EP0801050A1
Expired / Lapsed
EP
⏱️ 0.0 years remaining
Process for the preparation of acetic acid
Assignee: Topsoe AS
•
Filing: 1997-03-21
•
Granted: —
•
Expires: 2017-03-21
Abstract
Abstract The invention comprises catalytical steps of converting hydrogen and carbon monoxide in the synthesis gas to a mixed process stream containing methanol and dimethyl ether (DME) and carbonylating methanol and DME formed in the process stream into acetic acid. Carbon monoxide for use in the carbonylation step is recovered directly from the feed gas to the first reaction step of the above process.
Inventors
- 👤 Finn Joensen
- 👤 Bodil Voss
- 👤 Ib Dybkjaer
Bibliographic Details
Application Number
—
Jurisdiction
EP
Data Source
google_patents
Last Synchronized
2026-11-01 07:42
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C29/00; C07C29/15; C07C29/151; C07C51/00; C07C51/10; C07C51/12; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
190 words
A process for the preparation of acetic acid by catalytic conversion of a synthesis gas being rich in hydrogen and carbon monoxide, comprising steps of: (i) introducing a stream of the synthesis gas into a first reaction step at a predetermined pressure and temperature and reacting the synthesis gas in the presence of a catalyst being active in formation of methanol and dehydration of methanol, so as to obtain a gaseous process phase containing methanol, dimethyl ether, and water; (ii) cooling the gaseous process phase of step (i) and obtaining a liquid phase with the methanol, dimethyl ether and water and a gaseous phase comprising carbon dioxide and residual amounts of dimethyl ether; (iii) introducing the liquid phase formed in step (ii) into a second reaction step at a predetermined pressure and temperature and adding a predetermined amount of carbon monoxide; and (iv) carbonylating methanol and dimethyl ether in the liquid phase with carbon monoxide by contact with a catalyst being active in the carbonylation of alcohols and ethers with carbon monoxide; and (v) recovering from effluent of step (iv) a product stream mainly consisting of the acetic acid product.
Claim 2
Dependent Claim
76 words
The process of claim 1, comprising the further steps of: prior to introducing the synthesis gas into the first reaction step dividing the gas into a first and second portion; passing the first portion of the gas to step (i) of the process; treating the second portion of the gas for separation of carbon monoxide contained therein; and passing carbon monoxide separated from the second portion of the synthesis gas to step (iv) of the process.
Claim 3
Dependent Claim
23 words
The process of claim 2, wherein the treatment for carbon monoxide recovery comprises membrane separation of the carbon monoxide from the synthesis gas.
Claim 4
Dependent Claim
23 words
The process of claim 2, wherein the treatment for carbon monoxide recovery comprises cryogenic separation of the carbon monoxide from the synthesis gas.
Claim 5
Dependent Claim
26 words
The process of claim 2, wherein the volume ratio of the first and second portion of the divided synthesis gas stream is between 0.5:1 and 2:1.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
Maintenance schedule is calculated for granted US utility patents.