US4039613A
Expired / Lapsed
US
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Process for production of hydrogen and sulfur from hydrogen sulfide as raw material
Assignee: National Institute of Advanced Industrial Science and Technology
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Filing: 1976-03-09
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Granted: 1977-08-02
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Expires: 1996-03-09
Abstract
Abstract Sulfur and hydrogen are produced from hydrogen sulfide according to the present invention by bringing hydrogen sulfide into contact, at a temperature exceeding the boiling point of sulfur, with at least one member selected from the group consisting of the sulfides of molybdenum, tungsten and ruthenium to give rise to a gaseous mixture consisting of hydrogen sulfide, hydrogen and sulfur, cooling the produced mixture to separate therefrom the sulfur component in the condensed form and leave behind a gaseous mixture wherein the hydrogen component makes up the majority of the total weight thereof and subsequently removing hydrogen sulfide from this mixture by means of condensation or absorption.
Inventors
- 👤 Yoshihide Kotera
- 👤 Naoyuki Todo
- 👤 Kenzo Fukuda
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 14:50
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/04; C01B17/00; C01B17/02; C01B17/04; C01B17/0495; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/36
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
70 words
In a process for the production of hydrogen and sulfur from hydrogen sulfide, the improvement which comprises: 1. bringing hydrogen sulfide into contact with tungsten sulfide at a temperature of from 450° to 800° C. thereby giving rise to a gaseous mixture consisting of hydrogen sulfide, hydrogen and sulfur, 2. cooling the said gaseous mixture thereby condensing the sulfur component of the said mixture and separating and obtaining elementary sulfur,
Claim 2
Dependent Claim
70 words
In a process for the production of hydrogen and sulfur from hydrogen sulfide, the improvement which comprises: 1. bringing hydrogen sulfide into contact with tungsten sulfide at a temperature of from 450° to 800° C. thereby giving rise to a gaseous mixture consisting of hydrogen sulfide, hydrogen and sulfur, 2. cooling the said gaseous mixture thereby condensing the sulfur component of the said mixture and separating and obtaining elementary sulfur,
Claim 3
Dependent Claim
57 words
circulating back to the step (1) above the gaseous mixture remaining after removal of sulfur, 4. subjecting the circulated gaseous mixture to the steps (2) and (3) above continuously and recurrently for thereby forming a gaseous mixture having an increased hydrogen content and, 5. separating the hydrogen component from the gaseous mixture having an increased hydrogen content.
Claim 4
Dependent Claim
57 words
circulating back to the step (1) above the gaseous mixture remaining after removal of sulfur, 4. subjecting the circulated gaseous mixture to the steps (2) and (3) above continuously and recurrently for thereby forming a gaseous mixture having an increased hydrogen content and, 5. separating the hydrogen component from the gaseous mixture having an increased hydrogen content.
Claim 5
Dependent Claim
40 words
The process of claim 1, wherein the separation of hydrogen is accomplished by cooling the circulating gas to condense hydrogen sulfide and removing the condensed hydrogen sulfide from the gas consequently to leave behind hydrogen alone in the gaseous state.
Claim 6
Dependent Claim
53 words
The process of claim 1, wherein the separation of hydrogen is accomplished by passing the circulating gas through a solution capable of absorbing hydrogen sulfide alone for thereby having the hydrogen sulfide component alone absorbed in the said absorbent solution and allowing the hydrogen component alone to be obtained in the gaseous state.
Claim 7
Dependent Claim
173 words
In a process for the continuous production of hydrogen and sulfur from hydrogen sulfide, the improvement which comprises: 1. continuously bringing hydrogen sulfide into contact with tungsten sulfide at a temperature of from 450° to 800° C. thereby giving rise to a gaseous mixture consisting of hydrogen sulfide, hydrogen and sulfur. 2. continuously cooling the said gaseous mixture thereby continuously condensing the sulfur component of the said mixture and continuously separating and obtaining elementary sulfur. 3. continuously withdrawing a part of the gaseous mixture remaining after removal of the condensed sulfur and, at the same time, circulating the remaining part of the gaseous mixture back to the step (1) above. 4. separating and obtaining hydrogen from the withdrawn part of the gaseous mixture and; 5. circulating back to the step (1) above the hydrogen sulfide resulting from the said separation of hydrogen and introducing into the said step (1) such amount of fresh hydrogen sulfide as to make up for the hydrogen sulfide lost from the circulation gas in consequence of the reaction.
Claim 8
Dependent Claim
173 words
In a process for the continuous production of hydrogen and sulfur from hydrogen sulfide, the improvement which comprises: 1. continuously bringing hydrogen sulfide into contact with tungsten sulfide at a temperature of from 450° to 800° C. thereby giving rise to a gaseous mixture consisting of hydrogen sulfide, hydrogen and sulfur. 2. continuously cooling the said gaseous mixture thereby continuously condensing the sulfur component of the said mixture and continuously separating and obtaining elementary sulfur. 3. continuously withdrawing a part of the gaseous mixture remaining after removal of the condensed sulfur and, at the same time, circulating the remaining part of the gaseous mixture back to the step (1) above. 4. separating and obtaining hydrogen from the withdrawn part of the gaseous mixture and; 5. circulating back to the step (1) above the hydrogen sulfide resulting from the said separation of hydrogen and introducing into the said step (1) such amount of fresh hydrogen sulfide as to make up for the hydrogen sulfide lost from the circulation gas in consequence of the reaction.
Claim 9
Dependent Claim
39 words
The process of claim 4, wherein the separation of hydrogen is accomplished by cooling the withdrawn gaseous mixture for thereby condensing the hydrogen sulfide component thereof and enabling the hydrogen component alone to be obtained in the gaseous state.
Claim 10
Dependent Claim
53 words
The process of claim 4, wherein the separation of hydrogen is accomplished by passing the withdrawn gaseous mixture through a solution capable of absorbing hydrogen sulfide alone thereby having the hydrogen sulfide component alone absorbed in the said absorbent solution and allowing the hydrogen component alone to be obtained in the gaseous state.
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) | 1980-08-01 | 1981-01-31 | 1981-08-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-01 | 1985-01-31 | 1985-08-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-01 | 1989-01-31 | 1989-08-02 | $7700.00 | Window Closed / Lapsed |