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US4177250A
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US
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Method of removing acetylene and sulfur compounds from gases by absorption in dimethyl formamide
Assignee: Phillips Petroleum Co
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Filing: 1977-10-18
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Granted: 1979-12-04
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Expires: 1997-10-18
Abstract
Abstract Dimethyl formamide when used as an absorption solvent to remove acetylenes from olefin-containing gas streams acts as well as a promoter for the oxidative conversion of H 2 S, COS, and/or CS 2 , also contained in the feed stream, to elemental sulfur. Thus both acetylenes and sulfur compounds are efficiently removed from such olefin-containing gas streams as coke oven gas. Further, the loss of dimethyl formamide entrained and vaporized by the deacetylenized gas stream leaving the dimethyl formamide absorber is substantially reduced or effectively eliminated by the injection of a stream of liquid selected from the group consisting of paraffinic hydrocarbons having 4-8 carbon atoms per molecule containing at least one tertiary carbon atom per molecule and aromatic hydrocarbons having 6-10 carbon atoms per molecule above the point of injection of the dimethyl formamide solvent stream to the absorption column. This liquid stream injection is particularly advantageous when the stream is also a reactant in a downstream alkylation process.
Inventors
- 👤 Howard B. Irvin
- 👤 Fred T. Sherk
- 👤 Alfred A. Hoffman, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 20:33
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/08; C10K1/16; B; B01; B01D; B01D53/00; B01D53/14; B01D53/1418; B01D53/1456; B01D53/1487; B01D53/1493; C07; C07C; C07C15/00; C07C15/02; C07C7/00; C07C7/11; Y; Y10; Y10S; Y10S585/00; Y10S585/909; Y10S585/91
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
192 words
A process for the simultaneous desulfurization of and acetylene removal from a gas which process comprises contacting a gas stream comprising an olefin and oxygen, and, as contaminants, acetylenes and at least one oxidizable sulfur compound selected from the group consisting of H 2 S, COS, and CS 2 , in an absorption zone with liquid dimethyl formamide such as to produce a gaseous effluent comprising the olefin and being essentially acetylene-free and a liquid effluent comprising dimethyl formamide, acetylenes, and sulfur, introducing a liquid hydrocarbon selected from the group consisting of paraffinic hydrocarbons having 4-8 carbon atoms per molecule, containing at least one tertiary carbon atom per molecule, and aromatic hydrocarbons having 6-10 carbon atoms per molecule into the absorption zone at a location above the location of introduction of said dimethyl formamide, and withdrawing a gaseous effluent stream from said absorption zone comprising said olefin and said hydrocarbon and being essentially acetylene and sulfur-free and introducing at least a portion of said gaseous effluent into an alkylation zone and reacting said olefin and said hydrocarbon in the presence of an alkylation catalyst to form an alkylate in said alkylation zone.
Claim 2
Dependent Claim
192 words
A process for the simultaneous desulfurization of and acetylene removal from a gas which process comprises contacting a gas stream comprising an olefin and oxygen, and, as contaminants, acetylenes and at least one oxidizable sulfur compound selected from the group consisting of H 2 S, COS, and CS 2 , in an absorption zone with liquid dimethyl formamide such as to produce a gaseous effluent comprising the olefin and being essentially acetylene-free and a liquid effluent comprising dimethyl formamide, acetylenes, and sulfur, introducing a liquid hydrocarbon selected from the group consisting of paraffinic hydrocarbons having 4-8 carbon atoms per molecule, containing at least one tertiary carbon atom per molecule, and aromatic hydrocarbons having 6-10 carbon atoms per molecule into the absorption zone at a location above the location of introduction of said dimethyl formamide, and withdrawing a gaseous effluent stream from said absorption zone comprising said olefin and said hydrocarbon and being essentially acetylene and sulfur-free and introducing at least a portion of said gaseous effluent into an alkylation zone and reacting said olefin and said hydrocarbon in the presence of an alkylation catalyst to form an alkylate in said alkylation zone.
Claim 3
Dependent Claim
24 words
A process in accordance with claim 1 comprising separating said liquid effluent into a dimethyl formamide stream, an acetylene stream, and a sulfur stream.
Claim 4
Dependent Claim
62 words
A process in accordance with claim 1 comprising passing said liquid effluent to a separation zone in which said liquid effluent is separated into a gaseous stream comprising acetylenes and a liquid stream comprising dimethyl formamide and sulfur, passing said liquid stream to a settler and withdrawing a sulfur stream from said settler and withdrawing a dimethyl formamide stream from said settler.
Claim 5
Dependent Claim
25 words
A process in accordance with claim 2 wherein said dimethyl formamide stream is recycled into said absorption zone to absorb said acetylenes from said gas.
Claim 6
Dependent Claim
27 words
A process in accordance with claim 3 wherein said dimethyl formamide stream withdrawn from said settler is passed through indirect heat exchange relationship with said liquid effluent.
Claim 7
Dependent Claim
41 words
A process in accordance with claim 1 wherein said gas stream is a coke oven gas consisting essentially of hydrogen, nitrogen, oxygen, carbon monoxide, carbon dioxide, COS, H 2 S, methane, acetylene, ethylene, ethane, methylacetylene, propylene, propane, and some heavier hydrocarbons.
Claim 8
Dependent Claim
209 words
A process for the simultaneous desulfurization of and acetylene removal from a gas which process comprises the steps of (a) contacting a gas stream comprising an olefin and oxygen, and, as contaminants, acetylenes and at least one oxidizable sulfur compound selected from the group consisting of H 2 S, COS, and CS 2 , in an absorption zone with liquid dimethyl formamide such as to remove the acetylenes from said gas and to convert the sulfur compounds into elemental sulfur, (b) injecting a liquid hydrocarbon selected from the group consisting of paraffinic hydrocarbons having 4-8 carbon atoms per molecule, containing at least one tertiary carbon atom per molecule, and aromatic hydrocarbons having 6-10 carbon atoms per molecule into an absorption zone at a location above the location of introduction of said dimethyl formamide, (c) separating the liquid bottoms effluent obtained from the absorber in step (a) into a gas stream comprising acetylene, a first liquid stream consisting essentially of pure dimethyl formamide and a second liquid stream consisting essentially of sulfur, and (d) passing the gaseous overhead stream obtained from the absorber in step (a), wherein said gaseous overhead stream comprises said olefin and a portion of the liquid hydrocarbon injected in step (b), to a downstream alkylation process.
Claim 9
Dependent Claim
209 words
A process for the simultaneous desulfurization of and acetylene removal from a gas which process comprises the steps of (a) contacting a gas stream comprising an olefin and oxygen, and, as contaminants, acetylenes and at least one oxidizable sulfur compound selected from the group consisting of H 2 S, COS, and CS 2 , in an absorption zone with liquid dimethyl formamide such as to remove the acetylenes from said gas and to convert the sulfur compounds into elemental sulfur, (b) injecting a liquid hydrocarbon selected from the group consisting of paraffinic hydrocarbons having 4-8 carbon atoms per molecule, containing at least one tertiary carbon atom per molecule, and aromatic hydrocarbons having 6-10 carbon atoms per molecule into an absorption zone at a location above the location of introduction of said dimethyl formamide, (c) separating the liquid bottoms effluent obtained from the absorber in step (a) into a gas stream comprising acetylene, a first liquid stream consisting essentially of pure dimethyl formamide and a second liquid stream consisting essentially of sulfur, and (d) passing the gaseous overhead stream obtained from the absorber in step (a), wherein said gaseous overhead stream comprises said olefin and a portion of the liquid hydrocarbon injected in step (b), to a downstream alkylation process.
Claim 10
Dependent Claim
29 words
A process in accordance with claim 1 wherein said liquid hydrocarbon is benzene and wherein said olefin is selected from the group consisting of ethylene, propylene and mixtures thereof.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-12-03 | 1983-06-04 | 1983-12-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-12-03 | 1987-06-04 | 1987-12-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-12-03 | 1991-06-04 | 1991-12-04 | $7700.00 | Window Closed / Lapsed |