US5144068A
Expired / Lapsed
US
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Methanol carbonylation process
Assignee: Celanese International Corp
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Filing: 1991-01-07
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Granted: 1992-09-01
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Expires: 2011-01-07
Abstract
Abstract An alcohol such as methanol is reacted with carbon monoxide in a liquid reaction medium containing a rhodium catalyst stabilized with an iodide salt, especially lithium iodide, along with alkyl iodide such as methyl iodide and alkyl acetate such as methyl acetate in specified proportions. With a finite concentration of water in the reaction medium the product is the carboxylic acid instead of, for example, the anhydride. The present reaction system not only provides an acid product of unusually low water content at unexpectedly favorable reaction rates but also, whether the water content is low or, as in the case of prior-art acetic acid technology, relatively high, is characterized by unexpectedly high catalyst stability; i.e., it is resistant to catalyst precipitation out of the reaction medium.
Inventors
- 👤 Brad L. Smith
- 👤 G. Paull Torrence
- 👤 Adolfo Aguilo
- 👤 James S. Alder
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 13:52
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/10; C07C51/12
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
136 words
In a process for producing acetic acid by reacting methanol with carbon monoxide in a liquid reaction medium containing a rhodium catalyst and comprising water, acetic acid, methyl iodide, and methyl acetate and subsequently recovering acetic acid from the resulting reaction product, the improvement which comprises: maintaining catalyst stability and system productivity by maintaining in said reaction medium during the course of said reaction about 0.1 wt% to less than 14 wt% of water together with (a) an effective amount in the range of about 2 wt% to 20 wt% of a catalyst stabilizer selected from the group consisting of iodide salts which are soluble in said reaction medium in effective concentration at reaction temperature, (b) about 5 wt% to 20 wt% of methyl iodide, and (c) about 0.5 wt% to 30 wt% of methyl acetate.
Claim 2
Dependent Claim
136 words
In a process for producing acetic acid by reacting methanol with carbon monoxide in a liquid reaction medium containing a rhodium catalyst and comprising water, acetic acid, methyl iodide, and methyl acetate and subsequently recovering acetic acid from the resulting reaction product, the improvement which comprises: maintaining catalyst stability and system productivity by maintaining in said reaction medium during the course of said reaction about 0.1 wt% to less than 14 wt% of water together with (a) an effective amount in the range of about 2 wt% to 20 wt% of a catalyst stabilizer selected from the group consisting of iodide salts which are soluble in said reaction medium in effective concentration at reaction temperature, (b) about 5 wt% to 20 wt% of methyl iodide, and (c) about 0.5 wt% to 30 wt% of methyl acetate.
Claim 3
Dependent Claim
38 words
The process of claim 1 wherein said iodide salt is a quaternary iodide salt or an iodide salt of a member of the group consisting of the metals of Group Ia and Group IIa of the periodic table.
Claim 4
Dependent Claim
14 words
The process of claim 2 wherein said iodide salt is an alkali metal iodide.
Claim 5
Dependent Claim
12 words
The process of claim 3 wherein the iodide salt is lithium iodide.
Claim 6
Dependent Claim
29 words
The process of claim 4 wherein the rhodium catalyst is maintained in said reaction medium in a concentration of about 200 ppm to about 1000 ppm calculated as rhodium.
Claim 7
Dependent Claim
48 words
The process of claim 5 wherein there is maintained in the reaction medium about 1 to less than 14 wt% water, 10 to 20 wt% lithium iodide, 12 to 16 wt% methyl iodide, and 0.5 to 5 wt% methyl acetate, with the balance consisting essentially of acetic acid.
Claim 8
Dependent Claim
25 words
The process of claim 1 comprising maintaining in said reaction medium during the course of said reaction about 1 wt.% to about 12 wt.% water.
Claim 9
Dependent Claim
25 words
The process of claim 1 comprising maintaining in said reaction medium during the course of said reaction about 1 wt.% to about 10 wt.% water.
Claim 10
Dependent Claim
54 words
The process of claims 1, 7 or 8 wherein said iodide salt is lithium iodide and maintaining in said reaction medium during the course of said reaction 10 to 20 wt.% lithium iodide, 0.5 to 5 wt.% methyl acetate and 10 to 16 wt.% methyl iodide, with the balance consisting essentially of acetic acid.
Claim 11
Dependent Claim
25 words
The process of claim 9 comprising maintaining in said reaction medium during the course of said reaction 2 to 5 wt.% of said methyl acetate.
Claim 12
Dependent Claim
27 words
The process of claim 9 comprising maintaining in said reaction medium during the course of said reaction about 12 to about 16 wt.% of said methyl iodide.
Claim 13
Dependent Claim
121 words
In a process for producing acetic acid by reacting methanol with carbon monoxide in a liquid reaction medium containing a rhodium catalyst and comprising water, acetic acid, methyl iodide, and methyl acetate and subsequently recovering acetic acid from the resulting reaction produce, the improvement which comprises: maintaining catalyst stability and system productivity by maintaining in said reaction medium during the course of said reaction about 0.1 wt.% to less than 14 wt.% of water together with (a) about 2 wt.% to 20 wt.% of a catalyst stabilizer selected from the group consisting of lithium iodide, lithium acetate, and mixtures thereof, (b) about 5 wt.% to 20 wt.% of methyl iodide, and (c) about 0.5 wt.% to 30 wt.% of methyl acetate.
Claim 14
Dependent Claim
121 words
In a process for producing acetic acid by reacting methanol with carbon monoxide in a liquid reaction medium containing a rhodium catalyst and comprising water, acetic acid, methyl iodide, and methyl acetate and subsequently recovering acetic acid from the resulting reaction produce, the improvement which comprises: maintaining catalyst stability and system productivity by maintaining in said reaction medium during the course of said reaction about 0.1 wt.% to less than 14 wt.% of water together with (a) about 2 wt.% to 20 wt.% of a catalyst stabilizer selected from the group consisting of lithium iodide, lithium acetate, and mixtures thereof, (b) about 5 wt.% to 20 wt.% of methyl iodide, and (c) about 0.5 wt.% to 30 wt.% of methyl acetate.
Claim 15
Dependent Claim
25 words
The process of claim 12 comprising maintaining in said reaction medium during the course of said reaction about 1 wt.% to about 12 wt.% water.
Claim 16
Dependent Claim
25 words
The process of claim 12 comprising maintaining in said reaction medium during the course of said reaction about 1 wt.% to about 10 wt.% water.
Claim 17
Dependent Claim
53 words
The process of claims 12, 17 or 18 comprising maintaining in said reaction medium during the course of said reaction 10 to 20 wt.% of said catalyst stabilizer, 10 to 16 wt.% of said methyl iodide and 0.5 to 5 wt.% of said methyl acetate, with the balance consisting essentially of acetic acid.
Claim 18
Dependent Claim
25 words
The process of claim 15 comprising maintaining in said reaction medium during the course of said reaction 2 to 5 wt.% of said methyl acetate.
References Cited (Backward Citations)
GB1468940A
Cited
US5001259A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1995-09-01 | 1996-03-02 | 1996-09-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-09-01 | 2000-03-02 | 2000-09-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-09-01 | 2004-03-02 | 2004-09-01 | $7700.00 | Window Closed / Lapsed |