Patent US3961035A successfully refreshed from Google Patents.
US3961035A
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Process for preparing hydrogen sulfide
Assignee: Stauffer Chemical Co
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Filing: 1974-03-27
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Granted: 1976-06-01
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Expires: 1994-03-27
Abstract
Abstract The invention is a method for preparing hydrogen sulfide by reacting a gas mixture containing carbon monoxide with sulfur to provide a gas mixture containing carbonyl sulfide and reacting the gas mixture containing carbonyl sulfide with water in the vapor phase to provide a gas mixture containing hydrogen sulfide. The process is preferrably operated continuously. The water can be present in the step in which the carbon monoxide is reacted with the sulfur.
Inventors
- 👤 Harold S. Mickley
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 20:14
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/16; C01B17/161
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
148 words
A process for preparing hydrogen sulfide which comprises: a. providing a gas mixture containing carbon monoxide; b. heating said gas mixture to a temperature above about 500°F. by direct heat exchange with a heated material whereby the heated material is cooled in a first zone; c. introducing sulfur into the gas mixture and reacting the gas mixture with the sulfur at a temperature between about 500° and 1300°F. to form a gas mixture containing carbonyl sulfide in a second zone; d. reacting the gas mixture containing carbonyl sulfide with water, in the vapor phase, at a temperature between about 400°F. and about 1300°F. to form a reacted gas mixture containing hydrogen sulfide in a third zone; and e. cooling said reacted gas mixture by direct heat exchange with a cooled material whereby said cooled material is heated to be used as the heated material in said first zone.
Claim 2
Dependent Claim
148 words
A process for preparing hydrogen sulfide which comprises: a. providing a gas mixture containing carbon monoxide; b. heating said gas mixture to a temperature above about 500°F. by direct heat exchange with a heated material whereby the heated material is cooled in a first zone; c. introducing sulfur into the gas mixture and reacting the gas mixture with the sulfur at a temperature between about 500° and 1300°F. to form a gas mixture containing carbonyl sulfide in a second zone; d. reacting the gas mixture containing carbonyl sulfide with water, in the vapor phase, at a temperature between about 400°F. and about 1300°F. to form a reacted gas mixture containing hydrogen sulfide in a third zone; and e. cooling said reacted gas mixture by direct heat exchange with a cooled material whereby said cooled material is heated to be used as the heated material in said first zone.
Claim 3
Dependent Claim
20 words
The process of claim 1 wherein water is present when the gas mixture containing carbon monoxide is reacted with sulfur.
Claim 4
Dependent Claim
36 words
The process of claim 2 wherein the cooled material is a catalyst for the reaction of carbon monoxide with sulfur and of carbonyl sulfide with water and steps (c), (d) and (e) are carried out simultaneously.
Claim 5
Dependent Claim
29 words
The process of claim 1 wherein the cooled material is a catalyst for the reaction of carbonyl sulfide with water and steps (d) and (e) are carried out simultaneously.
Claim 6
Dependent Claim
26 words
The process of claim 1 wherein sulfur is introduced into the gas mixture containing carbon monoxide before the gas mixture is contacted with the heated material.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein the gas mixture contains hydrogen.
Claim 8
Dependent Claim
102 words
In a process for the preparation of hydrogen sulfide wherein a gas mixture containing carbon monoxide and sulfur is reacted to form carbonyl sulfide and the carbonyl sulfide is reacted with water in the vapor phase to form hydrogen sulfide, the improvement which comprises contacting a hot gas mixture containing carbon monoxide with liquid sulfur whereby the gas mixture is cooled to a temperature above about 500°F. and at least a portion of the sulfur is vaporized whereby a gas mixture containing sulfur is formed and said carbonyl sulfide is reacted with water at a temperature from about 400°F to about 1300°F.
Claim 9
Dependent Claim
102 words
In a process for the preparation of hydrogen sulfide wherein a gas mixture containing carbon monoxide and sulfur is reacted to form carbonyl sulfide and the carbonyl sulfide is reacted with water in the vapor phase to form hydrogen sulfide, the improvement which comprises contacting a hot gas mixture containing carbon monoxide with liquid sulfur whereby the gas mixture is cooled to a temperature above about 500°F. and at least a portion of the sulfur is vaporized whereby a gas mixture containing sulfur is formed and said carbonyl sulfide is reacted with water at a temperature from about 400°F to about 1300°F.
Claim 10
Dependent Claim
11 words
The method of claim 7 wherein the gas mixture contains hydrogen.
Claim 11
Dependent Claim
34 words
The method of claim 7 wherein only a portion of the sulfur is vaporized and whereby the gas mixture is scrubbed by the liquid sulfur and particulate matter is removed from the gas mixture.
Claim 12
Dependent Claim
25 words
The process of claim 7 wherein the gas mixture containing carbon monoxide and sulfur is reacted at a temperature from about 500° to about 1200°F.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-01 | 1979-12-01 | 1980-06-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-01 | 1983-12-01 | 1984-06-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-01 | 1987-12-01 | 1988-06-01 | $7700.00 | Window Closed / Lapsed |