Methanol Carbonylation System with Multiple Absorber Feed Options
First Claim
Patent Images
1. An apparatus for producing acetic acid comprising:
- (a) a reactor for carbonylating methanol or its reactive derivatives, the reactor containing a catalyst selected from rhodium catalysts, iridium catalysts and mixtures thereof, and a methyl iodide promoter in an acetic acid reaction mixture;
(b) a feed system for providing carbon monoxide and methanol or its reactive derivatives to the reactor;
(c) a flash system configured to receive a stream of the reaction mixture and separate it into (i) at least a first liquid recycle stream, and (ii) a crude process stream containing acetic acid;
(d) a first distillation column coupled to the flash system, the first distillation column being adapted to separate low boiling components including methyl iodide from the crude process stream, and generate a purified process stream,the first distillation column and optionally the reactor and flash system also operating to generate a vent gas stream comprising volatile organic components including methyl iodide;
(e) an absorber tower adapted for receiving the vent gas stream and removing methyl iodide therefrom with a scrubber solvent, the absorber tower also being coupled to first and second scrubber solvent sources which are capable of supplying different first and second scrubber solvents; and
(f) a switching system for alternatively providing first or second scrubber solvents to the absorber tower from either the first scrubber solvent source or the second scrubber solvent source.
0 Assignments
0 Petitions
Accused Products
Abstract
A methanol carbonylation system 10 includes an absorber tower 75 adapted for receiving a vent gas stream and removing methyl iodide therefrom with a scrubber solvent, the absorber tower being coupled to first and second scrubber solvent sources 16, 56 which are capable of supplying different first and second scrubber solvents. A switching system including valves 90, 92, 94, 96, 98 alternatively provides first or second scrubber solvents to the absorber tower and returns the used solvent and sorbed material to the carbonylation system to accommodate different operating modes.
-
Citations
14 Claims
-
1. An apparatus for producing acetic acid comprising:
-
(a) a reactor for carbonylating methanol or its reactive derivatives, the reactor containing a catalyst selected from rhodium catalysts, iridium catalysts and mixtures thereof, and a methyl iodide promoter in an acetic acid reaction mixture; (b) a feed system for providing carbon monoxide and methanol or its reactive derivatives to the reactor; (c) a flash system configured to receive a stream of the reaction mixture and separate it into (i) at least a first liquid recycle stream, and (ii) a crude process stream containing acetic acid; (d) a first distillation column coupled to the flash system, the first distillation column being adapted to separate low boiling components including methyl iodide from the crude process stream, and generate a purified process stream, the first distillation column and optionally the reactor and flash system also operating to generate a vent gas stream comprising volatile organic components including methyl iodide; (e) an absorber tower adapted for receiving the vent gas stream and removing methyl iodide therefrom with a scrubber solvent, the absorber tower also being coupled to first and second scrubber solvent sources which are capable of supplying different first and second scrubber solvents; and (f) a switching system for alternatively providing first or second scrubber solvents to the absorber tower from either the first scrubber solvent source or the second scrubber solvent source. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9)
-
-
10. An improved method of operating an apparatus for making acetic acid of the class including a production system having a reactor containing a reaction medium and a product purification train wherein the production system is vented to an absorber tower, the improvement comprising:
-
(a) carbonylating methanol or reactive derivatives thereof in the reactor in the presence of a Group VIII metal catalyst and a methyl iodide promoter while maintaining a concentration of water in the reactor of from 1-10% by weight of the reaction medium and concurrently maintaining in the reactor a predetermined partial pressure of carbon monoxide; (b) venting non-condensables from the production system so as to provide low pressure vent gas only; (c) feeding the low pressure vent gas from the production system to the absorber tower, the vent gas including methyl iodide and optionally additional volatile components; (d) supplying a scrubber solvent to the absorber tower, the scrubber solvent comprising methanol, methyl acetate or mixtures thereof; (e) contacting the low pressure vent gas with the scrubber solvent thereby removing methyl iodide and optionally additional volatile components from the gas and absorbing methyl iodide and optionally additional volatile components into the scrubber solvent; and (f) feeding an absorber return stream including scrubber solvent and absorbed methyl iodide and optionally additional absorbed volatile components to the reactor. - View Dependent Claims (11, 12, 13, 14)
-
Specification