Patent EP0567331A2 successfully refreshed from Google Patents.
EP0567331A2
Expired / Lapsed
EP
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Process for the production of acetic acid from methanol and carbon monoxide using supported rhodium catalyst
Assignee: Chiyoda Corp
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Filing: 1993-04-22
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Granted: —
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Expires: 2013-04-22
Abstract
Abstract A liquid feed containing methanol, carbon monoxide, an alkyl iodide and a solvent is contacted with a supported rhodium catalyst to produce acetic acid at a temperature of 140-250 °C and a pressure of 15-60 kg/cm 2 G with a partial pressure of carbon monoxide of 7-30 kg/cm 2 while maintaining (a) the water concentration of the product solution in the range of 0.5-10 % by weight and (b) the carbonylation degree C r , defined in the specification, of the solution within the reactor at 0.15 or more. The solvent may be a carboxylic acid or a carboxylic acid ester.
Inventors
- 👤 Noriyuki Yoneda
- 👤 Yoshimi Shiroto
- 👤 Kazuhiko Hamato
- 👤 Sachio Asaoka
- 👤 Tetsuo Maejima
Bibliographic Details
Application Number
—
Jurisdiction
EP
Data Source
google_patents
Last Synchronized
2026-11-01 10:12
CPC Classifications
B; B01; B01J; B01J31/00; B01J31/16; B01J31/18; B01J31/1805; B01J31/181; B01J31/165; B01J31/1658; C; C07; C07C; C07C51/00; C07C51/10; C07C51/12; B01J2531/00; B01J2531/80; B01J2531/82; B01J2531/822
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
322 words
A process for the production of acetic acid, comprising the steps of introducing a feed including methanol, carbon monoxide, an alkyl iodide and a solvent into a reaction zone containing a solid catalyst including an insoluble, pyridine-containing resin substrate, and a rhodium compound supported on said substrate; contacting said feed with said solid catalyst to react said methanol with said carbon monoxide and to obtain a reaction solution; and discharging at least a portion of said reaction solution from said reaction zone to obtain a product solution, characterized in that said solvent includes at least one organic solvent selected from the group consisting of carboxylic acids having at least two carbon atoms and carboxylic acid esters having at least two carbon atoms, and in that said reaction is performed at a temperature of 140-250 °C and a pressure of 15-60 kg/cm 2 G with a partial pressure of carbon monoxide of 7-30 kg/cm 2 while maintaining (a) the water concentration of said product solution in the range of 0.5-10 % by weight and (b) the carbonylation degree C r of the solution within said reaction zone at 0.15 or more, wherein the carbonylation degree C r is given by the following equation: wherein M[CH 3 COOH], M[CH 3 COOCH 3] , M[CH 3 COOR 1 ], M[CH 3 OCH 3 ], M[R 2 COOCH 3] , M[CH 3 0R 3 ] and M[CH 3 0H] represent the amounts, in terms of molarity, of CH 3 COOH, CH 3 COOCH 3 , CH 3 COOR 1 where R 1 represents an alkyl group having at least two carbon atoms, CH 3 0CH 3 , R 2 COOCH 3 where R 2 represents an alkyl group having at least two carbon atoms, CH 3 OR 3 where R 3 represents an alkyl group having at least two carbon atoms and CH 3 OH, respectively, which are present in the solution within said reaction zone.
Claim 2
Dependent Claim
322 words
A process for the production of acetic acid, comprising the steps of introducing a feed including methanol, carbon monoxide, an alkyl iodide and a solvent into a reaction zone containing a solid catalyst including an insoluble, pyridine-containing resin substrate, and a rhodium compound supported on said substrate; contacting said feed with said solid catalyst to react said methanol with said carbon monoxide and to obtain a reaction solution; and discharging at least a portion of said reaction solution from said reaction zone to obtain a product solution, characterized in that said solvent includes at least one organic solvent selected from the group consisting of carboxylic acids having at least two carbon atoms and carboxylic acid esters having at least two carbon atoms, and in that said reaction is performed at a temperature of 140-250 °C and a pressure of 15-60 kg/cm 2 G with a partial pressure of carbon monoxide of 7-30 kg/cm 2 while maintaining (a) the water concentration of said product solution in the range of 0.5-10 % by weight and (b) the carbonylation degree C r of the solution within said reaction zone at 0.15 or more, wherein the carbonylation degree C r is given by the following equation: wherein M[CH 3 COOH], M[CH 3 COOCH 3] , M[CH 3 COOR 1 ], M[CH 3 OCH 3 ], M[R 2 COOCH 3] , M[CH 3 0R 3 ] and M[CH 3 0H] represent the amounts, in terms of molarity, of CH 3 COOH, CH 3 COOCH 3 , CH 3 COOR 1 where R 1 represents an alkyl group having at least two carbon atoms, CH 3 0CH 3 , R 2 COOCH 3 where R 2 represents an alkyl group having at least two carbon atoms, CH 3 OR 3 where R 3 represents an alkyl group having at least two carbon atoms and CH 3 OH, respectively, which are present in the solution within said reaction zone.
Claim 3
Dependent Claim
49 words
A process as claimed in claim 1, wherein the solution within said reaction zone contains carbonyl group-containing compounds having at least two carbon atoms in an amount of at least 0.30 part by weight per part by weight of the methanol present in the solution within said reaction zone.
Claim 4
Dependent Claim
280 words
A process as claimed in claim 1, wherein said reaction is performed while maintaining the following conditions (c)-(e): (c) the water concentration of said product solution being 1-5 % by weight, (d) the carbonylation degree Cp of said product solution being at least 0.80, and (e) the water content W f of said feed being 0.30 or less, said carbonylation degree Cp and said water content W f being given by the following equations: wherein M[CH 3 COOH], M[CH 3 COOCH 3] , M[CH 3 COOR 1 ], M[CH 3 OCH 3 ], M[R 2 COOCH 3] , M[CH 3 OR 3 ] and M[CH 3 0H] represent the amounts, in terms of molarity, of CH 3 COOH, CH 3 COOCH 3 , CH 3 COOR 1 where R 1 represents an alkyl group having at least two carbon atoms, CH 3 0CH 3 , R 2 COOCH 3 where R 2 represents an alkyl group having at least two carbon atoms, CH 3 OR 3 where R 3 represents an alkyl group having at least two carbon atoms and CH 3 OH, respectively, which are present in said product solution, and wherein M[H 2 0], M[CH 3 COOCH 3] , M[CH 3 COOR 1 ], M[R 2 COOCH 3] , M[CH 3 OCH 3 ], M[CH 3 OR 3 ], M[R 4 0R 5 ]) and M[CH 3 0H] represent the amounts, in terms of molarity, of H 2 0, CH 3 COOCH 3 , CH 3 COOR 1 , R- 2 COOCH 3 , CH 3 0CH 3 , CH 3 0R 3 , R 4 OR 5 and CH 3 OH which are present in said feed.
Claim 5
Dependent Claim
14 words
A process as claimed in claim 1, wherein said alkyl iodide is methyl iodide.
Claim 6
Dependent Claim
39 words
A process as claimed in claim 1, wherein said solid catalyst is used in an amount of at least 400 ppm by weight in terms of elemental rhodium based on the weight of the solution within said reaction zone.
Claim 7
Dependent Claim
131 words
A process for the production of acetic acid, comprising reacting, in a reaction zone, carbon monoxide with methanol in a solvent at a temperature of 140-250 °C in the presence of an alkyl iodide and a solid catalyst including an insoluble, pyridine-containing resin substrate, and rhodium supported on said substrate, characterized in that said solvent includes an organic solvent selected from the group consisting of those having at least two carbonyl groups and mixtures thereof, that said reaction is performed at a pressure of 15-60 kg/cm 2 G with a partial pressure of carbon monoxide of 7-30 kg/cm 2 , and that the solution within said reaction zone contains said organic solvent in an amount of at least 0.30 part by weight per part by weight of the methanol contained therein.
Claim 8
Dependent Claim
131 words
A process for the production of acetic acid, comprising reacting, in a reaction zone, carbon monoxide with methanol in a solvent at a temperature of 140-250 °C in the presence of an alkyl iodide and a solid catalyst including an insoluble, pyridine-containing resin substrate, and rhodium supported on said substrate, characterized in that said solvent includes an organic solvent selected from the group consisting of those having at least two carbonyl groups and mixtures thereof, that said reaction is performed at a pressure of 15-60 kg/cm 2 G with a partial pressure of carbon monoxide of 7-30 kg/cm 2 , and that the solution within said reaction zone contains said organic solvent in an amount of at least 0.30 part by weight per part by weight of the methanol contained therein.
Claim 9
Dependent Claim
34 words
A process as claimed in claim 6, wherein said alkyl iodide is methyl iodide and said organic solvent includes at least one member selected from the group consisting of acetic acid and methyl acetate.
Claim 10
Dependent Claim
39 words
A process as claimed in claim 6, wherein said solid catalyst is used in an amount of at least 400 ppm by weight in terms of elemental rhodium based on the weight of the solution within said reaction zone.
References Cited (Backward Citations)
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