iWrnwchin~ica
0
205
Acta. 29 (1979) 205-209
Elsevier Scientific
Publishing Company,
Amstcrdnm
- Printed in the Netlwrlands
REACTIONS - A PHENOMENONSTUDIABLE BY DTA?
OSCILLATINS
E. Koch and B. Stilkerieg Institut
fiir Strahlenchemie
im MPI fUr Kohlenforschung,
Stiftstr.
34-36
D-4330 Mu1heim a. d. Ruhr INTRODUCTION The fascinating sophisticated
phenomenon of chemical
interchange
of numerous reactions;
SOV-ZHABOTINSKIIreaction,there The aim of our first thermal characteristics with respect tried
to represent
catalytic
bursts
meters E = 67.2 dependence for
‘studies
effects
in
reaction
field
was
showing unimolecular and reactant acid
rates
of Ferroine
in an isothermal
and non-isothermal energy of z 100 kJ/mol-
to
behaviour.
find
corresponding
(time=min),
non-iso-
way (Fig.
Kijrbs (4)
of auto-
to activation
Using reactant by Field
the oscillation 1)
has para-
the A value showing a
as proposed during
(l-3).
reactions
- as a series
concentration.
and Ferroine
rather
steps
than to study particular
on the oscillatory
the U.V. absorption
vation
this
kJ/mol and lg A = 10.56
KBr03, KBr, malonic
studied
in the case of the BELOU-
the system - due to temperature
of catalyst
is caused by a.very
are 14 or even more particular
of this
to their
oscillations
amounts
(5),
we
at h = 550 nm
in a net acti-
resulting
.
2LOsec
.283
276
Fig.
1
293
303
Tin
K
U.V. extinction at 550 nm for4heating rate 2.0 K/min; KBr = 0.053; KBrO = 0.1; Ferroine = 5x10 ; malonic acid = 0.375 M; 1 M sulfun -2 acid
DTA studies. Using DTA equipment spezialized we recorded varied rate.
ca.
100 DTA curves
such as concentrations Although
measured
part
were.partially
of
the
reactions
with features of
bromate,
solutions
high,
for
there
in stirred
depending
bromide,
was oscillating, were no direct
solution
(6),
on the parameters
catalyst
and heating
and the calorimetric
enthalpies indications
206
to the oscillations ations
in rate
the lag of our equipment must smooth the fluctu-
since
(kinetic
The influence
cell
constant
Z 0.18 min-l).
of the bromate concentration
on the overall
shows -a step increase from small values ratio of bromide and bromate (0.05 1.1; Fig.
reaction
enthalpy
beginning
at an equimole-
cular
2).
passing
a maximumof Z 500 kJ/mol for demonstration
of the oscillations
crease/The acid
reason
‘chanistic tion
considering
the less
cf.
a tendency
of cooperative
ref.
processes
reactions
Fig.
3).
centration
for
the overall
of. bromous
heat. we tried
of the mechanistic
increasing
coordinates
from the region
small S, M Z M2_order)
reaction
1' S z SI), A + B = C; periodical of mixed-order
conse-
M X M2). x 10m4) leads
of the catalyst
to a continuous
and even to the zone of higher-order
reactions
consecutive
con-
decrease
to the second-order
of zone
when cat =
3)_
the heating
plots
to
of KBr and KBr03; M Z M
A and B) and ending in the region
CeCl3,6H20 (1:25
Increasing
a me-
bromate con-
S and M due to .a movement from the autocatalytic
confusing
while
termination
steps,
hand, we have found that an increase
l-25 x IOm3 M (Fig.
de-
exothermic
bimolecular
For Ferroine,
zone (equimolarity
(S Z SI,
On the other
the formation
data of particular
then passing through the AB zone (formal cutive
the
is a subsequent
is stronly
exothermic
(process A preferred;
move to the first-order change of processes
(1))
for
based on the corrected shape indices S and the reac-
M(7-8;
centration.causes
step,
which reduces
activation
peak analysis
type indices
there
through
between bromate and bromide is not. For even
of HBr02 may prevail
Before
bromate),
(B process;
A-reaction
BrOi concentrations,
reaction
(0.1
which is appropriate
is that the autocatalytic
via the BrO; radicals
the concurrent higher
a composition
After
rate
from 0.3 to 4.3 K/min partially
in the mechanistic
leads
to
diagram (Fig. 4). Obviously, the change
of the bromate concentration from 0.1 t.1 (standard) to 0.12 I1 (catalyst: Ferroine) course-
causes
the line
of increasing
rate
to show a reversing
For the moment, the question remains of how many steps have to be
set up to give chani sms , it
such a phenomenon_ Considering
is obvious
ing first-order, i4 values if
that concurrent
the heating
rate
concentration,
it was confirmed the ceric
oscillations
salt,
two-reaction
the prior
me-
of which be-
type, would lead to decreasing
is increased. activation
that there
wherein EB is minimum and nearly 68 kJ/mol for
possible
reactions,
the later of second-order
From the trend of the overall
tions,
heating
independent
80 kJ/mol for
may be favourably
energy,
EB, with catalyst
is a range (10T3 to 1O-4 M) of this Ferroine).
performed.
concentration. Under these
(E
-
conds-ii
207
kJ/mol 500-DH
X LOO_
Ferroine
X
300200-
IOO-
(KE3r concentration)
Fig. 2
0.15 M
K!3r03 -
Overall reaction enthalpy for different KBr03 concentrations \\
25-
T
‘i,
)$rder \ \ \
22-
103.M ZOklllmol-K
line
Ia16-
12m = 1.5 Klmin
10-
123.10-3
0.2
Fig. 3
Mechanistic
103M
I
0.6
I
Mechanistic
I
1.2
1.0
-
\
\
x Ferroine. Karol. 0; M V----- + Ferroine. KSrO: 0.12 M *----0 Cerlum. K&O, OlM Numbers: Heatmg rote \
! a5 0
1.0 shape index ___c
Fig. 4
I
0.8 shope index S -
points vs. catalyst concentration
I 30
I
0.f.
1.5
points vs. heating rate
1.2
208 Mechanism: A+C=B A+B=2B+D D=C+E
m = 1.38 K/min ICI, = 0.053 [AlO = 0.1
E 49.3 117.6 58.5
16.7 92.7 175.3
E/Ig A 7.06 5.97 6.97
359K
323K fig.
AH
5.
Computer reconstructionof an individualDTA curve by the use of
a three-step
mechanism
TABLE:. Activation
data
and
other
quantities
for the particularreactionsof the
three-stepmechanism (cf. Fig. 5) Time unit: min lKBrl = 0.053 rd Activationenergies used:O El = 49.3 E2 = 79.7 E3 = 41.8 kJ/mol 21 experimentswith cat = Ferroine; CKBr031,= 0.04, 0.06, 0.075 or 0.10 $1 (0.10 in 5 cases) Heating rates: O-6-1.6 K/min Correlation: R = 0.970 -+ 0.036 step -AH kJ/mol 19 A k298 1 2 3
7.59 i-0.34 13.43 T 0.61 5.17 z 0.38
0.097 0.33 0.008
8 - 130 6- 80 15 - 197
7 experimentswith cat = CeC13-6H20;IKBr03Jo= 0.06, 0.10, 0.12 or 0.14 Heating rates: 0.5 - 1.5 K/min Correlation:R = 0.964 2 0.044 step -AH kJ/mol 19 A k298 1 z
7.57 + 0.43 12.93 5.18 T 0.39 0.32
z
0.092 0.008 0.105
415 42 72 - 238 133
209
of the DTA curves by computer.
Reproduction
All curves (9) and compared
were
both evaluated
with
a computer-generated
out 50% of all curves simple
bimolecular
better
than 0.99
340 K. The
obtained
of BORCHARDT and DANIELS
by the method
may
curve
(LO). bJe found
be reproduced
that ab-
by the assumption. of a
rate law since correlation coefficients, then, were including
remainder
the total measuring
of the curves
which
range
mostly
from about
involved
275 to
special
condi-
tions due to catalyst concentration, heating rate or bromate concentration, could
be reproduced
by the following
three-step
in many cases
mechanism
(Fig, 5 and Table), 1.
Bimolecular initiating
2.
Autocatalytic (initiating) step
3.
Bromide-regenerating
A = BrO;;
shows,
of SKRABAL
there
A+C=B
D=
catalyst;
will often
and WEBERITSCH
son. The enthalpies
when the
be a good fit when
our fitted
data
on the
much more complicated tely rate-determing be a too simple
is
heating
required. rate
steps of three
steps, however,
This
indicates groups
for EI the
since
the
catalyst
show enormous
and a certain
that
dependence
of
the true
mechanism is
assumed
are approxima-
of reactions.
to take the five-step
model
using
product(s).
mean value B no material for compari-
and that the three reactions
concept
a true non-isothermal
fit
B)
(cf. (12)) and for E2 the E
used for the individual
best
A)
C+E
C = Br-; E = final
of our AB-simulations, while for step 3 we found variations
(= process
A + B = 28 f D (= prokess
step
B = HBr02,- D = oxidized
As the table value
step
OREGONATOR
effects
It seems even to mechanism
cannot
(12) as
be explained
by it. REFERENCES 1 2 3 4 5
6 7 8
1: 11 12
B.J. Field and R.M. Noyes, J. Chem. Phys. 60 (1974) 1877-1884 D. Edelson, R.J. Field and R-M. Noyes, Int. J. Chem. Kinetics 7 (1975) 417-432 I. Lamprecht and B. Schaarschmidt, Thermochim. Acta 22 (1978) 257-266 E. Kdriis, Nature 251 (1974) 703-704 R.J. Field, Chemie in unserer Zeit 7 (1973) 171-176 E. Koch, Chem. Ing.-Techn. 37 (1965) 1004-1010 E. Koch, Non-isothermal Reaction Analysis, Academic Press, London, 1977, espec. Chapters 4 and 6 III E. Koch and B. Stilkerieg, Thermochim. Acta 17 (1976) 1-15 H.J. Borchardt and F. Daniels, J. Am. Chem. Sot. 79 (1957) 41-46 E. Koch, Therm. Anal. Proc. Int. Conf. (5th), Kyoto, 412 E_ Koch and B. Stilkerieg, Thermochim. Acta, in press; J. thermal Analysis, in press R.M. Noyes, R.J. Field and E. Kiiros, J. Am. Chem. Sot. 94 (1972) 8649-8663