US4511549A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the elimination of waste water produced upon the desulfurization of coking oven gas by means of wash solution containing organic oxygen-carrier, with simultaneous recovery of elemental sulfur
Assignee: Krupp Koppers GmbH
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Filing: 1982-07-09
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Granted: 1985-04-16
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Expires: 2002-07-09
Abstract
Abstract A process is disclosed for the elimination of waste water falling out with the desulfurization of coking oven gas by means of an organic oxygen carrier--containing washing solution with simultaneous recovery of elemental sulfur. The waste water is decomposed in a combustion chamber in a reducing atmosphere at temperatures between about 1000° and 1100° C. under such conditions that the mole ratio of H 2 S:SO 2 in the exhaust gas of the combustion chamber amounts to at least 2:1. Sulfur falling out is separated and the sensible heat of the exhaust gas is utilized for steam generation. The cooled and desulfurized exhaust gas is added to the coking oven gas before the pre-cooling. Sulfur falling out from the washing solution in the oxidizer is separated out and lead into the combustion chamber together with the part of the washing solution discharged as waste water from the washing solution circulation. Preferred embodiments include that the sulfur loading of the waste water can amount to up to about 370 kg sulfur per m 3 waste water; having the cooling of sulfur--containing exhaust gas leaving the combustion chamber follow in a waste heat boiler and a sulfur condenser heated by pre-heated boiler feed water, from which condenser sulfur is discharged in liquid state.
Inventors
- 👤 Peter Diemer
- 👤 Werner Brake
- 👤 Rainer Dittmer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 20:21
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05; C02; C02F; C02F11/00; C02F11/10; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129; Y02W; Y02W10/00; Y02W10/40; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/908; Y10S210/909
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
192 words
In a process for the elimination of H 2 S-containing waste water produced upon the desulfurization of coking oven gas by means of a washing solution containing organic oxygen carrier with simultaneous recovery of elemental sulfur, of the type in which the waste water is decomposed in a combustion chamber in a reducing atmosphere at temperatures between about 1000° and 1100° C. and in the H 2 S-- and SO 2 --containing exhaust gas in the combustion chamber the mole ratio of H 2 S:SO 2 amounts to at least 2:1, the sulfur produced therewith is separated, the sensible heat of the exhaust gas is utilized for steam generation and finally the cooled and desulfurized exhaust gas is added to the coking oven gas before a pre-cooling thereof, the improvement comprising separating out sulfur from the washing solution in an oxidizer of a desulfurization plant and leading the separated sulfur into the combustion chamber together with the part of the washing solution which is discharged as waste water from the washing solution circulation, sulfur loading of the waste water amounting to up to about 370 kg sulfur per m 3 waste water.
Claim 2
Dependent Claim
192 words
In a process for the elimination of H 2 S-containing waste water produced upon the desulfurization of coking oven gas by means of a washing solution containing organic oxygen carrier with simultaneous recovery of elemental sulfur, of the type in which the waste water is decomposed in a combustion chamber in a reducing atmosphere at temperatures between about 1000° and 1100° C. and in the H 2 S-- and SO 2 --containing exhaust gas in the combustion chamber the mole ratio of H 2 S:SO 2 amounts to at least 2:1, the sulfur produced therewith is separated, the sensible heat of the exhaust gas is utilized for steam generation and finally the cooled and desulfurized exhaust gas is added to the coking oven gas before a pre-cooling thereof, the improvement comprising separating out sulfur from the washing solution in an oxidizer of a desulfurization plant and leading the separated sulfur into the combustion chamber together with the part of the washing solution which is discharged as waste water from the washing solution circulation, sulfur loading of the waste water amounting to up to about 370 kg sulfur per m 3 waste water.
Claim 3
Dependent Claim
21 words
Process according to claim 1, wherein the sulfur-containing exhaust gas leaving the combustion chamber is cooled in a waste heat boiler.
Claim 4
Dependent Claim
44 words
Process according to claim 2, wherein further cooling of said sulfur-containing exhaust gas is performed after said waste heat boiler in a sulfur condenser, said sulfur condenser being heated by pre-heated boiler feed water, from which sulfur condenser sulfur in liquid state is discharged.
Claim 5
Dependent Claim
20 words
Process according to claim 1, wherein the reaction in the combustion chamber ensues at a temperature of about 1050° C.
Claim 6
Dependent Claim
23 words
Process according to claim 1, wherein the reducing atmosphere in the combustion chamber is obtained by burning coking oven gas under air exclusion.
Claim 7
Dependent Claim
35 words
Process according to claim 1, wherein the reducing atmosphere in the combustion chamber is obtained by burning coking oven gas as well as ammonia vapors resulting from the coking oven gas treatment, under air exclusion.
Claim 8
Dependent Claim
18 words
Process according to claim 1, wherein exhaust air resulting in the oxidizer is lead into the combustion chamber.
Claim 9
Dependent Claim
21 words
Process according to claim 7, further comprising leading into said combustion chamber exhaust air resulting from the coking oven gas treatment.
Claim 10
Dependent Claim
50 words
Process according to claim 1, further comprising filtering sulfur-containing washing solution leaving the oxidizer, as much washing solution still adhering to the sulfur present as filter cake as must be discharged as waste water from the washing solution circulation, whereupon the moist filter cake is lead into the combustion chamber.
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) | 1988-04-15 | 1988-10-15 | 1989-04-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-04-15 | 1992-10-15 | 1993-04-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-04-15 | 1996-10-15 | 1997-04-16 | $7700.00 | Window Closed / Lapsed |