H H H H
| | | |
C = C + H O + CO -------------> C = C
| | 2 | |
H H H C=O
|
OH
The synthesis of acrylic acid from ethylene, water, and carbon monoxide is
carried out at 200 deg C and 60 to 200 atm in tetrahydrofuran, with nickel
bromide used as the catalyst.
H H H H H H
| | oxidation | | | |
C = C ----------> C = C ----> C = C
| | | | | |
H CH3 H C=O H C=O
| |
H OH
The above is carried out in one step by passing a mixture of 10% propylene,
50% air, and 40% steam over a cobalt molybdenum catalyst at 400-500 deg C.
O OH H SO
|| HCN | 2 4 ??I can't make further sense
H C - C - CH ----> CH - C - CN -----> of the notes from here
3 3 3 |
CH
3
Synthesis of Esters of Acrylic Acid
H H H H
| | | |
HO - C - C - CN + CH -CH -OH + H SO ---> C = C + NH (+) (-)HSO
| | 3 2 2 4 | | 4 4
H H H C=O
|
O - CH - CH
2 3
Higher acrylates are prepared by choosing the proper alchol or by
the esterification of acrylic acid.
CH3 H CH3 H CH3
| conc. | | aq. MeOH | |
CH - C - CN -----> C = C --------> C = C
3 | H SO | | | |
OH 2 4 H C=O H C=O
| |
NH (+) O-CH
3 3
HSO(-)
4
The middle product is fed directly into aqueous methanol.
H H H H
| | | |
C = C + Nc(CO) + EtOH --> C = C
| | 4 | |
H H H C=O
|
O-CH -CH
2 3
Two syntheses of acrylonitrile- ethylene feedstocks
H H H H
| | | |
C = C + HCN ---> C = C
| | | |
H H H C
|||
N
The catalyst is cuprous chloride in HCl, and the reaction is carried out in
a liquid phase. The acetylene is passed through a solution of HCN with the
catalyst at 80- 90 deg C. The reactor effluent is cooled and passed into
water, where the acrylonitrile is extracted, stripped with steam and purified
by passage through a series of distillation columns, the last of which
operates under reduced pressure.H H O O OH CN H H | | 2 / \ HCN | | | | C = C + HCN ---> H-C = C-H ---> H-C - C-H ---> C = C | | | | | | | | H H H H H H H CNDehydration is carried out in the vapor phase over activated alumina at 300 deg C.
H H NH , O H H
| | 3 2 | |
C = C -------> C = C + 3 H O
| | | | 2
H CH H CN
3
catalyzed by Bi, U, M at 400 to 500 deg C, 1 to 3 atm
H H H H
| | 3 NO | |
2 C = C -------> C = C + N + 3H O
| | | | 2 2
H CH H C
3 |||
N
catalysed by silver
H H H H
| | | |
C = C + H O -----> C = C
| | 2 | |
H C H C=O
||| |
N NH
2
H H H H
| | | |
C = C ----> -[- C = C -]-
| | | |
H C=O H C=O
| |
OH OH
acrylic acid poly(acrylic acid)
and
H CH3 H CH3
| | | |
C = C ----> -[- C = C -]-
| | | |
H C=O H C=O
| |
OH OH
methacrylic acid poly(methacrylic acid)
A free radical process using solution polymerization is possible using
water as the solvent. Note that for solution polymerization there will
be a correlation between the growing polymer molecular weight and
viscosity. This differs from the emulsion and suspension polymerizations
in water discussed previously.
H H H H
| | | |
C = C + H O + CO -------------> C = C
| | 2 | |
H H H C=O
|
OH
H H H H H H
| | oxidation | | | |
C = C ----------> C = C ----> C = C
| | | | | |
H CH3 H C=O H C=O
| |
H OH
The above is carried out in one step by passing a mixture of 10% propylene,
50% air, and 40% steam over a cobalt molybdenum catalyst at 400-500 deg C.
H H H H
| | | |
C = C + Nc(CO) + EtOH --> C = C
| | 4 | |
H H H C=O
|
O-CH -CH
2 3
The above is carried out in one step by passing a mixture of 10% propylene,
50% air, and 40% steam over a cobalt molybdenum catalyst at 400-500 deg C.