US4302434A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing hydrogen and sulphur from hydrogen sulphide
Assignee: Davy McKee AG
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Filing: 1980-04-11
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Granted: 1981-11-24
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Expires: 2000-04-11
Abstract
Abstract A process is provided for the production of hydrogen and sulphur from a gas containing hydrogen sulphide. Such a process comprises passing the gas through a cracking zone at a temperature of from about 850° C. to 1600° C., cooling the cracked gas to a temperature of from about 110° C. to 150° C., and separating the condensed elemental sulphur. The uncracked hydrogen sulphide is separated and returned to the cracking zone; the remaining gas is withdrawn as hydrogen-rich gas.
Inventors
- 👤 Lars Hellmer
- 👤 Gerhard Keunecke
- 👤 Rainer Lell
- 👤 Ghazi R. Al-Muddarris
- 👤 Reinhard Pachaly
- 👤 Adolf Stauffer
- 👤 V. Rao Vangala
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 23:19
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: 15
Claim 1
Independent Claim
187 words
A process for the production of hydrogen and sulphur by thermal cracking, said process comprising: (A) conducting a hydrogen sulphide-containing feed gas through a cracking zone maintained at a temperature of from about 850° C. to 1600° C., to thereby effect cracking of the hydrogen sulphide in said feed gas; (B) cooling the cracked gas to temperatures of from about 110° to 150° C. to thereby condense elemental sulphur formed by the cracking; (C) separating said elemental sulfur condensed by said cooling from said cracked gas; (D) heating the cracked gas, after said separation of the condensed sulfur, to temperatures in the range of from 100° to 400° C.; (E) conducting the heated cracked gas over a hydrogenation catalyst; (F) washing the cracked gas with a basic and/or with a physically acting washing liquid in order to separate uncracked and reconverted hydrogen sulfide therefrom; (G) desorbing the separated hydrogen sulfide from said washing liquid and recycling the desorbed hydrogen sulfide to the cracking zone; and (H) drawing off the residual gas after separation of said elemental sulfur and said uncracked and reconverted hydrogen sulfide as hydrogen-rich gas.
Claim 2
Dependent Claim
187 words
A process for the production of hydrogen and sulphur by thermal cracking, said process comprising: (A) conducting a hydrogen sulphide-containing feed gas through a cracking zone maintained at a temperature of from about 850° C. to 1600° C., to thereby effect cracking of the hydrogen sulphide in said feed gas; (B) cooling the cracked gas to temperatures of from about 110° to 150° C. to thereby condense elemental sulphur formed by the cracking; (C) separating said elemental sulfur condensed by said cooling from said cracked gas; (D) heating the cracked gas, after said separation of the condensed sulfur, to temperatures in the range of from 100° to 400° C.; (E) conducting the heated cracked gas over a hydrogenation catalyst; (F) washing the cracked gas with a basic and/or with a physically acting washing liquid in order to separate uncracked and reconverted hydrogen sulfide therefrom; (G) desorbing the separated hydrogen sulfide from said washing liquid and recycling the desorbed hydrogen sulfide to the cracking zone; and (H) drawing off the residual gas after separation of said elemental sulfur and said uncracked and reconverted hydrogen sulfide as hydrogen-rich gas.
Claim 3
Dependent Claim
21 words
A process according to claim 1, wherein the hydrogen sulphide-containing feed gas is directly and/or indirectly heated to the cracking temperature.
Claim 4
Dependent Claim
27 words
A process according to claim 2, wherein a gas containing hydrocarbon and/or hydrogen is sub-stoichiometrically burnt for heating the hydrogen sulphide-containing feed gas to the cracking temperature.
Claim 5
Dependent Claim
18 words
A process according to claim 3, wherein a part of the hydrogen produced in the process is burnt.
Claim 6
Dependent Claim
17 words
A process according to claim 1, wherein the cracked gas is heated to 300° to 350° C.
Claim 7
Dependent Claim
55 words
A process according to claim 1, 2, or 3, wherein the cracked gas, after the separation of the major part of the condensed sulphur, is subjected to a washing with water; the sulphur which is washed out and dissolved gases are separated from the washing water; and said gases are returned into the cracking zone.
Claim 8
Dependent Claim
29 words
A process according to claim 1, 2 or 3, wherein before washing, the cracked gas is cooled to a temperature in the range of from 20° to 80° C.
Claim 9
Dependent Claim
24 words
A process according to claim 7, wherein the cracked gas is cooled to a temperature in the range of from 30° to 50° C.
Claim 10
Dependent Claim
23 words
A process according to claim 1, 2 or 3, wherein the gas drawn off from the hydrogen sulphide washing is purified by adsorption.
Claim 11
Dependent Claim
27 words
A process according to claim 1, 2, or 3, wherein a feed gas containing hydrogen sulphide and hydrocarbons is conducted together with steam through the cracking zone.
Claim 12
Dependent Claim
30 words
A process according to claim 1, 2, or 3, wherein the feed gas containing hydrogen sulphide is heated by the heat of the cracked gas before entering the cracking zone.
Claim 13
Dependent Claim
40 words
A process according to claim 1, 2, or 3, wherein the uncracked hydrogen sulphide and any carbon dioxide present are separated by liquifaction from the cracked gas and the separated hydrogen sulphide and carbon dioxide are thereafter separated by fractionation.
Claim 14
Dependent Claim
19 words
A process according to claim 12, wherein the uncracked hydrogen sulphide thus recovered is recycled to the cracking zone.
Claim 15
Dependent Claim
32 words
A process according to claim 1, wherein some of the hydrogen sulphide of the feed gas is burnt in the cracking zone, so as to maintain the cracking zone at reaction temperature.
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) | 1984-11-23 | 1985-05-25 | 1985-11-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-23 | 1989-05-25 | 1989-11-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-23 | 1993-05-25 | 1993-11-24 | $7700.00 | Window Closed / Lapsed |