Salovey and Bair [171]. The overall activation energy was reported t o be 27 kcal mole-' between 126 and 155OC and zero between 78O and 12OoC. A more complex chain mechanism was proposed. Initiation is identical to eqn. (95) but propagation proceeds according to
H H H H
I
l
l
1
4-C-C-C-
1
H
-
1
H H H H
I I I .
kP
1
I
-C-C-C=C-
--+
I
+ HCI
H
H C1
C1 H
Transfer occurs according t o H H H
I
I
*-(C=C),
I
H H H H
+ -c-c-c-c-
I
I
I
I
H C1 H C1
-
H H H I I 1
H H H H I I I I
c1
1 - 1 1 H H H
Taking into account their observation that the rate of dehydrochlorination in solution is first order and inversely proportional to the number average degree of polymerization, Bengough and Sharpe [ 1611 proposed the following end-initiated mechanism
I I
CHCl=CH-kH-CH2+HCl-CH2-
CHCl=CH-CH=CH-kH-CH,-
+ C1'
+ HC1 etc. References p p . 165-1 73
94
It may be that occasionally C1- atoms escape from their environment, attack a second polymer molecule and thus start a short chain. Between 1 7 8 and 212°C the rate expression proposed is
where [HCl] is expressed in mole 1-' and C, is the polymer concentration in polymole 1-' . Another route for initiation of PVC dehydrochlorination has been suggested by Russian workers [152] who maintain that a system of conjugated double bonds can be partly present in the triplet state even at room temperature if the sequence is long enough; the existence of triplet states of polyene chains at 170-200°C is certain. They propose that the polyene chain in the triplet state takes part in the reaction, for example,
t
t
-CH-CH=CH-CH=CH-CH=CH--CH-CH.-(CH=CH)4-CH-
1
c1
-
tl
+
c1 -(CH=CH),+H-
+ C1'
Conversion of the polyene into the ground singlet state yields energy that most probably excites the C-C1 bond into the triplet state. A chlorine atom is then formed and initiates dehydrochlorination by a radical chain mechanism. Another route for the formation of chlorine atoms is
t
--CH-(CH=CH),,-CH-
t
H
-kH-(CH=CH),-CH2-(a)
-(cH=cH),-~H-cH-
-
+ -( CH=CH),,,--CH%HI I
I
c1
-
C1
+ -(CH=CH),
-+H--CHI c1
(b) - ( C H = C H ) ~ + ~ - -+ c b
The triplet polyene interacts with another macromolecule containing hydrogen in the 0-position t o conjugated double bopds giving two
95 stabilized macro-radicals (a) and (b). The latter decomposes giving chlorine atoms which initiate polymer degradation. The polyene triplet state may also yield benzene
which is in fact observed in the degradation products. The participation of free radical intermediates has been proved by Bamford and Fenton [ 1931 by degrading PVC a t 180°C in labelled toluene. Since toluene becomes incorporated in the chain, free radicals must be intermediates. Investigation of the thermal degradation of mixtures of PVC and polymethylmethacrylate [194] shows that the elimination of HC1 is retarded in the presence of the methacrylate. Figure 53 shows the experimental results obtained by programmed or isothermal thermogravimetric analysis. The rate of gas evolution is measured with Pirani gauges situated behind cold traps, the temperatures of which are indicated on the figure. Methylmethacrylate is completely condensed at -lOO"C, whilst HC1 is not trapped at that temperature. The PVC is thus more stable in the mixture, but the polymethylmethacrylate is initially less stable and gives monomer at temperatures corresponding to PVC dehydrochlorination. This interaction is explained in terms of attack on polymethylmethacrylate by chlorine atoms from the degrading PVC. Many other polymer blends and block copolymers have been studied (section 14). A slight retardation of HC1 evolution is generally observed. The strongest evidence invoked for a radical elimination is the presence of an ESR absorption, which has been reported by many authors. Degraded solid PVC exhibits paramagnetic character, since a broad singlet line is observed with a polymer that has lost 10%of the total HC1 [195]. The signal intensity decreases with temperature but is stable over many weeks with the polymer in vacuo. This singlet has, however, been shown to be associated with the polyene system and not with a radical, since it is present in air and in solutiondegraded material and its intensity does not alter with time [ 1951. Stronger evidence for free radical generation in PVC at 220°C has been obtained more recently by Liebman et al. [196]. The radicals appear in the early stages of dehydrochlorination, and decay rapidly. Reference6 p p . 165-1 73
96
.-
C
e
-h-u
3-
c)
0
a
2-
--------___
1-
O r 4 200
-75.
300
400
E 0
Sample temperature (%I
Fig. 53a. Differential condensation TVA curves for 20 mg film samples of ( i ) P v c Breon 113, (ii) PMM FR 1. Heating rate 10 degC min-' [ 1941.
3-
-
> 1E. c
3
c a
a
.-
(i i)
C 0 L .-
-
a 3u c 0
a
200
300
E
Sample tempemture('C)
Fig. 53b. Differential condensation TVA curves for simultaneous degradation of PVC Breon 1 1 3 and PMM FR 1, 20 mg of each; ( i ) unmixed, (ii) mixed. Film samples, heating rate 1 0 degC min-' [ 1941.
97 Another type of argument to support a free radical mechanism was advanced by Palma and Carenza [ 1721. Thermal and y-initiated dehydrochlorination between 80 and 130°C were compared. In view of the resemblance shown by the kinetic data for polyene formation, the same mechanism was thought t o be operative in both cases. Since according to the authors, a free radical mechanism is clearly established for y-initiated processes, this is also operative in thermal degradation. Salovey and Bair [171] reported that the thermal degradation of PVC at 155°C is enhanced by irradiation with 1 MeV electrons. Since later stages of isothermal weight loss for thermal and radiolytic decomposition follow 3 / 2 order kinetics, a free radical mechanism is also postulated by these workers. 9.6.2 Molecular elimination
Many experimental results, however can not be explained by a free radical mechanism. Bengough and Sharpe [161] found that addition of radical inhibitors or radical precursors have no effect on the rate of degradation. But this is not a good argument, since little is known of the effect of such inhibitors at high temperatures. The effect of free radical sources like AIBN is also not conclusive since there is no agreement between the results in the literature. According to Bengough and Sharpe [161], they have no effect on the rate of dehydrochlorination in solution, while Geddes [ 1481 reports a strong acceleration effect of these additives in PVC films. Stronger evidence against the free radical mechanism arises from the catalytic effect of HC1. This is indeed difficult to explain if the dehydrochlorination involves free radicals. If, on the other hand, molecular elimination with a cyclic transition state is operative; namely, Cl---H * * *
IPCI
-CH2+H-CH-CHCl-
* * *
-HCl
-CH2+H=CH-CHCl-
the following modified process seems reasonable in the presence of HC1 [169].
p-3 $2 - - - -CH2
--+
.
-CH2-CH=CH-CHCl-+
2 HC1
*
It must also be noted that the products of chain termination H2 and C12, in the radical mechanism proposed by Stromberg et al. [165] (section 9.6.1) have not been detected. The following observations are in agreement with molecular elimination: (a) the model compounds in the gas phase d o not lose HC1 by a radical mechanism, and References p p . 165-1 73
98 (b) the dehydrochlorination of PVC proceeds violently in the presence of FeCl,, ZnClz, etc. Therefore, molecular, non-radical dehydrochlorination is suggested by many workers t o be the most probable mechanism for dehydrochlorination of PVC. A general kinetic treatment of polymer degradation by elimination has been presented by Tudos et al. [170, 1971. The detailed elementary reactions taking place in the course of degradation are not taken into account. The main features of the model are (i) The initiating step of the process is the random elimination reaction, which is unimolecular from the point of the polymer molecule. (ii) Chain propagation takes place in a series of activated unimolecular elimination reaction steps. The activation propagates in only one direction, determined by the head-to-tail linkage. (iii) The chain termination takes place either by the reaction chain reaching the end of a polymer sequence given a priori (it is determined by the length distribution of the polymer sequences), or by the occurrence of a reaction step interrupting the propagation of activation (that is, a reaction step which gives a product that has no activating effect on the neighbouring monomeric unit). The values calculated according to this model for the yield of HC1, and concentration and distribution of polyene sequences are in agreement with the experimental results that Tiidos et al. obtained for the degradation of polyvinylchloride. 9.7 CONCLUSION
It is quite clear that free radicals are formed during the thermal degradation of PVC. On the other hand, the existence of molecular elimination also seems probable. There are two ways of correlating the data. (a) Free radical and molecular elimination occur simultaneously and their relative importance depends on temperature, the former becoming more important at higher temperatures. This view is suppoked by the work of Rasuvaev et al. [ 1521 and seems very promising. (b) Dehydrochlorination occurs by a molecular elimination process, but free radicals are generated in the system by the breaking of weak bonds, such as peroxide or hydroperoxide, which become incorporated in the system during polymer synthesis, purification or processing.
10. Other vinyl polymers 10.1 POLYVINYLACETATE
When heated, polyvinylacetate liberates acetic acid, and conjugated double bonds are formed in the residual polymer. It was suggested, a.long
99 time ago [198],that the degradation proceeds by a non-radical chain mechanism initiated at chain ends and propagated from unit t o unit along the chain. The problem was more recently re-examined by Servotte and Desreux [ 1991.The loss of weight was measured a t constant temperatures between 230 and 300°C. Acetic acid proved t o be the most abundant volatile product formed (90-95%). The rate of weight loss was independent of the initial molecular weight, in disagreement with end initiated degradation. Insolubilization was found to develop in the residue even after a small weight loss. Infrared analysis of the heated polymer performed at different degrees of degradation shows that the absorption in the 1600 cm-' region (double bonds) is very weak, while progressive deacetylation of the polymer takes place. Some acetic ester groups, however, remained in the polymer when 70% weight had been lost. The residue was nevertheless observed to be deeply coloured in agreement with the existence of conjugated double bonds. Owing t o the important discrepancies between the results and mechanisms proposed by Grassie [ 1981 and Servotte and Desreux [ 1991,further work is needed. A thermal volatilization analysis of polyvinylacetate degradation has been reported by Gardner and McNeill [200] (Fig. 54).Two maxima are observed at 322 and 435°C. The Pirani gauge situated after the 0°C trap responds t o all volatile products, while the gauge situated after the -196°C trap responds only t o non-condensable gases. Infrared analysis has shown the presence of carbon monoxide and methane in this last fraction. The
t
0"
Temperature ( " C )
Fig. 54. Thermal volatilization analysis for polyvinylacetate. 100 mg film sample, 5 degC min-' 1200 1 . References p p . 165-1 7 3
100 differences in response between the -75OC and -196OC curves were assigned t o the formation of water, carbon dioxide and ketene. These last two products have also been identified in the products that are volatile at -75OC. The two peaks shown in Fig. 54 thus correspond to the same products: acetic acid, methane, water, ketene, carbon monoxide and dioxide. UV spectra (Fig. 55) of degraded polyvinylacetate films show the presence of new absorptions, which have been assigned by the authors to 2-4-6-octatriene chromophores (triad centred at 272 nm), and t o longer polyenes which extend the absorption up to 400 nm.
W a v e l e n g t h (nm)
Fig. 55. UV spectra for PVA as 2 0 mg films initially..(a) undegraded, (b) degraded to 289OC, (c) degraded to 301°C, ( d ) degraded t o 313OC, ( e ) degraded to 332OC, (f) degraded t o 3 8 l o C , at 5 degC min-' [ 2001. 10.2 POLY VINYLALCOHOL
The thermal degradation of polyvinylalcohol has been studied by several workers [201-2041. The main products of degradation have been shown to be water from an elimination reaction similar t o that observed with polyvinylacetate, and acetaldehyde from depolymerization. Small amounts of aldehydes and ketones of the general formula OCH-(CH=CH),-CH3 and CH3-CO-(CH=CH),-CH3 were also detected by Tsuchiya and Sumi [ 2041. Water is formed by a mechanism similar t o that for hydrogen chloride production from polyvinylchloride, and acetic acid from polyvinylacetate, leaving a conjugated polyene
101
-
structure; namely, -(CH*H2)n+H+H2--
I
OH
I
OH
+ nH20
-(CH=CH)n-CH-CH2-
I
OH Scission of some of the C-C bonds results in the formation of carbonyl ends according to -CH-CH,--( I OH
CH=CH)n+H-CH2-
I
OH
-
-CH-CH2-(CH=CH),-CH
I
OH
I1
+ CH3+H-
I
0
-CH-CH,-(CH=CH),-&CH2--CH1 I OH OH
OH
-
I OH
-CH--CH,--(CH=CH),--C=CH2 I I OH OH
+ CH-CH2-II
I
(99)
0
I
--CH-CH,-(
(98)
CH=CH),--C-CH3
II
OH 0 A thermogravimetric analysis by Gardner and McNeill [ 2001 has shown the existence of four degradation peaks (Fig. 56). The first corresponds to water elimination; absorbed water and chemically linked water may be involved. The second peak would correspond to the formation of water, acetaldehyde, formaldehyde and hydrogen. The two high temperature peaks have not been identified. The UV absorption spectrum is modified. Absorption appears between 250 and 400 nm. The new bands are similar to those observed with degraded polyvinylacetate but are much less resolved. The carbonization of polyvinylalcohol has been studied. After heating to constant weight at 25OoC, polyvinylalcohol was pyrolysed at 900°C. Hydrogen, carbon monoxide, carbon dioxide, methane, acetylene and ethane were identified in the volatile products [ 2051. When polyvinylalcohol is modified with phosphorous acid (monoesters are formed and also possibly some crosslinks), the dehydration is accelerated and occurs at lower temperatures [2061. Reference8 p p . 166-1 73
102
-
4-
> c
3
n
3-
c)
3
0
Tern perat u re ('C)
Fig. 56. Thermal volatilization analysis of polyvinyl alcohol. 100 mg film sample, 5 degC min-' [ 2001.
10.3 POLYCHLOROPRENE
Polychloroprene eliminates hydrogen chloride in high yield during its thermal degradation. Although its structure is analogous t o that of polyisoprene, its behaviour is quite similar t o that of polyvinylchloride. A typical thermogravimetric weight loss curve is shown in Fig. 57 [207]. In earlier work a sharp exotherm observed at 377OC for a heating rate of 10 degC/min [208] was found t o correspond t o the maximum rate of evolution of HC1. Thermogravimetric curves recorded at a heating rate of 200 degC/h [209] have proved that the reaction takes place in two stages: elimination of hydrogen chloride followed by decomposition of
200
I
1
1
300
400
500
600
700
700
Ternperat u r e ('C)
Fig. 57. Thermogravimetric curves for polychloroprene MC 30 (continuous line) and PC-A (dotted line) [207]. Dynamic nitrogen atmosphere, 10 degC min-', 10 mg samples.
103 the residue. It was also demonstrated that hydrogen chloride does not accelerate the dehydrochlorination as is observed with polyvinylchloride. Analysis of the volatile products has been performed [ 210, 2111. Heating for 20 min at 400°C removed 68% of the chlorine as hydrogen chloride and gave 2% monomer [210]. When the polymer is pyrolysed at 17OO0C on an electrically heated filament only monomer is formed, while polyvinylchloride heated in the same conditions yields hydrogen chloride and benzene [ 2111.
I
I
100
I
200
I
300
I
400
f
Temperature ( ' C )
Fig. 58. Differential thermal analysis of polychloroprenes MC 30 (upper curve) and PC-A (lower curve). Dynamic nitrogen atmosphere; 10 degC min-' , 20 mg samples; reference, glass beads [ 2071.
The thermal degradation of polychloroprene was reinvestigated more recently by Gardner and McNeill [ 2071 . The results of thermogravimetric, thermal volatilization and differential thermal analysis are given in Figs. 57-59 for comparison. HC1 evolution attains its maximum rate at about 35OoC as indicated by the weight loss curve, the first peak of the thermal volatilization curve and the sharp exotherm obtained by differential thermal analysis. Endothermic melting of the crystalline region of the polymer is responsible for the peak observed in the vicinity of 50°C in the DTA curve. Measurement of the quantity of HC1 evolved during heating was performed by titration [207]. Comparison of the data with the weight loss curve showed that HC1 does not entirely account for the weight References p p . 165-1 73
104
Temperature ("0
Fig. 59. TVA curves for polychloroprene MC 30 at heating rates of 10 degC min-' (upper curve) and 5 degC min-' (lower curve). 30 mg samples were used, as small pieces [ 2071.
loss below 40OoC. Some non-condensables are also evolved, in agreement with the results of thermal volatilization analysis. The kinetics of dehydrochlorination was also studied by isothermal methods [ 2071. Activation energies determined by different methods applied to isothermal and programmed techniques all extend from 33 to 42 kcal mole-' and the logarithm of the frequency factor lies between 10 and 12.4. Values of the activation energy for dehydrochlorination of polyvinylchloride extend from 22 to 33 kcal mole-' and are thus considerably lower. Detailed study of the products of degradation (gaseous, liquid and solid residue) was performed by the same workers [212]. Below 4OO0C, small amounts of ethylene and a trace of chloroprene were detected in addition t o hydrogen chloride. Above 4OO0C, methane became a significant product but smaller amounts of hydrogen, ethylene and propene were present. The liquid product found after degradation on the water-cooled part of the degradation tube is a complex mixture of dimers of chloroprene and less volatile components containing aromatic structures. The UV spectrum of the polymer residue showed similarities with that of polyvinylacetate; conjugated structures are formed but the polyene sequences are shorter than with polyvinylchloride. Triene structures predominate and there is little contribution from structures with more than ten double bonds in conjugation.
11. Polymers containing heteroatoms in the chain 11.1 POLYSILOXANES
The thermal stability of polydimethylsiloxane has been the subject of numerous studies [213-2241. When heated in an inert medium or in
105 vacuo [ 2131 it depolymerizes into cyclic low molecular weight products. It has also been demonstrated [214, 2151 that the thermal stability of polydimethylsiloxane essentially depends on the presence of impurities and traces of polymerization catalysts which are active centres for initiation of the degradation. Investigation of the thermal degradation of polysiloxanes with terminal hydroxy groups [219] indicates that, at low conversion to volatile products, increase in the molecular weight of the polymer occurs in the range 170--3OOOC. This was assigned t o a polycondensation involving the terminal hydroxy groups. Subsequent increase in temperature decomposes the polymer and decreases its molecular weight (Fig. 60). The volatile fraction consists mostly of cyclic trimer-hexamethylcyclo trisiloxane :
the mechanism of depolymerization proposed is CH3
I
CH3
I
CH3
I
CH3
I
--Si-O-Si-O-Si-O-Si-OH I I I I CH3 CH3 CH3 CH3
H3C H3C CH3 CH, Si<-si/o\&-CH3 I \I
-
-
I
H3C
. . :
H-6,
:
I
./ 0
-
s1
/ \
CH3 CH3
-
CH3
CH3 I -Si-OH
CH3
l o 1 CH3-Si \Si-CH3 + I I
The process is initiated at terminal hydroxy groups and favoured by the spiral-like structure of polysiloxanes. Replacement of the hydroxy groups by methyl, or blocking them by chelation t o copper, iron or zirconium acetylacetonates, considerably decreases the rate of decomposition of the polymer and increases its thermal stability (Table 9). However, pronounced crosslinking even at moderate temperatures was observed in the polymer stabilized by transition metal compounds. The effect of the metal additives during thermal ageing is associated with reactions leading References p p . 165-1 73
106
Temperature
("C)
Fig. 60. Molecular weight ( i ) of polysiloxane and its weight loss (ii) in thermal degradation during 4 h. TABLE 9 EFFECT OF TERMINAL GROUPS ON THERMOSTABILITY OF POLYDIMETHYLSILOXANE AT 400° FOR 4 h [219]
Terminal groups
Weight loss (%)
CH3
I I
84-8
-O--Si-OH CH3
FH3
32.3
-0-Si- CH3
I
CH3 11.7
FH3
4-Si-0-Fe
(AcAc)z
14.8
CH3
I I
+Si-O--Zr
(AcAc)
CH3
AcAc = acetylacetonate fragment.
8.2
107 to cleavage of the siloxane chain and insertion of metal hetero-atoms in the latter. Cyclic trimer-hexamethylcyclotrisiloxaneis also formed during thermal ageing of the stabilized polymer. Cleavage, however, would occur at random along the chain. The mechanism was confirmed by Thomas and Kendrick [220] who performed the thermogravimetric analysis of various samples of polydimethylsiloxane prepared with special emphasis on the exclusion of hydroxy groups. The rate of volatilization t o cyclic dimethylsiloxane was found to be independent of molecular weight. The activation energy is 42 k 3 kcal mole-'. The depolymerization is thus randomly initiated. Change in molecular weight distribution was also observed with hydroxy end-block polymer fractions. The chain lengthening process occurring in vacuo below the depolymerization temperature is assigned t o intermolecular condensation of terminal hydroxy groups in agreement with Rode et al. [219]. An apparent activation energy of 8.6 k 1kcal mole-' has been measured. 11.2 POLYOXYMETHYLENE
A study of the thermal stability of polyoxymethylene was made by Schweitzer et al. [ 2251. The rate of weight loss was measured at 222°C. Formaldehyde is evolved by a first-order reaction. The decomposition was assumed to take place mainly by unzipping from the chain end, since the rate of weight loss increases with molecular weight. This was confirmed later by Kern and Cherdron [226] who also showed that acetylation of end groups leads to improved thermal properties. The degradation was reinvestigated later by Grassie and Roche [227]. An inverse relationship between molecular weight and initial rate of volatilization was found. The change in molecular weight with percentage volatilization is given in Fig. 61. The position of this curve above the diagonal D indicates that the reaction is not a stepwise degradation in which a stable polymer molecule is produced, since each monomer molecule is liberated from the chain end. The results are in agreement with an end initiated chain process, the average length of which is less than the average degree of polymerization. There is also evidence that little or no transfer occurs. Acetylating the terminal OH groups of the polymer inhibits the chain end initiation for the chains terminated by OH groups. The degradation was also found to occur preferentially in the amorphous region of the polymer. Molecular, free radical and ionic mechanisms were considered in detail by Grassie and Roche [227]. The absence of any secondary volatile products, which would result from an end initiated radical reaction, are strong arguments against a free radical mechanism. Furthermore, inhibitors of radical reactions have no effect on the depolymerization. In the presence of basic catalysts the reaction is accelerated and undoubtedly References p p . 165-1 73
108
I
1
20
40
L
6(
%volatl I tzatlon
Fig. 6 1. Changes in the number average molecular weights of polyoxymethylene during degradation at 17OoC. (The molecular weights were obtained via viscosity measurements.) [227 1.
anionic. Anionic and molecular mechanisms can nevertheless not be distinguished for the uncatalysed reaction. The end initiated nature of the degradation of -OH terminated polyoxymethylene chains was also confirmed by Dudina et al. [228]. End-blocked polymers, on the other hand, degrade by random initiation. The kinetic chain length was shown t o be smaller than the macromolecular chain and formaldehyde participates in chain transfer. The reaction is first order for the end-blocked polymers. Deviation from the first-order law is observed for unstabilized polymers. This shows that the fragments formed by disappearance of the polymer active centres are more stable than the original polymer molecules. The activation energies of the degradation process are given in Table 10. The thermal properties of copolymers of trioxane with cyclic ethers and acetals, lactones and vinyl monomers have been reviewed by Jaacks [229]. In contrast to pure polyoxymethylene diols, they depolymerize only partially when heated to
200OC.
TABLE 10 TRUE ACTIVATION ENERGY ( E ) VALUES FOR FORMALDEHYDE POLYMERS [ 2281
0
II
End group
-OH
-C-CH3
-0-CH3
-C-C-OH
E (kcal mole-')
26
32
41
46
109 11.3 HIGHER POLYETHERS
A comparison of the thermal stability of polyethylene oxide, polypropylene oxide, polyethylene and polypropylene has been presented by Madorsky and Straus [230]. More recently, studies on the thermal degradation of polytetramethylene oxide (I), polyhexamethylene oxide (11) and polydioxolane (111)
have been reported by Blyumenfeld et al. [231]. Initiation was shown to occur at the carbon in a position t o the oxygen atom. Rupture of the C-H bond is followed by breaking of the main chain according t o
11.4 NYLON
The degradation of nylon-6,6.has been studied extensively [232-2351. A wide range of degradation products is reported. These include simple hydrocarbons, cyclopentanone, water, carbon monoxide, carbon dioxide and ammonia. Gelation also occurs in some cases and discolouration is observed [236]. A large variation (15-42 kcal mole-' ) rather than a single value has been reported for the activation energy. Residual water was also found to be very important. Owing to the variety of volatile products formed and the variation in the activation energy, a complex mechanism has t o be operative. Breaking of the -NH-CO- link, followed by decarbonylation and cyclization, were among the various steps proposed. F. Wiloth [ 2361 has recently re-examined the problem. Nylon-6,6 and nylon-6,lO were compared under different degradation conditions. Viscosity measurements, titration of acid and basic groups in the pyrolysed copolymer, and determinations of ammonia and carbon dioxide produced were performed. The considerably more pronounced instability of nylon-6,6 has been assigned t o the ring closure tendency of the adipic acid component. In the presence of water, the thermolysis is dominated by the reactions of end groups, and in dry, high-molecular weight systems by reactions involving chain-amide groups. The reactions proposed are presented in Schemes 11and 12. References p p . 165-1 73
110
6
u
60 f J
2
6
u ++-
x
I
z
Scheme 11. Thermolysis of low molecular weight nylon-6.6 in the presence of water [ 2361.
111
Other data were recently published by Peebles and Huffman [237]. The rate of gel and colour formation in nylon-6,6 is found t o be dependent on the rate of removal of the volatile products of degradation. CH2-CH2 I I CH2 CH2-CO-NH\
'CO-NH-
-
(1)+-NH2
See Scheme 11. Scheme 12. Thermolysis of high molecular weight product in absence of water.
If a sample of nylon is heated above its melting point in a sealed tube, the material remains soluble in organic solvents over extended periods of time; the intrinsic viscosity first passes through a maximum, then a minimum, followed by formation of insoluble material (Fig. 62). Discolouration is not observed. End-group concentration varies as shown in Fig. 63.
1lo
2
4
6
8 10 12 2 14 16 18 20 22 24 1 Time (h)
Fig. 62. Change in molecular weight as a function of time for nylon-66 at 282OC contained in a sealed tube such that the volatile materials were maintained over the melt [ 2371. References p p . 165-1 73
112
Tirne(h)
Fig. 63. End-group concentrations (in m.Eq./g) as a function of time [237]. Same conditions as in Fig. 62.
Comparison of these two figures indicates that the initial increase in molecular weight is due t o polymerization of the unreacted ends -NH2
+ NH2- + -NH-
+ NH3
Ammonolysis, namely,
and the usual hydrolysis of the amide group were also proposed to occur. Branches are formed at the site of the secondary amines:
0
II
-C--NH,
+ -NH-
-
-N-
I
+NH,
-c=o
Chain scission and crosslinking are thus occurring simultaneously. If the volatile materials formed are permitted to escape, rapid gelation and colour formation is observed even in the complete absence of oxygen. Ammonolysis and hydrolysis are, in fact, strongly reduced in these conditions. Careful analysis of the volatile products was also performed
113 TABLE 11 DEGRADATION PRODUCTS OF NYLON 66 AT 305OC [237]
Product Highly volatile materials
Less volatile materials Neutral fraction
Cyclic monomer Cyclopentanone Cyclopent ylidinec yclo pentanone Cy clopentylcyclopen tanone Hexylamine Hexamethyleneimine Hexamethy lenediamine [ b,e] -Pyridine Several unknown materials
Basic fraction
Polymeric residuum after hydrolysis (black) Neutral fraction
Acid fraction (straw-coloured)
Basic fraction (black oil)
a
3-Pentanonea Cyclopenty Ic yclopentanone, Cy clopenty Ic yclopentanol Cyclopenty lidinecyclopentanone Other unknowns, three in high concentration Succinic acid Glutaric acid Adipic acid Pimelic acida Suberic acida Many other unknowns, some in high concentration Hexylamine Hexamethy leneimine Hexameth ylenediamine 6,6’-Diaminodihexylamine Non-volatile black oil
Identification based on retention time only.
(Table 11).One major source of water is thermal cracking followed by dehydration
0 II -C-NH-CH2-
0 II + -C-NH2
L
+ CH,=CH-CN+H20 References pp. 165-1 73
114 Ammonia and carbon dioxide result from decarboxylation and deamination following hydrolysis of the amide group. Dimers of cyclopentanone and the cyclic monomer of nylon-6,6, namely,
0
r
II
0
II
C--(CH2)4*
LN--(cH,),-NJ I H
1
I H
are formed. 1 1 . 5 THERMOSETTING RESINS
Extensive discussion on the degradation mechanism of thermosetting resins is beyond the scope of this book. The subject was reviewed in 1970 by Conley [ 2381. Some of the recent results on two important classes of
a Temperature (OC)
Fig. 64. Thermogravimetric curves of phenolic condensation polymers [ 2391.Sample weight 100 mg, pressure 0.2 Tom; heating rate 9-10 degC min-'
.
115 thermosetting resins, epoxy- and phenol-formaldehyde polymers will be outlined briefly. Weight loss is initiated in the neighbourhood of 300°C for phenolformaldehyde polymers. A mechanism of degradation has been proposed by Conley [238] t o take into account the volatile products formed. It is summarized in Scheme 13. Oxidation is initiated at the site of the methylene group or at terminal - C H 2OH. Subsequent decomposition of the ketone and acid groups formed results in CO, C 0 2 and water production. Pure thermal degradation results in rupture in the a position to the methylene group. Char is formed under oxidizing conditions. A comprehensive study of the thermal degradation of epoxy resins has been reported by Lee [239]. Their stability was found to be lower than that of polycarbonate, polyphenylene sulphide and teflon (Fig. 64).
DER 331 resin
DEN 438 resin
Polycarbonate
Polyphenylene sulphide
MNA: methylbicyclo[ 2,2,1]hept-5-ene-2.3-dicarboxylicanhydride. MDA: methylene dianiline.
Many concurrent reactions are usually operative. Their relative importance depends on the structure of the resins and the type of curing agent. The degradation products are mostly phenolic compounds. Three mechanisms based on the principle of simple ether cleavage and on the experimental results obtained were proposed: (a) The residual epoxide isomerizes to an aldehyde which decomposes into propionaldehyde and/or ethane and carbon monoxide. This is summarized in Scheme 14, Route I and was proposed earlier by Anderson [ 2411. (b) The residual epoxide undergoes etherification to form 1,3-hydroxyl substituted diethers which dehydrate. Three routes are then possible References p p . 165-1 73
116
OH
OH
I>CH2
117
-0 \
CH3*
(111)
,CH2
\
CH, + ,CH*
OH
n + * O H
fJ--”o/
H2co
0
\
,CH2
I
COOH I
Scheme 13. Typical reactions proposed for resin decomposition at elevated temperatures. (Route I) oxidative degradation processes; (Route 11) fragmentation reactions; (Route 111) formation of benzenoid species [ 2381.
References p p . 165-1 73
118
+
Route 11-C
Route 11-B
I(
/( Etherification)
Etherification)
/(Dehydration)
~ O + H = C H - IC H z -
1 CHI=CH
I
I
/(Hydrogen abstraction)
CH, =CH+H,-O+€H
I
(Claisen rearrangement)
* I # I
OH
j(Cle=we)
CH,=CH, + C O
(Hydrogen abstraction)
('laben
?H OCH2+H=CH, \
CH,=CH+HO I(Decarbony1ation)
I
I(Hydrogen abstraction)
I
Polymer Scheme 14. Degradation of epoxide resins [239].
I
Polymer
0
+ CH,=C=CH,
120
/
-?-
gs Y + 8II Y
X
I
T-o++X
X
..yT -0I
T
p + + X
3
*I
I
8 - y=o 8
8+ t
57
8+
121 according to the mode of decomposition of the 1,%unsaturdted diethers formed: Routes 11-A, 11-B and 11-C. (c) Scission of 1,2,3-triethers, which are present in the cured epoxy resins, occurs according t o similar mechanisms, Route 111. In the presence of oxygen, hydroperoxides, that further decompose, are formed at allylic carbons, Route IV.
12. Fluorinated polymers Polytetrafluoroethylene (PTFE) has been known for about thirty years. It is the most stable addition polymer. Its exceptional thermal stability has been assigned to the high C-F bond strength and to the shielding effect of the highly electronegative fluorine atoms. Therefore much research has been devoted during the last decade t o the synthesis of a large variety of fluorine containing polymers. All of them, with the exception of copolymers of CF, =CF, and CF, -CF=CF, and polytetrafluoroethylene oxide, were found t o be less stable than PTFE. In this section the mechanism of PTFE degradation will be outlined, but since kinetic data on the other fluorinated polymers are very scarce, we shall only characterize their stability by thermogravimetric data (Table 1 2 and Figs. 65-67). Comprehensive reviews on the thermal behaviour of fluorinated polymers have been published by Wright [242, 2431 and Wall [ 2441. 12.1 POLYTETRAFLUOROETHYLENE
The thermal degradation of PTFE has been widely studied. The general kinetic pattern of the degradation between 360 and 600°C is as follows. (a) The rate of volatilization is independent of molecular weight [245, 2461. (b) The molecular weight decreases during pyrolysis [ 2461. (c) The rate of weight loss is reduced if reaction products are allowed to accumulate [245-2471. (d) The rate of weight loss in inert atmosphere or in vacuo is stated to be first order [245-2521, although Carroll and Manche [253] and Cox et al. [ 2541 disagree and report a zero-order reaction. (e) Activation energies and pre-exponential factors have been determined by various methods and are, respectively, of the order of 80 kcal mole-' and 10' s-I . (f) The volatile products formed between 500 and 12OO0C have been analysed by mass spectrometry [255]. The results are given in Table 13. (g) The nature of the reaction vessel has an effect on the rate of volatilization [ 2471. On the basis of these experimental results, an over-all mechanism of References p p . 165-1 73
122 TABLE 1 2 THERMAL STABILITY O F FLUORINE-CONTAINING POLYMERS IN VACUUM ~ 4 2 1 Polymer unit
Ethylenic homopolymers: +FHCH2+F2CH2-CFHCFCI--CFzCFH--CF2CFCI-
+F2CF(CF3 )--CF2CF(CSFllk * F ~ C F ( O C ~ H S)Diene polymer: 4-chloroperfluoroheptadiene-1,6 Ethylenic copolymers: CF2CH2/CF2CFCl (a) 19%CFzCHz (b) 53% CFzCHz (c) 67% CF2CH2
CF2CHz /CF2 CF(CF3 ) CF2CF2/CFZCF(CF3 ) CF,CFH/CFjNO CF~CF~/CFJNO
Styrene polymers: 0, 0-trifluorostyrene 2, 3, 4, 5, 6-pentafluorostyrene Condensation polymers: Perfluoroalkylene triazines (a) from perfluoroglutarodiamidine (b) from perfluoroglutarodiamidine and perfluorobutyroamidine (1:l)
Q,
Activation Arrhenius Rate o f energy factor w t. loss (heal mole-' ) (s-' at 35OoC ( % p e r min)
48 71 38 53 50 50 61 81 76 83 75 78 57 63
57 68 61 50 61 54 57 46 55 73 47 56 58
10'O
lozo
10' 10l2 10l2 10' 1019 1019 10'~ 1019
-
1019 10'
loz2 1015
lo2' loL5 1015 1015 10'6 10' 10' 10'2 10' 10' 'I
l o 2' lo2'
Temperature ( " C ) for 1 % w t . loss per min
0.1 0.02 4 20 0.005 410 330 2.6 0.02 415 0.2 370 0.3 370 0.3 365 2 ~ 1 0 - ~510 515 2.6 x 510 1.2 x -
2.2 x 77 "2600
0.1
-
-
512 290 240 300 390
0.18 370 0.06 390 0.12 385 0.06 390 395 0.06 0.04 395 0.04 410 2 ~ 1 0 - ~495 530 1.8 x 1000 255 1200 265 1200 270
64 65
1019 1017
4.8 0.03
340 395
39
lo6
6~
540
43
lo8
6 ~ l O - ~520
123 TABLE 12-continued
Polymer unit
Activation Arrhenius Rate of energy factor wt. loss (kcal mole-') ( s - l ) at 35OoC ( % p e r min)
(c) from perfluoroadipodiamidine and perfluorobutyroamidine ( 1:1.35) 31 Polyhexafluoropentylene 32 adipate Polyhexafluoropentylene adipatelisophthalate Tereph thal ylchloridel octafluorohexane diol Fluorosilicone
lo5 lo8
8x10-3
2.0 "1.7
58 44
1 0l6 1013
Temperature
("c)for I%
wt. loss per min
500 335
2.3 8~
0.01
420 440
random chain scission, followed by depolymerization and termination by disproportionation, has been proposed [ 246,24'11. The occurrence of chain transfer has been a subject for discussion. It was originally assumed to have a very low probability owing to the large C-F bond energy [ 2 5 6 ] , but it was later pointed out that the energetics of the transfer reaction are not unfavourable. Efforts have been made to improve the thermal stability of PTFE: initiation of polymerization with fluorocarbon catalysts, inclusion in the chain of structural units able to promote transfer of the depropagating chain and inclusion of additives for the same purpose [257-2591. Only the last method has had some success.
Fig. 65. Weight loss behaviour of polymers representing several degradation processes and a wide range of thermal stabilities. The curves show volatilization rates of polymers heated in nitrogen at atmospheric pressure and at a constant rate of temperature increase of 100 degC h-' [ 242 1. References p p . 165-1 7 3
124
Temperature
('C)
Fig. 66. Comparison of thermal stabilities of various fluorine-containing polymers in vacuo [ 2431; A CF3NO-CF2 CFH copolymer; B, CF3NO-CF2 CF2 copolymer; C, fluorosilicone A; D, methylmethacrylate octafluorocyclohexa-l,3-dienecopolymer; E, [ CHFCFCI], ; F, polyhexafluoropentylene adipate; G, [ CF2 CFCl], ; H, CF2 CFCI-CF2 CH2 copolymer (80/20); I, CF2 CFCl-CF2 CH2 copolymer (50/50);J, CF2 CFCI-CF2 CH2 copolymer (30/70); K, CF2 CH2-CF3CFCF2 copolymer; L, terephthalyl chloride-octafluorohexane-l,6-diol polymer; M, fluorosilicone B; N, [ CF2 CH2 I n ; 0, butadiene-octafluorohexa-l,3-diene copolymer; P, CF2 CF2 -CF3 CFCF2 copolymer; Q, [ CF2 CF2 ] n . A
200
240
280
320
360
400
440
480
5
Temperature ("C)
Fig. 67. Comparison of thermal stabilities of various fluorine-containing polymers in oxygen [ 243 1. A; CF3NO-CF2 CFH copolymer; B, CF3 N M F 2 CF2 copolymer; C, polyhexafluoropentylene adipate; D, fluorosilicone A; E, [ CHFCFCI],, ; F, CF2 CFCI-CF2 CH2 copolymer (50/50);G, CF2 CFCI-CF2 CH2 copolymer (30/70); H, CF2 CFCI-CF2 CH2 copolymer (80/20); I, [ CF2CFClI n ; J, [ CF2 CH2 ] n ; K, terephthalyl chloride-octafluorohexane-1,6-diol polymer; L, butadiene-octafluoroCF2C H 2 - C F 3CFCF2 copolymer; N, cyclohexa-1,3-diene copolymer; M, CF2 CF2-CF3CFCF2 copolymer; 0, [ CFz CF2 ] n .
125 TABLE 13 ANALYSIS OF VOLATILE PRODUCTS FROM PYROLYSIS OF POLYTETRAFLUOROETHYLENE AT ELEVATED TEMPERATURES IN A VACUUM [255]
At 5OO0C
Componenta
Expt.
HF CF4 CZ F4 C3F6
Vwr Total a
At 8OO0C
At 120OoC
1
2
3
4
5
6
0 1.5 94.8 3.7 0 ___ 100.0
0 1.2 95.1 3.7 0 100.0
0 1.6 92.5 5.9 0 100.0
0 1.8 89.9 6.5 1.8 -
0.2 1.7 81 .O 5.3 11.8 100.0
0.5 2.6 75.2 5.8 15.9 100.0
100.0
Components are in wt. % of total volatiles.
12.2 OTHER PERFLUORO AND HYDROFLUORO ADDITION POLYMERS
Polyhexafluoropropene and polyperfluorohept-1-ene have low thermal stability (Table 12). Perfluoroacenaphthylene polymer is not more stable than polytrichlorofluoroethylene [ 243, 2601. Perfluorobutyne-2 yields s highly branched and crosslinked material which is more stable than PTFE [261]. Perfluorallene also gives a highly crosslinked solid, the therma, behaviour of which has not been characterized [ 2621. The thermal stability of polytetrafluoroethylene oxide and PTFE have been compared under the same conditions by Donato et al. [263] between 450 and 600°C. The decomposition rate has a maximum at 628°C for the oxide and at 568°C for PTFE. The activation energy for the first-order degradations are 98 kcal mole-' between 8.5 and 85% for the oxide polymer and 85 kcal mole-' between 523 and 571°C for PTFE. The rate of weight loss is less than 1.2% per min for both polymers below T = 550°C for the oxide and T = 590°C for PTFE. The oxide, however, loses weight below 390°C whereas PTFE does not. The main components of the volatile material are trifluoroacetyl fluoride, carbonyl fluoride and tetrafluoroethylene. An end-initiated thermal degradation with small zip length is proposed. Madorsky et al. [ 2641 have studied polyvinylfluoride, polyvinylidene fluoride and polytrifluoroethylene degradation in the range 372-500°C. Their behaviour is shown in Table 12. Hydrogen fluoride is an important volatile product. Polyvinylfluoride was reinvestigated recently [2651. It is stable in vacuo up to 300°C. The degradation products of polyvinylidene fluoride were analysed by Pravednikov et al. [266] and a mechanism of degradation was proposed. References p p . 165-1 73
126 Various other polymers have been prepared [242-2441. stable than PTFE.
All are less
12.3 CHLOROFLUOROPOLYMERS
The thermal degradation of polychlorotrifluoroethylene has been thoroughly studied [ 2671 . Only 28% of degradation products (mainly monomer) is volatile at room temperature. The remaining 72% has an average molecular weight of 900 but is volatile at the temperature of pyrolysis. The degradation of this polymer commences 150 degC lower than for PTFE. This was attributed t o the lower C - C l bond strength (81 kcal mole-') and confirmed by infrared methods: CF=CH2 groups were detected, confirming the splitting off of chlorine [268]. The thermal behaviour of other chlorofluoropolymers is given in Fig. 66 and Table 12. 12.4 FLUOROSTYRENE POLYMERS
Poly-a,p,@trifluorostyrene has slightly lower stability than polystyrene (Table 12). The relatively large amount of monomer formed suggests that chain scission is followed by depolymerization. Poly-2,3,4,5,6 pentafluoropolystyrene is much more stable than polystyrene (Table 12). Wall et al. [269] attributed this increased stability to the loss of resonance interaction between the phenyl group and the chain because of the presence of the fluorine atoms. Perfluorostyrene polymerized by yirradiation has, however, been found recently t o have a stability close to that of polystyrene: a rate of weight loss of 0.4% per min was found at 335°C and complete decomposition of the polymer is observed at 432'C [ 2701. 12.5 COPOLYMERS
Various copolymers of the fluorinated monomers have been prepared [ 2431. Copolymers of tetrafluoroethylene and hexafluoropropene have under vacuo a stability close t o that of teflon (Fig. 66). Copolymers with trifluoronitrosomethane have a lower stability than PTFE (Figs. 66 and 67). The copolymer of vinylidenefluoride and hexafluoropropene is one of the most stable elastomers available at the present time (Fig. 66 and Table 12). For a typical copolymer containing 70% vinylidene fluoride, the rate of weight loss is 0.04% per min at 350°C and the activation energy is 57 t o 46 kcal mole-', according t o Wright [243]. A wide range of other addition copolymers have been synthetized and examined for thermal stability in vacuo and in oxygen. Typical weight loss data are given in Fig. 65.
127 12.6 FLUOROAROMATIC POLYMERS
Perfluoropolyphenylene shows about the same stability as the unfluorinated analogues [ 2711. Perfluoropolyphenylene ethers are less stable than the corresponding polyphenylene ethers [ 2721. Perfluoropoly-p-phenylenesulphide is less stable than p-polyphenylenesulphide in the range 360-440°C [273]. 12.7 OTHER CONDENSATION POLYMERS [ 2431
Linear aliphatic fluorinated polyurethanes have been tested with respect to the location of the fluorine atoms in the diol or diisocyanate component. Fluorine atoms introduced into the diisocyanate unit increase the stability of the urethane group, but the presence of these atoms in the diol unit favours dissociation of the urethane group to monomer. Comparison of PTFE and perfluoroamidine polymers shows that introduction of triazine rings in fluoromethylene ,chains enhances their stability. Various fluorinated polyesters have been synthetized. The thermal stabilities of some of them in oxygen and in vacuo are compared in Figs. 66 and 67. The terephthalyl chloride/octafluorohexane-l,6diolpolymer shows a good stability in vacuo. Polymers containing triazine in the chain
X
decompose by a complex mechanism in which hydrolysis probably plays an important part. Some of them can be used for a short period in air at 300-350°C. Polybenzimidazoles of the type
L
Jn References pp. 165-1 73
128 readily decomposes with elimination of HF. This is attributed to a reaction of the hydrogen atom from the imino group with the fluorine atoms. 12.8 EVOLUTION OF HF FROM HYDROFLUORO AND PERFLUORO POLYMERS
The evolution of hydrogen fluoride or other products giving rise to Fions in aqueous solution has been studied quite recently for a number of hydrofluoro and perfluoro polymers heated in nitrogen or in air [274]. Such data are important since they indicate the maximum temperature of use for such polymers and also the risks of corrosion in high-temperature applications. The results obtained for degradation in a nitrogen atmosphere are given in Tables 1 4 and 15. They can be compared with the data for degradation in air (Tables 1 6 and 17). The temperature for initial weight loss and initial F- yield are the same in many cases. For other polymers, however, F- is detected at temperatures much lower than those for weight loss. This has been observed for instance with polyvinylfluoride, polyvinylidene fluoride and some Viton rubbers which are important commercial products. TABLE 14 EVOLUTION OF HYDROGEN FLUORIDE FROM PERFLUOROPOLYMERS IN NITROGEN [ 2741 Polymer structure
Temperature ("C) for Initial weight loss
fCFzCFz-3 Platinum boat 350 Calcium fluoride boat f-CFzCF2 /CF,CFCF2 -3 400 f-P-c6F44 High molecular weight 330 Low molecular weight 350 150 P-C~FSC~F~C~F~C ~FS f-m-c6F44
High molecular weight Low molecular weight m-C6Fs C6F4C6 F4 c6 F5
f-c6F4
s+
Crosslinked Linear +CSNF34 +C6F4CFz o-+ +C6F3(CF3)CF20+
1% weight loss
Initial F yield
F yield
Final total yield of F (%)
432
289 190 293
510 518 530
11.6 11.2 6.6
271 337
504 512 > 700
22.9 12.8
457 376 393 175
-
1%
150 120 120
162 144 126
160 212
-
403 502 > 700
200 170 150 40 100
315 215 280 60 128
180 212 291 168 198
374 467 355 437 486
-
16.7 13.7
-
31.3 16.1 56.9 7.0 5.1
129 TABLE 15 EVOLUTION O F HYDROGEN FLUORIDE FROM HYDROFLUOROPOLYMERS IN NITROGEN [274] ~~
~~
Polymer structure
Temperature ("C) for 1%
Initial weight loss
I% weight loss
Initial
240 240 320 340 290 270 350 400 170 250 270 220 340 340 213 250 270
320 320 390 365 305 350 410 440 320 305 295 270' 375 365 255 280 350
177 337 284 396 475 329 413 492 312 136 457 430 141 271 442 361 188 292 >SO0 337 >SO0 254 494 192 366 244 368 205 260 329 244 499 437
F
yield
Final total yield of
F yield F(%)
70.8 70.5 8.5 0.9 4.8 12.9 13.2 13.5 28.5 1.1 1.7 4.8 35.3 41.0 87.6 33.7 32.9
TABLE 16 EVOLUTION OF HYDROGEN FLUORIDE FROM PERFLUOROPOLYMERS IN AIR [274] Polymer structure
fCF2CF2-3 Platinum boat Calcium fluoride boat ~CFZCF~/CF~CFCF~+ fp-c6F4+ High molecular weight Low molecular weight P-C6FSC6F4C6F4C6FS fm-C6F4+ High molecular weight Low molecular weight m-C6F5C6F4C6F4C6F5 fCbF4S+ Crosslinked Linear fCSNF3+ fc6F4CF20+ fC6F3(CF3)CF20+
Temperature ( " C ) for
F yield
Final total yield of F(%)
424
236 239 298
433 3 59 429
68.2 70.7 78.4
280 300 150
344 384 164
180 337 198
354 462 587
50.7 54.6 2.0
120 140 110
163 186 124
142 122 70
402 368 579
70.0 61.3 1.7
200 160 180 50 100
243 270 290 75 122
154 191 286 182 163
334 364 410 310 372
79.4 82.5 72.6 25.2 12.9
Initial weight loss
1% Initial weight loss F yield
300
392
400
1%
References p p . 165-1 73
130 TABLE 17 EVOLUTION OF HYDROGEN FLUORIDE FROM HYDROFLUOROPOLYMERS IN AIR [274] Polymer structure
Temperature ("C) for Initial weight loss
1% weight loss
Initial 1% F F yield yield
190 250 300 290 300 340 380 370 200 200 240 260 250 180 190 240 295
250 320 330 325 320 395 420 425 360 250 270 290 360 250 255 260 380
153 214 311 294 294 143 195 259 220 199 243 269 175 186 153 221 280
276 386 373 359 387 431 417 420 383 334 348 333 361 327 266 296 420
Final total yield of F(%)
93.7 75.4 36.0 63.4 6.9 54.2 54.7 46.5 56.2 31.7 25.9 36.3 54.0 59.7 91.2 51.7 61.3
The nature of the primary breakdown products that give rise t o the Fions is not yet determined for perfluoropolymers. Hydrogen fluoride is evolved directly from hydrofluoropolymers. 12.9 CONCLUSION
The preceding discussion shows that PTFE is the most stable addition polymer. Until now, from the large range of fluorinated polymers and copolymers, only two are found to have a thermal stability approaching that of PTFE. Other fluorinated polymers show no advantage with respect to degradation in vacuo over the unfluorinated analogues. In oxygen, however, fluorinated polymers are often more stable.
13. Thermostable organic polymers 13.1 INTRODUCTION
One of the greatest disadvantages of high polymers, when compared to metal and stone as everyday materials, is the limited range of temperature
131 within which they can be used. Therefore extensive research has been undertaken during the last twenty years to improve the thermal stability of existing polymers and to synthetize new thermally stable polymers. The number of papers published in this field increases exponentially each year and exceeds one thousand at the time of writing; they mainly report the synthesis of new polymers and the results of thermogravimetric analysis. Also, many reviews have been published [ 275-2841. We will discuss in this section the various ways that can be used to improve the thermal stability of polymers. The synthesis and thermal behaviour of some typical heat-resistant polymers (sometimes commercially available) will then be given. The volatilization of these materials has very seldom been thoroughly studied: orders of reaction, activation energies and pre-exponential factors have generally not been determined. Therefore the thermal stability of the polymers will be characterized in an arbitrary way for the purpose of comparison. It must be stressed, however, that the physical properties of a polymer are at least as important for use at high temperature as the volatilization characteristics; an infusible polymer is very difficult t o process, and a heat resistant polymer with a low softening temperature is often useless. The softening temperature corresponds to the loss of mechanical properties. It can be measured by the standard heat deflection test. A t the end of the section, some recent studies on the thermal degradation of polymers with aromatic rings will be reviewed, but extensive discussion of results described in the literature on thermostable polymers is not possible within the scope of this chapter. Some improvement in the physical properties of polymers with respect to temperature can be obtained by increasing the chain interactions. The useful temperature range can also be increased through greater crystallinity. Low density amorphous polyethylene has a heat deflection temperature at 66 lb/in2 (ASTM-D648) of 38-50°C, whereas it is 60-88°C for crystalline high density polyethylene. Since isotactic polymers are generally more crystalline, they usually have better mechanical properties than the corresponding atactic polymers. The thermal stability, however, is not affected by crystallinity if volatilization occurs above the melting point. End groups and weak links, which are responsible in many cases for thermal degradation, depend on the methods used for polymer synthesis. Therefore the rate and mechanism of volatilization are often very different for isotactic and atactic polymers. The useful temperature can be improved by the intermolecular attraction induced by polar groups between the chains. The heat deflection temperature for high density polyethylene (-CH, -CH,-), , polyoxymethylene - ( C H , +),and nylon-66 (-R-CO-NH-R'-)n are, respectively, 6O-8O0C, 170°C and 185°C. The nature of the side chains has a profound effect on the thermal behaviour of polymers as reflected by the melting point (Table 18). The data in this table also show that branching of the side chain in the References pp. 165-1 73
132 TABLE 18 MELTING POINTS O F CRYSTALLINE POLYMERS Melting point ("C)
Polymer 3 C H 2 -CH2 -)n -( CH2-O-), -( R-CO-NH-R'
In
-( CH-CHz-),
I
A -( CH-CH2 ),
I
R
(CHR 7H-CH2)n
3
I
High density polyethylene Polyoxymethylene Polyhexamethylene adipamide (Nylon 6-6) A = CH3 polypropylene A = C1 polyvinylchloride A = C6Hs polystyrene A = CN polyacrylonitrile R = CH3 polypropylene R = C2Hs poly(butene-1) R = C3H7 poly(pentene-1) R = C4H9 poly(hexene-1) R=R'=H poly( butene-l) R = CH3R' = H poly(3-methylbutene-1) R = C6H5R' = H poly(3-phenylbutene-1)
138 175 255-265 198-212 21 2 230 317 198-212 (116) 124-142 130 55 (116) 124-142 300 360
CH~R'
position to the double bond raises the melting point because it restricts the freedom of rotation. The most thoroughly investigated and most efficient route t o high temperature polymers involves increasing the useful temperature by chain stiffening. If an inflexible ring is built into the backbone, softening temperature can be raised significantly. Typical ring systems that have been introduced into polymer chains are given in Table 19. They can be of the aromatic hydrocarbon or heterocycle type. TABLE 1 9 INFLEXIBLE RINGS FOR CHAIN STIFFENING
Polyphenylene
Poly thiazole
Polydiazine
Polyoxadiazole
Polydiimide
Polytriazine
Polytriazole
Pol y imide
Poly imidazopy rrolone
133 13.2 POLYMERS CONTAINING AROMATIC HYDROCARBONS IN THE MAIN CHAIN
Some of the most important structures are summarized in Table 20. Many of them are commercial products. Their stability is often very good. Representative data are given in Fig. 68. TABLE 20 STRUCTURES OF SOME AROMATIC POLYMERS
poly -p-phenylene
polytolylene n
poly-p-xylylene
polyphenylene oxide
azopolymers
polysulphone
polysulphide
Linear p-polyphenylene is thermally stable and crystalline, but brittle, insoluble and infusible. Therefore there has been considerable effort to insert flexible links such as -0-, -CO-, -NH-, 0-CO--, -0-C0-0, N,, -S- or SO2 without loss of thermal stability. Poly-p-xylylene has a melting point of 4OO0C and its mechanical properties are good. It is, however, insoluble and cannot be thermoprocessed. If one or more References p p . 1 6 5 - 173
134 hydrogens of the aromatic ring are substituted by halogen, acetyl, alkyl or ester groups, more soluble polymers are obtained. Various copolymers have also been synthetized. Poly-p-phenylene oxide is insoluble. Substitution in the aromatic ring increases the solubility but decreases the softening temperature. Thermal stability is sometimes but not always lower. The chloro-derivatives are usually more stable than the bromoderivatives. The azopolymers are crystalline, cannot be thermoprocessed and are always coloured. 1001
90
-
$
00-
kn
70-
2
60-
c
E
c
0
1 N
50-
5
c 40-
0
c
-
30-
c
g 200
-200
n
1
1
I
250
300
350
400
Tern perature('
I
I
1
450
500
550
C)
Fig. 68. LOSSin weight of various polyphenylene-type polymers after heating in vacuo for 2 h at different temperatures [ 2761. A, poly-p-2,3,5,6-tetramethylphenylene methylene; B, poly-9,lO-anthrylene ethylene; C, poly-p-2,5-dimethoxyphenylene ethylene; D, poly-p-2,5-dimethylphenylenemethylene; E, poly-p-phenylene ethylene; F, poly-p-2,3,5,6-tetramethylphenyleneethylene; G , poly-2,6-naphthylene ethylene; H, poly-p,p'-diphenylenemethylene; I, poly-m-phenylene;J, poly-p-phenylene.
Many thermoplastics can be obtained by condensation of bisphenol A with various reactants. Typical examples are given in Table 21. These polymers are generally transparent plastics. Polycarbonate prepared from bisphenol A has high toughness, dimensional stability and self-extinguishing properties. Many other polycarbonates, not derived from bisphenol A, have been synthetized. Thermal stability is improved when the backbone does not contain aliphatic groups. The >C(CH,), groups, in fact, constitute the weakest link. This is true for all the polymers containing aromatics in the main chain. Weight loss starts at 375-458OC according to the chemical structure [ 2851. Polysulphones from bisphenol A have high heat deflection temperature and good oxidation resistance and mechanical properties. They can be used up t o 260°C. Polyphenylene sulphides are semitransparent and melt at 270-29OOC. They show little volatilization
135 below 400°C [286, 2871. Various polyaromatic esters and amides have also been prepared. Para-linked polymers are always more stable than the meta isomers. Ortho-linking always results in a decrease in thermal stability. TABLE 21 POLYMERS FROM BISPHENOL A
polysulphonate
13.3 HETEROCYCLIC POLYMERS
A large variety of polymers containing heterocyclic rings in the chain have been synthetized. Some of these structures are given in Table 22. The most stable compounds are those that do not contain aliphatic groups in the chain. A very high thermal stability is obtained from this class of polymers: many of them are commercially available. There have been various studies of the mechanism of degradation. Some data on the thermal stability of the most representative polymers are given below. References u p . 165-1 73
TABLE 22 THERMAL STABILITY (TEMPERATURE A T WHICH DECOMPOSITION BEGINS) OF SOME POLYMERS CONTAINING HETEROCYCLES IN THE CHAIN [280] Chain unit and polymer
Starting materials Dicarbox ylic acid or deriua tiu e
Second component
Diphenyl terephthalate
Benzene-l,2,4,5-tetraamine
Diphenyl isophthdate
Benzene-l,2,4,5-tetraamine
Diphenyl terephthalate
Biphenyl-3,3',4,4'-tetraamine
Temp. ("C,
5 00
5 00
550
Poly-2,2'-p-phenylene-5, 5'-bibenzimidazolyl
Diphenyl isophthalate
Biphenyl-3,3', 4,4'-tetraamine
550
w
w
Diphenyl isophthalate
490
Diphenylmethane-3,3', 4,4'. tetra-amine Poly-2,2' -rn-phenylene-5,5'-dibenzimidazolylmethane
Diphenyl isoph thalate
4 90
2,2'-DimythyIbiphenyl3,3 ,4,4 -tetra-amine
Poly-4,4'-dimethyl-2,2'-rn-phenylene-5, 5'-bibenzimidazolyl
Diphenyl isophthalate
Diphenyl isophthalate
2,2'-DimethyI,diphyylmethane-3,3 ,4,4 -tetraamine
4, 4'-Diaminobiphenyl3,3 -diol
400
Poly-4,4'-dimethyI-rn-phenylene-5, 5'-dibenzimidazolylmethane
-
c
<
:
~
:
>\ c
~
500
Poly-2,2'-rn-phenylene-6,6'bibenzooxazolyl
a
$ I'
Diphenyl isophthalate
3', 3"-Diamino;2, a-diphenylpropane4 , 4 -diol
II
Poly-2', 2"-rn-phenylene-2,2-dibenzoxazol-5', 5"-ylpropane
2
-
500
b
P
o,
7
b
c;
Pyromellitic anhydride
Phenoxy benzene-pp'-diamine
450 Poly -pp'-phenoxyphenylpyromellitimide
TABLE 22-continued Starting materials Dicarboxylic acid or derivative
Second component
Pyromellitic anhydride
p-Diphenoxybenzenep'p''diamine
Chain unit and polymer
Temp. ("C)
-N N c o C o \
'co
C0lN
~
-
-
- 0
-
Poly-p-diphenoxybenzene-p>" -pyromellitimide
Pyromellitic anhydride
450
Anilinephthalein
0 Polydiphenylphthalide-pp'-pyromellitimide
Pyromellitic anhydride
Biphenylylene-pp'-dihydrazine
400
Poly-N-p-benzidinopyromellitimide
Diphenyl isophthalate
550
4,4'-Diaminobiphenyl-3,3'dithiol Poly-2,2'-m-phenylene-6,6' -bibenzothiazolyl
~
Pyromellitic anhydride
Benzene-l,2,4,5-tetramine
p-Bisdiazoxylene
p-Diethynylbenzene
450
0 Polybenzimidazopyrrone
N-N
ok,$j-
550
H Poly-5-p-phenylenepyrazol-3-yl
N-N Terephthaloyl chloride
Terephthalodihydrazide
'0'
-
400
Poly-5-p-phenyleneoxadiazol-2-yI
N-N
g'
Isophthaloy 1 chloride
Isophthalodihy drazide
40,AfJ
400
Poly-5-rn-phenyleneoxadiazol-2-yl b b-
VI o,
I
k
y
menoxybenzenepp'-dicarbonyl chloride
Phenoxybenzene-ppldicarbohydrazide
430
Poly -5-ppr-phenoxyphenyleneoxadiazol-2-yl
TABLE 22-continued Starting materials Dicarbox ylic acid or derivative
Chain unit and polymer
Temp. ("C)
Second component
N-N
Polyisophthalohydrazide
Aniline
4 .I N , y ) -
45 0
C6H5 Poly-4-phenyl-5-rn-phenylenetriazol-3-yl p-Diglyoxyloylbenzene
Biphenyl-3,3', 4,4'tetra-amine
470
Benzidine-3,3'dicarboxylic acid
p-Phenylene di-isocyanate
540
Poly-1, l', 2, ?,3,31,4,4r-octahydro-2,2',4,4'-tetraoxo-3,3 -p-phenylene-6,6'-biquinazolinyl
141 Polyimide. A typical polyimide results from the condensation of The final insoluble pyromellitic dianhydride and bi~-4(aminophenyl)ether. polydiimide is obtained by dehydration of a soluble polyamic acid, namely, 0 II
0
0
pyromellitic dianhydride
bis-4(aminopheny1)ether
Soluble polyamic acid
Insoluble polydiimide This commercial polymer is stable for a year at 275°C and can be used for 200 h at 358°C and 10 min at 377°C. At 600°C,volatiles are formed. They include CO, CO,, H,O and H, [288]. The activation energy of decomposition in vacuo in the range 585-632"C was estimated [289]to be 74 kcal mole-'. The purified polymer decomposes primarily by breaking of the amide group. Various other polyimides have been synthetized.
M-Si'
Polyoxadiazole. A typical polyoxadiazole is [--AI-C,~,C--] but various others have been synthetized. Some polyoxadiazole films have measurable fibre properties even after prolonged heating to a temperature of 400°C in air or nitrogen [290].Aliphatic linked polymers are of lower stability. Polybenzimidazole. Polymers of the type
References p p . 165-1 73
142 are commercially available. They can be used for 10 min at 650°C and 300 h a t 320°C. If the phenyl group is substituted in the 1-4 position, the weight loss is 1%after 1 day in nitrogen at 400°C. If the sample is then heated for one hour at successively higher temperatures the cumulative weight losses are as follows: 2% at 45OoC, 2% at 5OO0C,1.7%at 550°C and 4.7% at 600°C [291]. The polymers also show remarkable resistance to oxidative degradation. Polybenzothiazole. The polymers of general formula
can be used for 10 min at 538°C and 200 h at 330-343°C [292]. Table 22 summarizes data on the thermal stability of various other heterocyclic polymers. Aromatic ladder polymers. Ladder polymers which withstand red heat are obtained by cyclization of polyacrylonitrile [ 293, 2941 :
The softening point determined by thermomechanical methods may be as high as 500°C. A true ladder polymer can also be obtained by condensation of an aromatic tetracarboxylic acid or a dianhydride with an aromatic tetramine. An example is
ladder structure
143 By varying the heating rate, cyclodehydration takes place, giving either a semi-ladder or ladder structure. The semi-ladder polybenzimidazolone is soluble in some solvents. The ladder polymer subsequently formed is insoluble. This type of polymer is stable to 450-650”C in nitrogen. 13.4 MECHANISM OF DEGRADATION OF SOME POLYMERS CONTAINING AROMATIC RINGS IN THE CHAIN
The thermal behaviour of five thermostable polymers has been compared by Davis [ 2951. These are Poly [ 2,2-propane-bis-(4-phenylcarbonate)]
PC
1, Poly [ 2,6-dimethylphenylene ether]
PPO
A polysulphone prepared from bisphenol A and 4,4’-dichlorodiphenylsulphone PS
A polyarylate prepared from terephthaloylchoride and bisphenol A
TD
References p p . 165-1 73
144 A polyarylate prepared from terephthaloylchloride and phenolphthalein TPP
Gel is formed with all the polymers. The 3'6 gel formation as a function of time is given in Fig. 69. Gel does not form in the polyesters and polycarbonates if the volatile products are not removed. The relative
Time (h)
Fig. 69. Gel content of polymer PC, PPO, TP, and TD as a function of time at 37OoC and of PS at 38OoC [ 2951.
Temperature ("C)
Fig. 70. Relative gas evolution of five aromatic polymers heated in nitrogen at 32 degC min-' [ 2951.
145 TABLE 23 RATE OF GAS EVOLUTION AND GAS COMPOSITION FOR THE POLYMERS AT 38OoC [295] Polymer
PS TD PPO PC TPP
Rate of gas evolution (em3 at NTP per g polymer)
co
coz
0.3 1 4 4 5
9 34.5 7.2 3 79
59 4 95 20.9
% Gas composition -___
I
CH4
CzH6 Hz
35 5 44 2 -
-
0.3 2 -
3.2 0.2 41.4 0.1
so2
42.2 -
-
C6H6
C7Hs
1 -
3.6 0.1 1.3 -
m ~ o u n tof volatiles formed is given in Fig. 70 and their composition in Table 23. If volatile and gel formation are considered, it appears that polysulphone is the most stable of these five polymers. In these highly aromatic polymers, it is the nonaromatic linkages which are the most labile. The large amount of CO, formed in polycarbonates indicates that the carbonate linkage is the weakest. Methane formation in polycarbonate, polyarylate and polysulphone would result from a loss of CH; followed by hydrogen abstraction from the isopropylidene moiety. The large yield of H, and CH, in the degradation of the polyphenylene ether is indicative of the lability of the CH, groups on the aromatic ring. A detailed study of the same aromatic polysulphone (PS) has been reported by Davis [296]. The gas composition does not change with the time of heating. Volatile liquid and solid products have been separated and identified by gas chromatography and mass spectrometry; the results are given in Table 24. After three hours heating, a gel is formed. The amount of gel is not affected by the presence of the volatile pyrolysis products. If the theory of Charlesby-Pinner is applied to the gel formation data, a straight line with a positive intercept of 0.35 is obtained. This means that chain scission also occurs. The rate of SOz evolution is in agreement with the results of Levy and Ambrose [297] on the pyrolysis TABLE 24 VPC/MASS SPECTROGRAPHIC ANALYSIS OF THE VOLATILE LIQUID AND SOLID PRODUCTS OF HEATED POLYSULPHONE [296] Product
Relat. Product amount
Phenol p-Cresol p-Ethyl phenol p-Isopropylphenyl phenol Bisphenol A
200 1 2 2 1
<
Relat. amount
Diphenyl ether p-Tolyl phenyl ether p-Ethyl diphenyl ether p-Isopropenyl diphenyl ether Two isomers of tolyl(ethy1-pheny1)ether
5 20 5 20 10
References p p . 165-1 73
146 of diphenylsulphone. This led Davis [296] to propose a similar mechanism for SOz production in the polymer; namely,
radical abstraction e.g. CH3
...
radical-radical recombination
4 eo -o I -
or
radical addition to other polymer chains
CH3
CH3 A e e H 3 I CH3 Subsequent breakdown of the isopropylidene linkage at the chain ends produced by (1)would account for the ether products; namely,
. .. -
(_>.e& CH2
and 2 isomers of H3C I CH3 The mechanism of formation of phenol is not clear. It may arise from pyrolysis and interaction of phenolic end groups. The detailed data on the thermal stability of the poly[2,2-propanebis(4-phenylcarbonate)], PC, have been reviewed by Davis and Golden [298]. If the degradation products are not removed, a decrease in molecular weight obeying first-order kinetics, with an activation energy of 39 kcal mole-', is observed. In an evacuated system gelation occurs with an activation energy of 27 heal mole-'. The difference between degradation in a closed or in an evacuated system is due t o ' the
/ \
147
0
6
4
2 Time ( h )
Fig. 71. Amount of volatile products evolved from polycarbonate at 36OoC with respect to time: A, COz ; B, bisphenol A; C, phenol; D, 2-(para-hydroxyphenyI)-2phenylpropane; E, CO; F, CH4 ; G , diphenyl carbonate [ 2981.
competition between condensation and hydrolysis reactions. The most important volatile liquid and solid products formed are phenol, diphenyl carbonate, and 2(4-hydroxyphenyl)-2-phenylpropane. The gaseous products evolved are given in Table 23 and their rate of evolution in Fig. 71. The mechanism of degradation of the polycarbonate was elucidated by the detailed study of a model compound diphenylcarbonate. The following degradation paths are reported to justify the formation of the major volatiles, C 0 2 and bisphenol A, crosslinking and chain scission. Chain scission in closed systems occurs by step (6); gel is formed by step (8);namely,
COOH
G
- 4 3 - 3 4 3 - ( ; COOH
G
o
H2O + o
o c
o
; 4
3
e
Z
o F
-
2
-
o -
0
+
H
2
0
0
H + CO,
(6) References PP. 165-1 73
148
(7)
COOH
/coo0\
/
0
0
+H
\o /
e + C02
The liberation of gaseous compounds during pyrolysis of polycarbonate has also been studied by Kammermaier [299]. Three polyphenylene oxides were investigated by Powell et al. [300]. These are
(a) Poly (1,3-phenylene oxide) L
CH3 (b) Poly( 2,6-dimethyl-l,4-phenyleneoxide) [ - O p ] n
(c) Poly (2,5-dimethoxy-l,4-phenylene oxide)
149
I
1
100
I
200
300
400
500
600
700
800
900
Temperature ("C)
Fig. 72. Thermogravimetric analyses of poly( 1,3-phenylene oxide) [ 3001. 1, Aminco thermobalance, vacuum 0.3 mm, 3 degC min-' ; 2, Chevenard thermobalance, nitrogen, 24 degC min-' ; 3, Chevenard thermobalance, air, 24 degC min-'
.
Polymer (a) has number average molecular weight of 7.200, and the thermogravimetric analysis is given in Fig. 72. The major weight loss occurs between 500 and 600°C. The analysis of volatile products at different temperatures has been performed (Table 25). Some products sublimed; and, according t o mass spectral analysis, they may correspond to the chain fragments
4
HO
OH
TABLE 25 ANALYSES OF VOLATILES FROM POLY(1,B-PHENYLENE OXIDE [300] Temp. mnge
("C) ~~
H2
CH4
H2O
CO
C02
C6H6
26.0 37.3 61.5
7.3 7.2 7.5
32.8 16.4 7.7
23.2 35.1 21.8
9.6 3.7 1.4
1.1 0.3 0.1
Weight volatiles (%)"
Total weight loss (%)a
~~~~
20-450 450-550 550-620 ~~
a
Volatile products (mole %)
~
~~
~
3.7 5.8 3.9
55.5 7.0 3.9
~
Of starting material. References p p . 165-1 73
150 The composition of the residue is C6H1,600,1. A mechanism including chain breaking at the ether linkage has been proposed. Subsequent reactions of the phenoxyradical give crosslinking and formation of C 0 2 , CO, CH4, H2 and H20. The proportion volati1e:sublimate:residue is about 13%: 66% : 2196, as determined from isothermal experiments at 450, 550 and 62OoC. The polyether (b) substituted by methyl groups degrades about 100 degC below the Qnsubstituted polymer. Much more methane is formed. Scission of the methyl group is thus an important process which adds to random chain scission. If the aromatic ring is substituted by methoxygroups (polymer (c)), considerable weight loss occurs below 30OoC. Methane and methanol are produced and indicate that CHj and .0CH3 radicals are formed by side chain scission. Three aromatic polyesters were studied by Powell et al. [301]; namely, (i) Poly-p-phenylene isophthalate-co-terephthalate
r o
1
(ii) A condensation polymer from 4,4'-dihydroxydiphenyldimethylmethane and isophthalic acid r
1
(iii) A condensation polymer from 4,4'dihydroxydiphenylether and 5-amyloxyisophthalic acid
The highest rate of degradation of polyester (i) is observed between 500 and 55OoC. Differential thermal analysis indicates that decomposition occurs around 465OC. CO and C 0 2 are the major products formed in this
151 TABLE 26 ANALYSES OF VOLATILES FROM POLY@-PHENYLENE ISOPHTHALATE-COTEREPHTHALATE) [ 3011 Temp. range ( OC)
Weight volatiles
Volatile products (mole %) HZ
CH4
H2O
co
(%)'.)a
~
20-4 50 450-550 550-620
2.0 10.9 22.7
0.4 1.8 3.6
0.4 0.7 1.8
61.7 57.9 50.3
34.8 27.2 21.0
(%la
C6H6
c02
~~
~~
0.7 1.5 0.6
Total weight loss
29 8 3
~~
52.3 8.0 3.2
Of starting material.
first step (Table 26); they result from breakdown of the ester group. Hydroquinone appears in the sublimate. A t higher temperatures, formation of hydrogen and methane'is indicative of some ring breakdown. After removal of the major part of the ester linkages, the principal reaction is believed to be the formation of free radicals that recombine t o form polyphenyl and polyphenylether structures. Polymers (ii) and (iii) degrade about 100 degC below polymer (i). The major solid product of polymer (ii) is bisphenol A; CO and COz are the most important gaseous products. The mechanisms of degradation of polymers (i) and (ii) thus present important similarities. With polymer (iii), the amyloxy group is almost completely removed below 350°C. Weakness of the alkoxy linkage on aromatic groups has previously been reported for polyethers. The thermal behaviour of sulphur containing polymers has been reported on [ 3021. The major breakdown in poly( 1,Cphenylene sulphide)
occurs around 500" C. Hydrogen sulphide is the predominant volatile product at the lower temperatures and hydrogen at higher temperatures. A colourless, liquid to waxy condensate also separates. The structures suggested by mass spectral analysis to be present are
References p p . 165-1 73
152 The following simplified scheme represents the most important reactions. The primary step is cleavage of carbonsulphur bonds. Above 45OoC, the evolution of hydrogen becomes very important and results in extensive crosslinking in the residue [ 3021 .
I I The polysulphonate prepared by condensation of diphenylether-4-4'disulphonylchloride and 4,4'-dihydroxydiphenyl; namely,
decomposes at relatively low temperatures. Loss of weight becomes appreciable at 300°C. The maximum rate of SO, evolution is observed in the range 250-350°C. A review and some new results on the thermal degradation of poly-p-xylylene have been presented by Jellinek and Lipovac [ 3031. Little volatile material is formed but appreciable amounts of dimer, trimer, tetramer and pentamer were isolated. Typical vacuum volatilization curves are given in Fig. 73. It has been proposed that the mechanism consists of random chain scission a t abnormal structures in the chain, followed by a depropagation reaction resulting in low molecular weight polymer but very little monomer.
153
Tirne(rnin)
Fig. 7 3 . Typical vacuum volatilization curves (mo = 2.0 X monomeric unit moles); ( i ) 408OC, (ii) 436OC, (iii) 424OC, (iv) 45OoC, (v) 515OC [303].
14. Copolymers and polymer blends 14.1 COPOLYMERS
The presence of a comonomer can deeply affect the thermal behaviour of polymers. A comonomer can in some cases confer stability but in others may render a homopolymer unstable. Some important systems will now be described and discussed; a review on the subject has been published by Grassie [ 3041. 14.1.1 Destabilized homopolymers
( a ) Polymethacrylonitrile and polyacrylonitrile containing acrylic acid It was shown many years ago that if some methacrylic acid is copolymerized with methacrylonitrile, the discolouration reaction References p p . 165-1 73
154 observed with pure polymethacrylonitrile is accelerated [ 305-3081. According to the authors, the effect of the acid is to initiate the condensation of neighbouring nitrile groups according to
The conjugated carbon-nitrogen sequences formed are responsible for the observed colour. Radicals do not seem to be involved in this reaction. Identical effects are observed when acrylonitrile is copolymerized with acrylic acid. ( b ) Polyacry lonitrile containing methylvinylketone
The thermal degradation of polymethylvinylketone is a random reaction in which water is liberated from pairs of adjacent units resulting in cyclization and conjugated sequences of limited length [309]. When methylvinylketone units are incorporated into polyacrylonitrile, the rate of thermal colouration is greater than with pure polyacrylonitrile [309]. The acceleration effect of methylvinylketone units has been ascribed to their behaving as initiators according t o one of the following
155
I
1
I
I
Propagation can apparently pass through methylvinylketone units, conjugation being preserved. ( c ) Copolymers of vinylchloride and vinylacetate [310] The rates of production of volatile material from polyvinylacetate, polyvinylchloride and vinylacetate-vinylchloride copolymers, covering the entire composition range, have been compared by thermal volatilization analysis. It has been found that, at both extremes of the composition range, incorporation of the comonomer unit induces destabilization. Minimum stability occurs for composition of approximately 40-50 mole 7% vinylacetate. The rate of volatilization as a function of the composition of the copolymers is given in Fig. 74. The results were confirmed by a study of the thermal degradation in tritolylphosphate solution. The stability of the copolymers is a minimum at 30-40 mole 7% vinylacetate. HC1 and acetic acid catalyse the degradation of the
I
,
20
,
40 60 Mole % V A
00
L
0
Fig. 74. Compaf;ison of rate of volatilization for copolymers of vinyl chloride and vinyl acetate at 248 C as measured by Pirani reading, with copolymer composition, for heating rate of 5 degC min-' . References p p . 165-1 73
156 copolymer. Many other organic acids were found to have no catalytic effect. The UV spectrum is quite similar t o that reported for pure PVC. The variation of absorbance at three wavelengths with mole % vinylacetate in the copolymer, for 5%degraded samples, is given in Fig. 75. It is apparent
0
I
I
20
40
60
a0
0
Mole % V A
Fig. 75. Comparison of absorbance by copolymers of vinyl chloride and vinyl ace ate at three maxima in the UV spectrum for 5% degraded samples with copolymer composition.
that for compositions in the range 20-30 mole % vinylacetate longer sequences are formed. Grassie et al. [ 3101 proposed that both the over-all rate and the development of conjugation are increased considerably by some heterogeneity of the chain units. One or both units are labilized by the immediate proximity of a unit of the opposite type. ( d ) Copolymers of styrene and acrylonitrile [311] When acrylonitrile units are copolymerized into polystyrene, the rate of volatilization measured by thermal volatilization analysis increases in direct proportion t o the acrylonitrile content. From the changes in molecular weight that occur during the reaction, it is clear that the primary effect of the acrylonitrile units is to cause an increased rate of chain scission but the unzipping process which follews chain scission is not greatly affected. Acrylonitrile monomer thus appears among, the volatile products. The rate coefficient of the chain scission process associated with acrylonitrile units is about thirty times that for “normal scission” in styrene segments of the polymer chain. The proportion of chain fragments (dimer, trimer, etc.) increases with acrylonitrile content; these fragments also incorporating acrylonitrile units. Yellow colouration develops in the residues from copolymers with high acrylonitrile content
157 at advanced stages of degradation. Infrared and ultraviolet analysis suggest that this is due t o conjugated unsaturation in the polymer chain which may be associated with liberation of hydrogen cyanide. ( e ) Copolymers, methylmethacrylatel-chloroacrylonitrile and styreneh-chloroacry lonitrile a-Chloroacrylonitrile induces instability into polystyrene and polymethylmethacrylate [312]. With both copolymers as with the homopolymer of a-chloroacrylonitrile, the threshold degradation temperature is around 14OoC, which suggests that the same initiation process is involved. Random chain scission occurs in both copolymers; methylmethacrylate, hydrogen chloride and some a-chloroacrylonitrile are liberated during the degradation of the copolymer of methylmethacrylate/a-chloroacrylonitrile, but styrene is not evolved from the second copolymer. Grassie and Grant [ 3121 proposed that initiation occurs at the C-Cl bond of the a-chloroacrylonitrile unit, and the mechanisms suggested were as follows. For the m$thylmethacrylate copolymers CH3 c1 I I -CH2+-CH2-C
I
COOCH,
I
CN
CH3
I
____+
I COOCH,
CH3 I -CH,-C-CH
I
CH3 I 2-&CH2-C-----
COOCH3
CH3
I -CH2 <-CH I
I
CN
COOCH3 CN
I
CH3 I --.CH,-C-CH=C-CH;
I
COOCH,
CH3
=C-CH,-C-
I
I
COOCH, CN
+ c1*
I
I
I I
+ HC1
COOCH3
CH3 .I + C-
7
I
COOCH3
1
monomer References pp. 165-1 73
158 For the styrene copolymers
I
CN Ph Ph I -CH2-CH-CH2-&CH2+&H-
+ C1-
I
CN
I
Ph
Ph
I
-CH2-CH-CH=C-CH2-CH-
I
I
+ HC1
CN The two C-C bonds in the /3 position t o the ethylene unsaturation and the aromatic ring are much reduced in strength compared with normal C - C bonds. Scission of one of these bonds occurs and stable molecules are formed by disproportionation of the radicals: Ph
I
-CH,--CH--GH;
Ph
I
+ *CH--CH=C-
I
CN Ph
I
-CH2--C=CH2
Ph
I
+ CHZ-CH=CI
CN
14.1.2 Stabilized homopolymers
( a ) Poly methylme thacry late containing acrylonitrile
Grassie and Melville [313] observed that the presence of acrylonitrile in polymethylmethacrylate causes an induction period (Fig. 76) in the production of methylmethacrylate monomer at 220°C. During this induction period the molecular weight decreases rapidly and tends to a limiting value close to that corresponding t o the average distance between acrylonitrile units. Later, the rate of monomer production builds up and passes through a maximum after 2.3 hours heating. This led Grassie and Melville to believe that the acrylonitrile units constitute “weak links” in the polymer structure.
159
B'
220°C
Time (min)
Fig. 76. Rate of evolution of monomer at 22OoC from a methyl methacrylateacrylonitrile copolymer containing 0.24 mole % acrylonitrile (mol. wt. = 617,000) [313].
This system was recently reexamined by Grassie and Farish [314] and the work extended t o copolymers containing higher proportions of acrylonitrile. The occurrence' of induction periods and rate maxima reported by Grassie and helville [313] at 220°C was confirmed. A comprehensive study of the degradation a t 280°C was performed. The changes in molecular weight with the extent of volatilization are given in Fig. 77. They are independent of the composition of the copolymers. The induction period observed at 22OoC for the volatilization has disappeared at 280OC.
%volatilization
Fig. 77. Changes in mol. wt. with volatilization at 28OoC of methyl methacrylateacrylonitrile copolymers. ( 0 , 410/1; 0, 40/1; 0 16/1; 0 , 8/1) [314]. References p p . 165-1 73
160 A unified picture of the reaction mechanism at 220 and 280°C was proposed by Grassie and Farish [314]. At 220°C the degradation is initiated at unsaturated chain ends but radical depolymerization cannot pass through acrylonitrile units. Degradation is thus stopped at the first acrylonitrile unit, thereby accounting for inhibition of monomer production at an early stage in the reaction. Chain scission, however, occurs at random at a very slow ra$e at 22OoC. This random scission produces radicals which disproportionate in a cage. Unsaturated chain ends are thus formed at this stage; namely,
The concentration of these unsaturated chain ends increases and, since they are unstable at 220"C, the rate of volatilization is accelerated. Since depolymerization cannot pass through acrylonitrile, the chain length of the residue is the average distance between adjacent acrylonitrile units. A t 28OoC there are two fundamental changes in the nature of the reaction. First, random chain scission to depropagating radicals occurs. Secondly, depropagation can pass through the acrylonitrile units which are then liberated as monomer. Thus, the stabilization effect of acrylonitrile observed at 220°C is lost at 280°C because acrylonitrile units are liberated in the depropagation process.
( b ) Polymethylmethacrylate containingphenylacetylene Comparison of the TVA thermograms of the copolymer and of pure polymethylmethacrylate [ 3151 shows that end initiation at polymethylmethacrylate units is inhibited in the copolymer. Degradation above 300°C is the result of scission at the unsaturated phenylethylene units. ( c ) Poly me thy lme thacry late containing meth y 1 and higher acry lates
By comparison with pure polymethylmethacrylate it was shown that volatilization in the neighbourhood of 300°C is almost completely eliminated [315, 3161 (Fig. 78). The acrylate units in the chain exert a blocking effect on the depolymerization process, as in the case of acrylonitrile copolymers. The high temperature peak, however, is not affected by the presence of acrylate since the depropagation process can pass through the second monomer and methylacrylate appears among the volatile products. The property of blocking the end-initiated monomer producing reaction is common to straight chain acrylate monomers.
161
Temperature ("C) of P M M A
Fig. 78. Effect of copolymerization with methyl acrylate on the thermal stability TVA thermograms for 26/1(dashed line), and 8/l(dotted line) copolymers, compared with that for polymethylmethacrylate of comparable molecular weight (full line) [316].
( d ) Copolymers of methylmethacrylate with styrene The degradation behaviour of these copolymers is interesting in view of the fact that both homopolymers undergo depolymerization t o yield monomer. Copolymers containing 50% and 20% styrene have been prepared [316]. The TVA thermogram of pure polystyrene is independent of molecular weight, and for a heating rate of 10 degC/min, a single peak with a maximum at 418OC is observed. When the copolymers are compared to polymethacrylate of comparable molecular weight, an important improvement in stability is observed in the copolymers (Fig. 79). The end-initiated reaction is eliminated. It is improbable that styrene exerts a blocking effect on the depropagation
Temperature ("C)
Fig. 79. Effect of copolymerization with styrene on the thermal stability. TVA thermograms for 4/1 (dashed line) and 1/1 (full line) copolymers, compared with that for polymethylmethacrylate of comparable mol. wt. (dotted line) [ 3161. References p p . 1 6 5 - - 1 7 3
162 reaction as observed for acrylonitrile, since polystyrene depolymerizes on heating, whereas polyacrylonitrile does not. Grassie and Farish [ 3171 have attributed this effect to the absence of terminal double bonds in the copolymers, which was previously demonstrated by Bevington et al. [ 3181. 14.2 POLYMER MIXTURES
The nature of the interactions between polymers in a blend depends strongly on the physical state of the system. It is well known that polymers are generally incompatible in the solid state; films cast from a solution containing a mixture of polymers are, in fact, usually opaque. It has been shown by microscope methods that incompatible pairs can, in certain cases, be included in a two-phase system [319]. One polymer tends to form a continuous phase while the other is dispersed in that continuous phase in the form of micelles of dimension (1-15) x cm. The polymer blends described next have been obtained by freezedrying a solution of the mixture (Richards and Salter [320]) or by casting films from solutions (McNeill et al. [321-325]), Their physical state is, however, not defined.
( a ) Polystyrene-poly-a-methylstyrenemixtures The degradation of polye-methylstyrene is unaffected by the presence of polystyrene, but depolymerization of the latter polymer can be brought about at temperatures below 3OO0C by heating in the presence of polye-methylstyrene [ 3201. The rate of polystyrene volatilization then varies as an inverse function of the molecular weight of poly-a-methylstyrene. The system is heterogeneous, consisting of micelles of poly-amethylstyrene embedded in a polystyrene matrix. It has been suggested that the poly-a-methylstyrene chain unzips completely to a monomer radical which diffuses into the polystyrene matrix and attacks a polystyrene molecule.
( b ) Polypmpylene-polystyrene and polypropylene-polymethylmethacrylate mixtures [326] Polymethylmethacrylate and polystyrene are accelerators of the degradation of polypropylene. Acetone ex traction of the degraded polypropylene reveals the formation of graft and block copolymers. The presence of these graft copolymers can be used in the modification of the ability of polypropylene to retain dye.
( c ) Polymethylmethacrylate-polystyrene mixtures No interaction is observed in this case [321].
163
(d) Polyvinylchloride-polymethylmethactylatemixtures The thermaholatilization curves for this mixture are given in Fig. 80. The polyvinylchloride is slightly more stable in the mixture, but polymethylmethacrylate is initially less stable and gives monomer at temperatures corresponding to polyvinylchloride dehydrochlorination [ 3221. Subsequent breakdown of the remaining polymethylmethacrylate, under programmed heating conditions, is shifted to higher temperatures.
Sample temperature ("C)
Fig. 80. TVA curves for simultaneous degradation of PVC Breon 113 and PMM anionic, 5 mg of each, ( i ) unmixed, (ii) mixed. Film samples, heating rate 5 degC
All the observed features of the interaction of polymethylmethacrylate and polyvinylchloride, when degraded as a blend, are explained by two simultaneous reactions [ 322, 3231. (i) A chlorine atom from the degrading polyvinylchloride attacks polymethylmethacrylate according to C1' + M,
Pi Pi
+
--*
+
HC1+ P i
Hydrogen abstraction
P,:
Chain scission
+ M,- j
P,:- 1
+ MI
Depropagation
This chlorine atom attack accounts for the decrease in the molecular weight of polymethylmethacrylate, monomer production at abnormally low temperature and the delay in the dehydrochlorination of polyvinylchloride. This delay in dehydrochlorination is general for blends of polyvinylchloride and any polymer containing hydrogen atoms that can be abstracted by chlorine atoms. References p p . 165-1 73
164 (ii) HC1 abstracted from polyvinylchloride reacts with the methacrylate ester group and accounts for the anhydride structure shown in the IR spectrum of degraded polymethylmethacrylate. Degradation of the anhydride group results in formation of COz , CO and methane. These ring structures in the chain act as blocking units in the depolymerization and drastically reduce the zip length. A displacement of the curve to higher temperature, corresponding to volatilization of polymethylmethacrylate, is the expected result. This was further studied by gas chromatography of the volatile products, by IR analysis of the residual polymethylmethacrylate and by pyrolysis of polymethylmethacrylate in the presence of HCl [324]. The behaviour of graft copolymers [323] prepared by mastication of polyvinylchloride in the presence of methacrylate monomer is similar to that of a mixture of both polymers. This is in agreement with the mechanism suggested. ( e ) Polyvinylchloride-polystyrenesystem [ 3231
The thermal volatilization analysis of a mixture of polyvinylchloride and polystyrene is given in Fig. 81. The first peak corresponds t o the elimination of HCl and the second t o that of styrene. Dehydrochlorination is retarded in the mixture. The production of styrene is also retarded; styrene evolution, in fact, does not occur below 35OoC. This contrasts with the behaviour of polyvinylchloride-polymethylmethacrylate mixtures for which methacrylate formation accompanies dehydrochlorination. The observed behaviour implies that, if chlorine radical attack on polystyrene occurs, the polystyrene radicals produced are unable to undergo depolymerization at 30OoC. According to McNeill et al. [ 3231, structural changes leading to increased stability in the polystyrene must take place. This could also occur by addition of C1- t o the aromatic ring, yielding a cyclohexadienyl-type radical which is unable t o induce depolymerization of the styrene chain. Delay in dehydrochlorination is also observed with graft copolymers, but some chain fragments are produced a t the same temperature as is HCl. The behaviour of random copolymers is quite different. The copolymers become progressively less stable as the vinylchloride content increases. Initiation of styrene production, and the temperature corresponding to the maximum rate of volatilization, are both displaced to lower temperature. ( f ) Polyvinylchloride-poly-a-methylstyrene system [ 3231
The delay in dehydrochlorination is particularly marked in this system and a-methylstyrene production is initiated earlier than in polyvinylchloride-polymethylmethacrylate mixtures.
165
Tern perature ("C)
Fig. 81. TVA behaviour of PVC + PS ( 1 : 4 ratio by weight) degraded simultaneously in twin-limbed tube, in unmixed and mixed condition. Heating rate 10 degC min-' [323].
( g ) Polychloroprene-polymethylmethacrylatemixtures
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