11 Catalytic Reductions Using Carbon Monoxide and Water in Place of Hydrogen R. PETTIT, K. CANN, T. COLE, C. H . MAULDIN, and W. SLEGEIR
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University of Texas at Austin, Austin, TX 78712
Carbonyl complexes of rhodium, ruthenium, osmium, iridium, and platinum, in the presence of H O and a weak base (e.g., trimethylamine), act as catalysts for the conversion of propene to a mixture of butanal and methylpropanal; with the exception of the platinum system, these catalysts are considerably more active than Fe(CO) as reported by Reppe. Under the same conditions, but in the absence of olefin, the carbonyls act as catalysts for the conversion of CO and H O to CO and H . The metal carbonyls, together with Fe(CO) , in the presence of H O, C O , and a weak base such as Me N, serve as catalysts for the conversion of nitrobenzene, dinitrobenzene, and 2,4- and 2,6-dinitrotoluene to the corresponding aminobenzene derivatives. 2
5
2
2
2
5
2
3
/ ^ a r b o n m o n o x i d e is r e a d i l y a v a i l a b l e f r o m l o w - g r a d e ^
carbonaceous
m a t e r i a l s u c h as c o a l , l i g n i t e , etc., a n d i t is r e a d i l y c o n c e i v a b l e
that
this m a t e r i a l c o u l d p l a y a n i n c r e a s i n g l y i m p o r t a n t r o l e i n t h e e n e r g y a n d " p e t r o c h e m i c a l " fields as t h e sources of p e t r o l e u m c o n t i n u e t o d i m i n i s h . I n several cases, s u c h as t h e F i s c h e r - T r o p s c h synthesis of h y d r o c a r b o n s ( I ) a n d t h e K o c h synthesis of c a r b o x y l i c acids (2), t h e p o t e n t i a l s i g n i f i c a n c e of C O is w e l l r e c o g n i z e d , a n d i t is v e r y l i k e l y t h a t other n e w uses w i l l e m e r g e f o l l o w i n g f u r t h e r research w o r k . I n this c h a p t e r w e s h a l l discuss o u r results t o date c o n c e r n i n g t h e use of C O a n d w a t e r i n p l a c e of h y d r o g e n as a r e d u c i n g m e d i u m . I n p r i n c i p l e , a n y r e d u c t i o n o f a substrate SH
2
S b y hydrogen to yield
( R e a c t i o n 1) c a n b e c o n d u c t e d w i t h C O +
H
2
0 as i n d i c a t e d i n
R e a c t i o n 2, a n d f o r e a c h h y d r o g e n m o l e c u l e i n v o l v e d t h e latter
process
is a l w a y s a p p r o x i m a t e l y 7 k c a l / m o l m o r e t h e r m o d y n a m i c a l l y f a v o r a b l e . 0-8412-0429-2/79/33-173-121$05.00/0 © 1979 American Chemical Society In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
122
INORGANIC
COMPOUNDS
S + H -> S H ; F = 2
2
WITH
2
PROPERTIES
- x kcal/mol
S + C O + H 0 -> S H + C 0 ; F = 2
UNUSUAL
2
II
(1)
- (x + 7) k c a l / m o l
(2)
T h e k e y p r o b l e m i n the p o t e n t i a l use of C O as i n R e a c t i o n 2 is of course the d e s i g n of catalysts w h i c h a l l o w the r e a c t i o n to p r o c e e d at a n a c c e p t a b l e rate. Just as h y d r o g e n does not r e a d i l y a d d to most substrates ( t h e a d d i t i o n of h y d r o g e n to ethylene, f o r e x a m p l e , does not o c c u r , a n d the r e a c t i o n is i n fact f o r b i d d e n b y the W o o d w a r d - H o f f m a n n r u l e s ) , a n d Downloaded by UNIV OF ARIZONA on November 9, 2012 | http://pubs.acs.org Publication Date: May 5, 1979 | doi: 10.1021/ba-1979-0173.ch011
i n most cases r e q u i r e s i n t e r v e n t i o n of a catalyst, s u c h w i l l also b e t r u e w h e n C O -f- H 0 is u s e d . 2
Reppe Modification
of the
Hydroformylation
Reaction
O u r i n i t i a l efforts i n the area of r e d u c t i o n s w i t h C O + H 0 i n v o l v e d 2
a s t u d y of the m e c h a n i s m of w h a t w e s h a l l t e r m the R e p p e m o d i f i c a t i o n of the h y d r o f o r m y l a t i o n r e a c t i o n ( 3 ) .
I n the n o r m a l h y d r o f o r m y l a t i o n
process, the elements of h y d r o g e n a n d C O are a d d e d to a n olefin t o generate a n a l d e h y d e ( R e a c t i o n 3 ) .
I n the R e p p e m o d i f i c a t i o n of t h i s
process, the same r e a c t i o n is a c h i e v e d u s i n g C O -f- H 0 i n p l a c e of h y d r o 2
gen (Reaction 4). R R -
I n the n o r m a l process, the catalyst u s e d is u s u a l l y a
C H =
C H + CO + 2
H -» 2
RCH CH CH0 2
(3)
2
C H — C H + 2C0 + H 0 -» R C H C H C H 0 + C 0 2
2
2
2
2
(4)
c a r b o n y l d e r i v a t i v e of c o b a l t or r h o d i u m , w h e r e a s i n the R e p p e m o d i f i c a t i o n , i r o n c a r b o n y l i n c o n j u n c t i o n w i t h a L e w i s or B r o n s t e d base is u s e d . A c o m p a r i s o n of the t w o processes reveals s e v e r a l i n t r i g u i n g p o i n t s of interest.
T h u s , i n the n o r m a l process w i t h c o b a l t c a r b o n y l as
the
catalyst, temperatures of 150 ° C or h i g h e r a n d pressures of 3000 p s i are u s e d , w h e r e a s i n the R e p p e m o d i f i c a t i o n the c o n d i t i o n s are m u c h less severe;
100 ° C t e m p e r a t u r e a n d 500 p s i of C O pressure are sufficient.
Furthermore, when F e ( C O )
5
is u s e d as a catalyst i n the n o r m a l process
w i t h h y d r o g e n , it p e r f o r m s v e r y p o o r l y ( 4 ) ; l i k e w i s e , w e find that w h e n c o b a l t c a r b o n y l is u s e d u n d e r R e p p e ' s c o n d i t i o n s i t too p e r f o r m s v e r y poorly (zero activity). T o u n d e r s t a n d the m a n n e r i n w h i c h the F e ( C O )
5
p l u s base catalyst
system uses C O -f- H 0 i n p l a c e of h y d r o g e n , s p e c u l a t i n g that s u c h a n 2
u n d e r s t a n d i n g w o u l d b e of v a l u e to the d e s i g n of other catalysts c a p a b l e of effecting r e d u c t i o n s w i t h C O + H 0 , w e i n v e s t i g a t e d the m e c h a n i s m 2
of the R e p p e r e a c t i o n . T h e p e r t i n e n t results are s u m m a r i z e d b e l o w . W e f o u n d that
the h y d r o f o r m y l a t i o n r e a c t i o n s t r o n g l y
o n t h e p H of the m e d i u m i n t h e reactor ( 5 ) .
depended
W h e n an autoclave was
In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
11.
PETTIT ET AL.
Catalytic
Reductions
Using CO and
c h a r g e d w i t h ethylene, w a t e r , F e ( C O ) , a n d N a C 0 5
C O , the F e ( C O )
2
d i s s o l v e d to f o r m N a H F e ( C O )
5
4
2
u n d e r 500 p s i of
3
a c c o r d i n g to
t i o n 5. T h e f o r m a t i o n of the H F e ( C O ) " a n i o n f r o m F e ( C O ) 4
Na C0 2
+ Fe(CO)
3
5
+ H 0 -> N a H F e ( C O ) + C 0 2
123
H0
4
2
Reac-
a n d base
5
+ NaHC0
(5)
3
is the o l d a n d w e l l - e s t a b l i s h e d r e a c t i o n , a n d the a n i o n is a w e l l - c h a r a c t e r i z e d species (6,7).
U p o n c o m p l e t e d i s s o l u t i o n of the F e ( C O )
in
5
this m a n n e r , the p H of the m e d i u m is a r o u n d 12.0, b u t o n l y w h e n the Downloaded by UNIV OF ARIZONA on November 9, 2012 | http://pubs.acs.org Publication Date: May 5, 1979 | doi: 10.1021/ba-1979-0173.ch011
p H d r o p s to the v i c i n i t y of 10.7 ( a t t r i b u t a b l e to the r e a c t i o n of C O O H " -> H C O O " ) does the f o r m a t i o n of p r o p a n o l b e g i n to o c c u r .
+
(Propa-
n a l is the i n i t i a l p r o d u c t , b u t u n d e r the c o n d i t i o n s u s e d i t is r e a d i l y r e d u c e d to p r o p a n o l ) . I n a s i m i l a r e x p e r i m e n t i n w h i c h 1,5-cyclooctadiene
is u s e d i n p l a c e
of ethylene, a g a i n , o n l y w h e n the p H d r o p s to a b o u t 10.7 is there o b s e r v e d i s o m e r i z a t i o n of 1,5- to 1,3-cyclooctadiene.
W h e n the same e x p e r i m e n t is
r u n w i t h o u t a n y olefin present, t h e n h y d r o g e n begins to a p p e a r i n the reactor w h e n the p H a g a i n reaches a p p r o x i m a t e l y 10.7. I n a s i m i l a r e x p e r i m e n t to that d e s c r i b e d w i t h ethylene, b u t w i t h a d d i t i o n of a c e t a l d e h y d e , i t is f o u n d that the a c e t a l d e h y d e is i m m e d i a t e l y r e d u c e d to e t h a n o l at a p H of 12.0, b u t a g a i n o n l y w h e n the p H is l o w e r e d to 10.7 does the h y d r o f o r m y l a t i o n of e t h y l e n e b e g i n to take p l a c e . A p l a u s i b l e e x p l a n a t i o n of this p H d e p e n d e n c e is that a significant c o n c e n t r a t i o n of H F e ( C O ) 2
4
begins to f o r m at a p H of a b o u t 10.7 a n d
t h a t this is the species w h i c h initiates the h y d r o f o r m y l a t i o n r e a c t i o n . H Fe(CO) 2
4
is k n o w n to b e a p o w e r f u l catalyst f o r the i s o m e r i z a t i o n of
olefins ( 8 ) , a n d i t also w o u l d b e a sensible c a n d i d a t e f o r the f o r m a t i o n of molecular hydrogen through simple thermal decomposition
(9).
The
H F e ( C O ) " a n i o n is not the catalyst f o r these three reactions; h o w e v e r , 4
it is c a p a b l e of r e d u c i n g a l d e h y d e s to a l c o h o l s . W e c o n s i d e r t h e n that the m e c h a n i s m of the R e p p e m o d i f i c a t i o n of the h y d r o f o r m y l a t i o n r e a c t i o n c l o s e l y p a r a l l e l s that of the n o r m a l process as d e s c r i b e d b y H e c k a n d B r e s l o w (10).
T h e p r i n c i p a l steps are g i v e n
i n the f o l l o w i n g s c h e m e : H CH =CH 2
H Fe(CO) 2
2
CO
4
*CH CH 3
-Fe(CO)
2
4
HFe(CO)"4 CH CH CH OH 3
2
2
In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
124
INORGANIC
COMPOUNDS
WITH
UNUSUAL
PROPERTIES
II
T h e n o r m a l h y d r o f o r m y l a t i o n r e a c t i o n a n d the R e p p e m o d i f i c a t i o n are m e c h a n i s t i c a l l y c l o s e l y r e l a t e d ; the k e y p o i n t w h i c h emerges is t h a t i n the latter process it is easier to f o r m the species H F e ( C O ) 2
r e a c t i o n of F e ( C O )
f r o m the
4
5
a n d a q u e o u s base t h a n it is f r o m F e ( C O )
molecular hydrogen.
F o r this reason, the c o m b i n a t i o n of C O +
5
and H 0 2
p r o v i d e s a s u p e r i o r r e d u c i n g system f o r the r e d u c t i v e a d d i t i o n of C O t o a n olefin t h a n does m o l e c u l a r h y d r o g e n .
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Other Catalysts for
the Hydroformylation
T h e f o r m a t i o n of the H F e ( C O ) 2
4
Reaction with CO
+
H0 2
catalyst d e s c r i b e d a b o v e p r e s u m -
a b l y occurs v i a n u c l e o p h i l i c attack of h y d r o x y l i o n o n a C O l i g a n d of Fe(CO)
5
w i t h g e n e r a t i o n of the a n i o n i c m e t a l l o c a r b o x y l i c a c i d f o l l o w e d
b y decarboxylation and protonation (Reaction 6).
OH-
(CO) Fe(CO) 4
0 O || -C0 O > (CO) Fe—C—OH > (CO) FeH 2
4
4
1
H H Fe(CO) 2
(6)
+
4
W h e n aqueous amines are u s e d as the base i n s t e a d of N a C 0 , p r e 2
3
s u m a b l y the a m i n e rather t h a n h y d r o x y l i o n acts as the a t t a c k i n g n u c l e o p h i l e ; h y d r o l y s i s of the r e s u l t i n g m e t a l l o c a r b o x y a m i d e d e r i v a t i v e t h e n affords the m e t a l l o c a r b o x y l i c a c i d 1
(II).
T h e s e considerations n o w p r o v i d e a g u i d e l i n e f o r the
development
of other p o t e n t i a l catalysts f o r the use of C O -f- H 0 i n the h y d r o f o r m y l a 2
t i o n of olefins. I f the catalyst is to f u n c t i o n i n the same m a n n e r as just d e s c r i b e d f o r F e ( C O ) , t h e n a m i n i m u m r e q u i r e m e n t is that the system 5
f o r m a m e t a l c a r b o n y l w h i c h w i l l b e r e a d i l y a t t a c k e d b y a w e a k base to f o r m a n a n i o n analogous to 1. A w e a k base is essential b e c a u s e C 0 a n i n e v i t a b l e b y - p r o d u c t , a n d o n l y the carbonate regenerate the base a n d C 0
2
2
is
salts of w e a k bases
u p o n h e a t i n g . T h u s , i f the system is to b e
c a t a l y t i c i n base as w e l l , t h e n c l e a r l y o n l y a w e a k base c a n b e u s e d . T h i s w o u l d a p p e a r to b e the c r i t i c a l r e q u i r e m e n t , f o r the l i t e r a t u r e i n d i c a t e s t h a t m e t a l l o c a r b o x y l i c acids r e a d i l y d e c a r b o x y l a t e
(12),
a n d the
final
step i n R e a c t i o n 6, the p r o t o n a t i o n of a h y d r i d o m e t a l c a r b o n y l a n i o n , w o u l d seem to offer n o p r o b l e m p r o v i d e d the catalyst system w a s n o t i n a h i g h l y basic m e d i u m . O f the s i m p l e m o n o n u c l e a r m e t a l c a r b o n y l s , o n l y F e ( C O ) to b e r e a d i l y a t t a c k e d b y a w e a k base w i t h s u b s e q u e n t metal hydride bonds.
5
appears
f o r m a t i o n of
W e r e a s o n e d that i f the m e t a l c a r b o n y l system
In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
11.
PETTIT
ET
AL.
Catalytic
Reductions
Using CO and
125
H0 2
c o n t a i n e d the s t r u c t u r a l feature s h o w n i n f o r m u l a 2, i.e., a m e t a l - m e t a l b o n d system c o n t a i n i n g a b r i d g i n g c a r b o n y l g r o u p a n d a t e r m i n a l carb o n y l l i g a n d , t h e n n u c l e o p h i l i c attack of O H " m i g h t b e f a c i l i t a t e d . T h i s w o u l d b e a t t r i b u t a b l e to the p o s s i b l e d e r e a l i z a t i o n of n e g a t i v e
charge
f r o m the m e t a l a t o m to a n o x y g e n a t o m t h r o u g h the resonance i n t e r a c t i o n i n d i c a t e d i n 3.
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M
M = C = 0
OH"
~ M—COOH
M
\/
v
c
»M
\/
c
II
M—COOH
c
II
0
II
0
0 -
T h e s e c o n s i d e r a t i o n s thus p o i n t e d to a l a r g e n u m b e r of m e t a l c l u s t e r c a r b o n y l c o m p o u n d s w h i c h h a v e the s t r u c t u r a l features i n d i c a t e d i n 2. A s m e n t i o n e d earlier, the d e c a r b o x y l a t i o n of c o m p o u n d s of t y p e 3 to g i v e m e t a l h y d r i d e s w a s e x p e c t e d to p r o c e e d easily. S e v e r a l m e t a l cluster systems h a v e n o w b e e n t r i e d i n the h y d r o f o r m y l a t i o n r e a c t i o n of p r o p y l e n e a n d C O +
H 0 ( 1 3 ) , a n d as is seen 2
f r o m the d a t a i n T a b l e I, some of t h e m are f o u n d to b e m u c h s u p e r i o r to Fe(CO)
5
as catalysts. T h i s is e s p e c i a l l y t r u e of R h ( C O ) i a n d I r ( C O ) i . 6
6
4
2
S i n c e each of these catalyst systems w a s e x p e c t e d to p r o c e e d v i a i n t e r m e d i a t e f o r m a t i o n of a m e t a l h y d r i d e a n i o n ( f r o m 3 ) a n d p r o t o n a t i o n to a n e u t r a l d i h y d r o g e n m e t a l species, t h e n i n the absence of a n y olefin, e a c h c o u l d b e e x p e c t e d to p r o d u c e m o l e c u l a r h y d r o g e n u p o n therm a l d e c o m p o s i t i o n . T h a t is, e a c h also s h o u l d b e a catalyst f o r the w a t e r gas s h i f t r e a c t i o n ( R e a c t i o n 7 ) .
S u c h w a s f o u n d to b e t h e case; i n t h e
C O + H 0 -> C O + H 2
2
(7)
last c o l u m n of T a b l e I there is l i s t e d the moles of h y d r o g e n p r o d u c e d p e r m o l e of catalyst u s e d u n d e r i d e n t i c a l r e a c t i o n c o n d i t i o n s as w i t h t h e h y d r o f o r m y l a t i o n r e a c t i o n except f o r the o m i s s i o n of olefin. It is seen t h a t e a c h of the catalyst systems u s e d are catalysts f o r the f o r m a t i o n of hydrogen from C O and H 0 . 2
It m u s t be p o i n t e d o u t that the exact n a t u r e of the c a t a l y t i c species has n o t b e e n e s t a b l i s h e d i n the case of the m e t a l cluster c o m p o u n d s l i s t e d i n T a b l e I.
Rearrangement
of the a d d e d cluster c o m p o u n d s to
some other cluster species u n d e r the r e a c t i o n c o n d i t i o n s is r e a d i l y c o n c e i v a b l e , a n d i n s e v e r a l cases, v e r y p r o b a b l e .
In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
126
INORGANIC
COMPOUNDS
Table 1.
WITH
UNUSUAL
PROPERTIES
Hydroformylation of Propane
Experiment"
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II
T(°C)
1 2 3 4 5 6 7 8 9
110 125 100 100 180 180 180 125 125
Fe(CO) Rh (CO) Ru (CO) H Ru (CO) Os (CO) H Os (CO) H Os (CO)i Ir (CO) (Bu N) [Pt (CO) ]5 5
6
1 6
3
1 2
4
4
1 2
3
1 2
2
3
4
4
1 0 2
4
a 2
4
2
3
6
° A l l experiments run for 10 hr in a 300 m L stirred autoclave containing 0.05 mmol of catalyst, 22 m L of 25% aqueous trimethylamine, 78 m L of T H F , 350 psi of C O , and 150 psi of propylene. Small amounts of propane were formed in experiments 2, 5, 6, 7, and 8. Reduction In
of Aromatic
Nitro
Compounds
1925, i n a G e r m a n p a t e n t
solutions of F e ( C O )
5
(14),
to
Amines
it was revealed that alkaline
w o u l d reduce aromatic nitro compounds to amines
in a stoichiometric manner.
M o r e recently, L a d e n s b e r g a n d co-workers
( 1 5 ) h a v e s h o w n t h a t salts of t h e t r i n u c l e a r a n i o n H F e ( C O ) u " 3
also effect t h e r e d u c t i o n , a n d W a t a n a b e
a n d co-workers
will
(16)
have
o b t a i n e d s i m i l a r results w i t h t h e m o n o n u c l e a r a n i o n H F e ( C O ) ~ .
Each
4
of these species c o u l d h a v e b e e n f o r m e d u n d e r t h e c o n d i t i o n s u s e d i n the first r e p o r t , a n d p r e s u m a b l y o n e or b o t h w o u l d b e t h e r e a c t i v e r e d u c i n g species.
( H . A l p e r has r e c e n t l y s h o w n t h a t F e ( C O ) > i n t h e p r e s e n c e 5
of N a O D / D 0 , w i l l c o n v e r t n i t r o b e n z e n e i n t o ND ; h o w e v e r , t h e n a t u r e 2
2
of t h e r e d u c i n g species has n o t b e e n e s t a b l i s h e d
(17).)
W i t h H F e ( C O ) " as t h e r e d u c i n g agent, W a t a n a b e a n d c o - w o r k e r s 4
report that the reaction remains stoichiometric rather t h a n catalytic w h e n c o n d u c t e d u n d e r a pressure of C O . T h e s t o i c h i o m e t r y , h o w e v e r , is m o s t r e m a r k a b l e i n t h a t 1 m o l of H F e ( C O ) ~ salt w i l l r e d u c e 1.8 m o l of n i t r o 4
b e n z e n e t o a n i l i n e . Since, i n terms o f e l e c t r o n - t r a n s f e r r e d u c t i o n , t h e c o n v e r s i o n o f n i t r o b e n z e n e t o a n i l i n e i n v o l v e s six electrons p e r m o l e c u l e , then the H F e ( C O )
4
salt is a c t i n g as a n 11 ( 1 0 . 8 ) e l e c t r o n - t r a n s f e r agent.
I r r e s p e c t i v e o f t h e exact m e c h a n i s m of t h e electron-transfer
process,
c l e a r l y m o s t of these electrons m u s t b e p r o v i d e d b y t h e C O l i g a n d s , w h i c h i n turn become oxidized to C 0 . 2
A r a t i o n a l e x p l a n a t i o n o f t h e process w o u l d b e a succession of t w o electron-transfer steps as i n d i c a t e d i n R e a c t i o n s 8 a n d 9. W i t h c o m p l e t e d e p l e t i o n of t h e C O l i g a n d s a n d final o x i d a t i o n of F e ° to F e
+ +
(Reaction
1 0 ) , t h e n a t o t a l of 12 electrons c o u l d b e p r o v i d e d b y F e ( C O ) . 5
In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
11.
PETTIT ET
AL.
Catalytic
Reductions
and Water Gas Shift with C O + Moles of C Aldehyde/Moles of Catalyst
Using CO and
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2
H 0 2
C Aldehyde/ C Alcohol
Water Gas Shift Reaction (Moles of H /Moles of Catalyst)
4.5 40 43 37 6.6 - 300 -300 - 300 —
5 1700 3300 3400 270 270 400 300 700
h
n-/Isoaldehyde Ratio
5.2 300 47 79 13 6 9 250 0.5
127
H0
h
2
6
h
1.0 1.4 11.5 11.0 1.9 1.2 1.4 1.8 1.9
Identical conditions as in (a) expect that the propylene is omitted; a temperature of 150°C was used for experiments 2 and 8. Optimum conditions for each catalyst system have not been determined. 6
S i m p l e i n s p e c t i o n of R e a c t i o n s 8, 9, a n d 10 leads t o t h e c o n c l u s i o n that t h e r e a c t i o n s h o u l d b e m a d e to b e c a t a l y t i c i n F e ( C O )
i f it w e r e
5
c o n d u c t e d u n d e r a C O pressure i n the presence of excess base. Fe(CO)
4
g e n e r a t e d as i n R e a c t i o n 8 s h o u l d r e v e r t to F e ( C O )
treatment
with
C O , a n d p r o v i d e d i n e v i t a b l e loss
of
Fe°
5
to F e
The upon + +
is
a v o i d e d ( C O does n o t r e d u c e t h e ferrous i o n u n d e r m i l d c o n d i t i o n s ) , t h e n o n l y c a t a l y t i c q u a n t i t i e s of F e ( C O ) T h i s p r e d i c t i o n has b e e n
realized.
5
w o u l d be required. Various aromatic nitro com-
p o u n d s h a v e b e e n r e d u c e d to t h e c o r r e s p o n d i n g amines b y t r e a t m e n t at 25 ° C i n a q u e o u s s o l u t i o n of g l y m e c o n t a i n i n g c a t a l y t i c q u a n t i t i e s Fe(CO)
5
a n d l a r g e a m o u n t s of t r i e t h y l a m i n e u n d e r a pressure of
p s i of C O (18).
of
1700
T o observe catalysis, h o w e v e r , i t w a s necessary to
m a i n t a i n the c o n c e n t r a t i o n of the o x i d a n t , i.e., the n i t r o b e n z e n e , l o w at all times.
I f this w e r e n o t d o n e , t h e n r a p i d loss of t h e C O l i g a n d s
o c c u r r e d ( R e a c t i o n 9 ) a n d i r r e v e r s i b l e f o r m a t i o n of i r o n oxides ( R e a c t i o n 10)
resulted.
T h e c o n c e n t r a t i o n of t h e o x i d a n t w a s m a i n t a i n e d l o w
i n s i d e the reactor vessel s i m p l y b y p u m p i n g i n the n i t r o b e n z e n e o v e r a
Fe(CO)
Fe(CO)
m ( M
HFe(CO) "-» Fe(CO) 4
4
+ H
+ OH> H F e ( C O ) - . ! -> F e ( C O ) . i + M
F e ° -> F e
+ +
m
+
+
+ 2e
H
+
+
2e"
In Inorganic Compounds with Unusual Properties—II; King, R.; Advances in Chemistry; American Chemical Society: Washington, DC, 1979.
(8)
2e
(9)
(10)
128
INORGANIC
Table II.
COMPOUNDS
WITH
UNUSUAL
PROPERTIES
Catalytic Reductions w i t h F e ( C O ) s
II
0
% Compound
Product
N i t r o b e n z e n e (11.0 m-Dinitrobenzene 2,4-Dinitrotoluene 2,6-Dinitrotoluene
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% Nitroarene Reduced
g) (8.2 g) (16.8 g) (9.3 g)
aniline m-phenylene diamine 2,4-diaminotoluene 2,6-diaminotoluene
Fe(CO), Remaining b
100 100 100 100
95 12 32 56
"Reaction conditions: the nitro compound dissolved in 50 m L of glyme was pumped over a 10-12 hr period into a stirred 300 m L reaction vessel containing 120 m L of glyme, 6g H 0 , 30 g of E t N , and 1 g Fe(CO)s. The reaction was run at room temperature under 1700 psi of C O . Determined by I R absorption intensities. 2
3
6
r e l a t i v e l y l o n g p e r i o d of t i m e ( a p p r o x i m a t e l y 12 h r ) . the F e ( C O )
5
E v e n so, s o m e of
w a s d e s t r o y e d a n d a p p e a r e d as oxides of i r o n . T h e p e r t i -
n e n t d a t a are s h o w n i n T a b l e I I . I n a separate, n o n c a t a l y t i c t y p e of e x p e r i m e n t , w e d e m o n s t r a t e d t h a t n i t r o b e n z e n e c o u l d b e r a p i d l y r e d u c e d t o a n i l i n e i n a l k a l i n e s o l u t i o n s of K H F e ( C O ) m a i n t a i n e d at a p H of 12.0; this i n d i c a t e d t h a t the H F e ( C O ) 4
anion rather than H F e ( C O ) 2
4
is c a p a b l e of e f f e c t i n g the r e d u c t i o n .
o u r e a r l i e r studies d e a l i n g w i t h h y d r o f o r m y l a t i o n ( 1 3 ) ,
4
In
w e have shown
t h a t s e v e r a l m e t a l c l u s t e r species r e a d i l y generate m e t a l h y d r i d e a n i o n s u p o n t r e a t m e n t w i t h m i l d bases, a n d these w e r e also tested as c a n d i d a t e s f o r t h e c a t a l y t i c r e d u c t i o n of n i t r o b e n z e n e t o a n i l i n e w i t h C O -f- H 0 as 2
t h e r e d u c i n g agent. T h e results o b t a i n e d are s u m m a r i z e d i n T a b l e
Table III.
Reduction of Nitrobenzene with C O +
Catalyst Rh (CO) Ru (CO) H Ru (CO)i2 Os (CO) H Os (CO) H Os (CO) Ir (CO)i2 [Bu N] [Pt3(CO) ] Re (CO) e
1 6
3
1 2
4
4
3
1 2
2
3
1 0
4
3
1 2
4
4
2
2
6
1 0
5
T
Time (hr)
125 100 100 180 180 180 150 125 180
1 2 2 1 1 1 10 10 2
III.
H 0 2
Reduction (%)
(%)
100 71 73 100 100 100 47 42 10
2-6 52 56