245
Applied Chtalyysis, 4 (1982) 246-256 Elsevier Scientific Publishing Company,
EFFECTS
OF CATIONS
INTRODUCED
Amsterdam
- Printed in The Netherlands
INTO 12-MOLYBDOPHOSPHORIC
ACID ON THE CATALYST
PROPERTIES
Mamoru
AI
Research
Laboratory
of Resources
Nagatsuta,
Midori-ku,
(Received
15 December
Yokohama,
Tokyo
Utilization,
Institute
of Technology,
227, Japan.
1981, accepted
IO July 1982)
ABSTRACT The effects of the kind and amount of a cation introduced into 12-molybdophosphoric acid, HSPMo 12’4fy on its function as an acid-catalyst, its reducibility and reoxidizabllity, I s oxidation activity, and its thermal stability are examined. With a change in the amount of a cation, the catalytic activity for acidcatalyzed reaction varies in a manner different from the acidity measured by means of NH-J adsorption, although there exists a correlation between them as far as the neutral salts are concerned. The neutral salts ar divi ed into two groups depending on the reducibility: Group A, salts of Ag+, Pd?+ , Cu $+ , and Cr3+ and Group B, the other salts. The reoxidizability varies in the same direction as the reducibility. The oxidation activity for 1-butene and methacrolein is related to the electronegativity of the metal ion, but is independent of the reducibility. The thermal stability is markedly enhanced by the introduction of Cr3+, whereas the effects of Cs+, Rb+ and K+ are limited by their deleterious effect on the catalytic activity.
INTRODUCTION Catalysts in certain
based on 12-molybdophosphoric
mild oxidations,
of their technical oxidation,
notably
importance
acid, H3PMo,2040,
in "acid-formation-type"
in the synthesis
much care has recently
of methacrylic
been taken to improve
[l-43. It should be noted that their selectivity the well-known
bismuth molybdate
on the characteristics
catalysts.
perform
excellently
reactions.
Because
acid by direct
their catalytic
is quite different
action
from that of
In a preceding paper [5], we reported
of IE-molybdophosphoric
acid and its salts as catalysts
for mild oxidation.
In the present paper, we attempt to clarify in more detail the effects of different
kinds and amounts
stressing
its function
and its thermal
of cation
introduced
as an acid-catalyst,
stability
into 12-molybdophosphoric
its reducibility
as well as its oxidation
acid,
and reoxidizability,
activity.
EXPERIMENTAL Catalysts IP-Molybdophosphoric 0166-9834/82/000&0000/$02.75
acid, H3PMo,2040.
aH20, from Kanto Chemical
0 1982 Elsevier Scientific Publishing Company
Co. was used
246 without
further
Salts of 12-molybdophosphoric
purification.
OJo (where M represents
an n valent cation and x is the extent
ment, 0 5 x 6 3), were prepared [6]. They were supported catalyst
preparation
according
to the principle
on pumice originating
was identical
[5], except that the calcination
Reaction
acid, M!+,3H3_xPMo12
from volcanic
with that described
temperature
of proton
reported
replace-
by Tsigdinos
rock. The method
in the preceding
of
paper
was fixed at 360°C.
procedures
The vapor-phase of 2-propanol perimental
air oxidation
were carried
procedures
Reducibility
out in a continuous-flow
and the dehydration
system. The reactor
were the same as those emplyed
and reoxidizability
The reducibility
of I-butene and methacrolein
in earlier works
and ex-
[5,7,8].
measurements
and reoxidizability
of the catalyst
a closed system using H2 and O2 as reductant
were measured
and oxidant
by means of
respectively. A 2.0 g 3. in volume and 15 cm
portion of the catalyst was put in a glass tube (about 8 cm in length) and heat-treated
in an electric
furnace
at about 330°C for 2 h under
a stream of dried air injected from a fine steel pipe inserted Immediately connected
with a BET apparatus
the catalyst
had cooled
modified
into the system,
was raised at a constant
programmed
furnace.
to measure
after which the temperature
with the rise in the temperature. temperature
until
was calculated
of the
rate (100°C h-l) by means of a temperature-
The same procedures
had previously
N2 in place of Hp. as a blank test, because
certain
it was quickly
a low area and pumped
to 0°C. A fixed amount of H2 (about 26 cm3 STP and 66
kPa) was then introduced catalyst
into the bottom.
after the glass tube had been taken out of the furnace,
been followed,
the pressure
but with
of the system
increases
The amount of H2 reacted with a catalyst from the difference
run with H2 and that with N2. The temperature 0.3 mole per mole of 12-molybdophosphoric
in pressure
between
at which the H2 consumption
acid, TR, was employed
at a the reaches
as the index
of the reducibility. After the determination
of the TR value, the reduction
ued until the H2 consumption measure
the reoxidizability
the system was outgassed Then, the same procedures the reduced catalyst
reached
1.0 mole per mole of H3PMo,2040
for a fixed degree of initial reduction.
until the catalyst were repeated
was obtained
ion of 0.15 mole per mole of H3PMo,20Q0,
were continin order to Thereafter,
had been cooled to room temperature.
with 02. The amount of 02 reacted with
from the difference
run with O2 and that with N2. The temperature
reoxidizability.
procedures
in pressure
corresponding
TRO, was employed
between
the
to the 02 consumptas the index of the
241 RESULTS Function
as acid-catalyst
It was found that, when the kind of countercation is changed, a manner
the oxidation
distinctly
different
of NH3 [51. This prompted function
activity
for butadiene
from the acidity
us to examine
is fixed, while
and methacrolein
measured
the effects
the amount
varies
in
by means of the adsorption
of countercations
on the
as an acid-catalyst.
The dehydration reaction.
of E-propanol
The activity
the presence
decreases
to propylene
was chosen
with the duration
of an excess of air. Therefore,
as a model acid-catalysed
of the reaction
time even in
care was taken to measure
the activi-
ty at a fixed time (30 min) after the start of each run. The main product was propylene;
the amounts
of acetone
and ether were
less than 3 mol %. The results
obtained
under fixed conditions (T = 15O'C; 2-propanol = 1.65 mol % in air; total -1 flow rate = 1.0 1 min ; catalyst = 2 to 10 g) are plotted as a function of the
extent of substitution manner
FIGURE
different
1
by a cation,
from the acidity
Activity
x, in Figure measured
of M~+,nH3_xPMo,2040
1. The activity
varies
in a
by means of the NH3 adsorption
catalyst
for dehydration
[5].
of 2-propanol.
248 As is shown in Figure 2, a correlation the electronegativity concerned,
is observed
between
the activity
ion, Xi [9], as far as the neutral
in the case of acid salts,
it is hard to find any correlation
O40'
5
while
of the metal
such as M"+ ,,nH2PMo,2040
between
salts are
and M2+ 2/nHPMo12
them.
I
-_-_-_-H+--__
4-
and
I
b
_g$/@d 0
0
T2
4
I 6
6
aNi**
I 10
I 12
I 14
Xi
FIGURE 2
Relation
E-propanol
between
the activity
and the electronegativity
Reducibility
of M~~,,PMo,~O~~ for dehydration
of metal
of
ion.
and reoxidizability
The reducibilility
- that is, the oxidizing
power - was measured
for a series
of neutral
salts, M"+ according to the method described above. The 3/nPMo12040' results are plotted as a function of the electronegativity of the metal ion,
X i, in Figure 3. Pd was readily reduced beyond the fixed extent even 3/2PMo12040 at 0°C; consequently, it was hard to evaluate the reducibility, TR. As may be seen in Figure 3, the salts are divided 3+ , the reducibility
salts of Pd 2+, Ag+, Cu2+, and Cr
than that of the free acid, H~PMo,~O~~. bility
is lower (TR is higher)
electronegativity
of the metal
In group A,
(TR is lower)
In Group 6, the other salts, the reduci-
than that of the free acid and is related
to the
ion.
On the other hand, the reducibility, of formation
into two groups. is higher
TR, is plotted
of the metal oxide corresponding
as a function
to the cation
of the heat
in Figure 4. It is
249
3oc
o,,,j2+
-_-_-
200
OFe’+ OS?+
Ii+-_-_-.-
Y N
%+
e
l
cu=+
1oc : I 2
An’
I 4
I 8
-6
Pdtn \I
I 10
I 12
I 14
Xi FIGURE 3
evident
TR as a function
of the electronegativity
that the heat of formation
Group A salts is low compared The effect of amount Ag+. The results markedly
of oxides corresponding
ion.
to the metal
ion of
with that of the other oxides.
of added cations
was examined
for Ca+, NH;, Cu2+, and
are shown in Figure 5. It was found that the reducibility
affected,
even when the amount of cation
Then, the reoxidizability, are plotted
of metal
as a function
of the reducibility,
the Group A salts stay about case of the Group B salts,
TRO, was measured
lOO"C, regardless
the TRo value
is
is small.
for each neutral
salt. The results
TR, in Figure 6. The TRO values of of the TR value. However,
increases
with an increase
in the
in the TR
value.
Oxidation
activity
First, the oxidation salt catalysts
of methacrolein
was conducted
over a series of neutral
T = 350°C; methacrolein - steam = 1.6 -1 7.5 mol % in air; total flow rate = 1.0 1 min , and catalyst = 10 g. The con-
version
under fixed conditions:
to methacrylic
the metal
acid is plotted
ion in Figure 7.
as a function
of the electronegativity
of
250
Ei!O
v0
200
’ -
i0 8 -m-e_-_- of=+ Q3 i,OJ
H,PMo,~O,,
b0,
z
1oc :A,0
0
&
-a
-AH FIGURE 4
TR as a function
the cation,
I 120
I
I 80
I 60
I 40
20
100
1 140
I kcal IO gdOm
of the heat of formation
of oxide corresponding
Except for BiPMo,2040, the activity
is related,
all the salts are less active to a certain
is, the electronegativity.
It should,
extent, however,
than the free acid, and
to the nature of the cation,
metals and Ag, which are very low in the activity
catalyzed
(Figure 1) and the acidity
reaction
to the same extent as the salts consisting
for acid-
[5], can produce methacrylic
of a metal
ion of a moderate
such as Mn 2+, Zn2+, Co2+, and Ni2+. The selectivity
from 35 to 55 mol %, and it appeared
that
be noted that the salts of alkali
and alkaline-earth
negativity,
to
AH.
acid
electro-
was in the range
to vary in the same direction
as the
activity. Since the activity
for oxidation
I-butene was chosen as the olefinic fixed conditions:
T = 35O'C;
of butadiene reactant.
1-butene
flow rate = 1.0 1 min -', and Catalyst is plotted catalyzed
Thermal
in Figure 8. The activity reaction
has previously
The oxidation
been studied
was conducted
[5],
under
- steam = 1.0 - 7.5 mol % in air; total = 10 g. varies
The conversion
to maleic
in the same manner
anhydride
as that for acid-
shown in Figure 2.
stability
12-Molybdophosphoric
acid is known to decompose
at around
400°C
C61, and to
253
X FIGURE 5
TR as a function
lose its catalytic disadvantage thermal
of the extent
activity
in an oxidation
stability
at lower temperatures Actually,
catalyst.
has been claimed
related
to the activity
to ascertain
activity
for a simple model reaction
- for example,
2.0 g portion of a catalyst
was heat-treated
was carried 2-propanol
in
[I]. This prompted
for olefin
reaction.
and aldehyde
It is, therefore,
from the lowering the dehydration
is
possible
of the activity
of 2-propanol.
at a fixed temperature
in a stream of air for 2 h. The dehydration
A
in the of 2-propanol
under fixed conditions: T = 160°C; -1 = 1.65 mol % in air, and total flow rate = 1.0 1 min . The activity
was measured
out over the heat-treated
X.
This is a serious
an improvement
literature
activity
for acid-catalyzed
range from 390 to 480°C
by a cation,
on the stability.
the oxidation
the loss of oxidation
[1,5,10]. however,
in the patent
us to study the effect of countercations As has been shown above,
of proton replacement
exactly
catalyst
30 min after the start of each run. The results
obtained
only from the catalysts
example,
the neutral
possessing
a relatively
salts of alkali and alkaline-earth
metals were too inert for the effect
could be
high activity; metals
of the heat-treatment
for
and some other
to be measured.
The
results are shown in Figure 9. It was found that: thermal
stability,
Rb+ and Cs+ enhance
(i)
(ii)
Li+, Na+, Ba2+, Cu2+, Zr4+, and A13+ reduce the the effect of 8i3+ and Fe 3+ is small,
the stability
to a certain
extent,
and (iv)
(iii)
NH:, K+,
Cr3+ shows an
/ 0
cs+
200 -
ry
# y+ *’
/ .ti+
H+./
l
' 4
d
++
.2*
N’
----I
L
0
100
FIGURE 6
Relation
excellent presence
effect.
between TRO and
It is noticeable
TR' that the stability
of steam in the surrounding
is not affected
by the
gas of the heat-treatment.
DISCUSSION The results
shown in Figures
1 and 2 may be summarized
as follows,
though
there are some discrepancies: (i)
When the extent of replacement acid-catalyzed
reaction
by means of the NH3 adsorption with the addition (ii)
The activity addition
by a cation
does not decline
of a certain
is still retained
of an alkali metal
is low, x $ 1, the activity
for
as steeply as the acidity measured
[53. In contrast,
the activity
increases
cation. or is even increased,
with the further
ion up to x = 2 (except for the case of Li+).
such as (iii) In the case of cations of a relatively high electronegativity, 2+ Bi3+, Fe3+, and Cu , the effect is small, even if the amount of the cation is great. (iv)
The activity
decreases
steeply
upon the addition
of a large amount
(x z 2)
of cation of a lower electronegativity. (VI
The activity
of neutral
(vi)
As far as the neutral
salts of alkali and alkaline-earthmetals
and Ag is
very low. salts are concerned,
clear correlations
exist among
253
J
20-
Bi3’ I I ,
H+-__
-_e__
I
1’ /’
lo-
I 2
00
I 4
6
8
10
I 14
12
Xi FIGURE 7
Relation
between
and the electronegativity
the activity,
the conversion of metal
the acidity,
of methacrolein
to methacrylic
acid
ion.
and the nature of the cation,
notably,
electro-
negativity. From the finding manner different
that the activity
from the acidity
we are induced to consider acidity
obtained
as follows.
by a static method
Bulk acid may be extinguished the cation; as a result, of the cation.
for acid-catalyzed
measured
As has been mentioned
represents
gradually
the acidity
to be different
and more complex. reflect
in preference
activity,
when the extent of acidic
however,
It is likely that (i)
(ii)
sites are generated replacement
new acidic
it is difficult
the bulk acid to the catalytic [3,51.
action
[51, the
by
the situation
the acidic
seems
activity
sites located
to the catalytic
of coordinat-
of the cation, is so eminent
action
and (iii)
in number of
At the present
stage,
the action of the bulk from that of the
surface for each salt of 12-molybdophosphoric
catalyst
[51,
of the protons
sites consisting
by the addition
of low, the catalyst
to distinguish
earlier
the catalytic
contribute
sites that all the sites do not act effectively.
however,
in a
fashion with the amount
the amount of bulk acid, because
to the bulk acid;
varies
the amount of bulk acid.
in a regular
on the surface or in the bulk near the surface
ively unsaturated
mainly
by the replacement
falls
In the case of catalytic
does not always
reaction
by means of the NH3 adsorption
acid, though the contribution
has been pointed
out for the free acid
of
254
thPi!nz*~~ 00 /co* /. $i2+ 0
0
2
4
6
6
Cr*
? ea+ I 12
I 10
I 14
Xi FIGURE 8
Relation
between
the electronegativity
of metal
It can be postulated of countercation formation
the conversion
of I-butene to maleic anhydride
ion.
from the results
is not the same between
of the oxides corresponding
shown in Figures
3 and 4 that the action
Group A and Group B salts. The heat of
to the cation of Group A salts is lower
than that for Moo2 + 0.5 02 + Mo03, -AH = 38 kcal [II], whereas ation of the other oxides
species,
the oxygen
in the &se
species
role in the reduction
to oxidize
of the Group 6 salts, oxygen
ing to this view and the results
of the catalyst.
shown in Figure 3, it can also be deduced
the reactivity,
i.e. the oxidizing
in the electronegativity
different
On the other hand,
bonded with MO reacts or migrates
role in the reduction
with a decrease
formity with the results obtained
the former oxygen
in the bulk, play an
is bonded more strongly with the counter-
the oxygen
more easily and plays an important
compounds
or migrate
of the bulk of the catalyst.
cation than with MO; as a result,
organic
bonded loosely with the counter-
species bonded with MO or P. Possibly,
having a higher ability
important
the heat of form-
is higher than 38 kcal (Figure 4). In the case of the
Group A salts, there may exist oxygen cation besides
and
power, of oxygen
that
bonded with MO decreases
of the countercation;
this is in con-
by an ESR study of the salts reduced with various
in ionization
potential
[12].
At any rate, it is true that most of the salts of 12-molybdophosphoric at least in a high oxidation
Accord-
state, are more eminent
in reducibility
acid,
than metal
255
I 'C
‘Temperature FIGURE 9
Catalytic
temperature
oxides;
activity
for 2-propanol
dehydration
as a function
of the
of heat-treatment.
for example,
the TR value of V205 is about 320°C and that of Moo3 is
above 380°C. It is surprising as the reducibility
to find that the reoxidizability (Figure 6), suggesting
From the results,
osites. governed
the bulk of the catalyst, strength.
we are induced to consider
by the same factor,
possibly
which
in the same direction
connected
by the results
are not opp-
that both properties
by the ease of the migration
is closely
This view is also supported
varies
that the two properties
are
of oxygen
with the metal-oxygen obtained
by Akimoto
in
bond et al.
c131. The oxidation acid-catalyzed mainly
activity
reaction,
by the activation
for I-butene indicating on acidic
In the case of methacrolein the same. The salts of Cs+, Ba
can be well related with the activity
that the oxidation
for olefins, produce methacrylic 2+ of Mn 2+, Zn2+, Co , and NJ.2+ , suggesting the presence
ectivity
for methacrylic
property
but, possibly,
is controlled mentioned
[53.
oxidation, however, the situation is not exactly 2+ , and Ag+, all showing a very low oxidation
activity
not necessitate
of olefin
sites, as has been previously
for
acid to the same extent as the salts that the oxidation
of methacrolein
does
of strong acid sites, and also that the high sel-
acid formation
is not ascribable
to the mild oxidizing
power.
to the strong acidic
256
It should be noted that the oxidation lated to the electronegativity
is a Group A or Group B salt. Moreover, increases with the addition bility decreases
markedly
activity
of the cation,
the oxidation
with the addition
by the oxidizing
istics which are connected The thermal gravimetric,
stability
of view [6,14,15]. the catalytic
thermal,
or melting
activity
can only with difficulty
the cation. unsuitable temperature
provide system
be predicted
because
activity
an answer to our old question
stability
suggest
temperature
salts corresponding
to
salts of Cs+, Rb+ and K+ are though their decomposition
salts, for example,
M2HPMo,2040,
about 200°C lower than the decom-
neutral
salt. At present,
remains
undetermined,
of why the addition
the reason
but the results
of Cr 3+ to W03-P205
the acidity
that the addition
of 12-tungstophosphoric
of catalytic
from the decomposition
of neutral
at a temperature
of the corresponding 3+ action of Cr addition
that is, the results
far lower than the decom-
of their low activity,
(calcined at 500°C) increases
point
shown in Figure 9 that
effect of Cs+, Rb+, K+, and NH: is re-
temperature
temperature
for the excellent
from the structural
and that the stability
are very high, and that the acidic
lose their catalytic position
at temperatures
It should be noted that the neutral as catalysts
is not
in the bulk, character.
salts has been studied by means of thermo.
temperature
the enhancing
lated to the high decomposition
the reduci-
bond strength.
and X-ray analyses
is destroyed
temperature
salt, although
for these compounds
for these compounds
of the oxygen
it is clear from the results
position
of neutral
activity
with the metal-oxygen
However,
activity
activity
is re-
the catalyst
of a small amount of NH: or Cs+
power or mobility
of many neutral
differential
of whether
of NH; or Cs+ up to x = 2 [5], whereas
(Figure 5). It is clear that the oxidation controlled
for olefin and aldehyde
irrespective
in a dramatic fashion [16]; 3+ of Cr also enhances the thermal
acid.
REFERENCES
12 13 14
T. Ohara and A. Niina, Symp. Catal. Sot. Japan, Fukuoka, No.10 and 11 (1976). T. Ohara, Shokubai (Catalyst), 19 (1977) 157. M. Otake and T. Onoda, Shokubai (Catalyst), 18 (1976) 169. W.W. Swanson, Molybdenum Catalyst Bibliography, Suppl. No.5. Climax Molybdenum Co. Michigan, (1978) 61. M. Ai, J. Catal., 71 (1981) 88. G.A. Tsigdinos, Ind. Eng. Chem. Prod. Res. Dev., 13 (1974) 267. M. Ai, J. Catal., 67 (1981) 110. M. Ai, J. Catal., 52 (1978) 16. K. Tanaka and A. Ozaki, J. Catal., 8 (1967) 1. H. Niiyama, H. Tsuneki and E. Echigoya, Nippon Kagaku Kaishi, (1979) 996. Kagaku Binran (Handbook of Chemistry), the Chem. Sot. Japan Ed. Maruzen, (1975) 950. M. Akimoto, Y. Tsuchida and E. Echigoya, Chem. Lett., (1980) 1205. M. Akimoto, K. Shima and E. Echigoya, Shokubai (Catalyst), 23 (1981) 281. "Topics in Current Chem.," Vo1.76, Springer-Verlag, Fi;j5;sigdinos, New York,
15 6
K. Eguchi, N. Yamazoe and T. Seiyama, M. Ai, J. Catal., 49 (1977) 305.
1 2 3 4 5 6 7 8 9 IO 11
Nippon Kagaku Kaishi,
(1981) 336.