US4569832A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for desulfurizing coke oven gases
Assignee: Carl Still GmbH and Co KG
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Filing: 1984-10-23
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Granted: 1986-02-11
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Expires: 2004-10-23
Abstract
Abstract A method of desulfurizing coke oven gas comprises directing the coke oven gases upwardly and in a hydrogen sulfide scrubber tower, washing the coke oven gases in a cyclic ammonia washing including admixing sulfur compounds containing waste gases and without cooling with ammonia in a degasifying unit which is supplied with ammonia containing water which is advantageously obtained from a tar separator and using the heat content of the waste gases to expel the ammonia from the water, and directing the waste gases laden with the expelled ammonia into the tower. The waste gases advantageously come from a Claus plant process and they are laden with ammonia and they are advantageously directed into the upper portion of the scrubber tower. Ammonia water is circulated in an ammonia circuit from an outlet which is advantageously located in the upper portion of the tower to an inlet which connects to the tower above the outlet. The apparatus includes in addition to the tower in the ammonia water circuit connected into the tower a degasifying unit which is supplied with Claus plant waste gases and into which an ammonia liquor from a tar separator is advantageously circulated. The heat of the waste gases causes a liberation of the ammonia to the waste gases which are then directed to the tower above or substantially at the level at the outlet of the ammonia water circuit.
Inventors
- 👤 Dieter Laufhutte
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 01:19
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/08; C10K1/10; C10K1/12; C10K1/121; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
217 words
Method of desulfurizing coke oven gases, comprising directing the coke oven gases upwardly in a hydrogen sulfide scrubber tower having a lower portion, a middle portion and an upper portion, while washing the coke oven gases in a cyclic ammonia washing, wherein an ammonia cooling circuit is connected to the upper portion of the tower for circulating ammonia water into the tower, including a circuit outlet connected to the upper portion of the tower and a circuit inlet connected from the circuit outlet back to the upper portion of the tower at a level above the circuit outlet, independently separately admixing sulphur compounds containing hot waste gases from a Claus process used to produce sulfuric acid or elemental sulfur, and which hot waste gases have not been cooled, with ammonia in a degasifying unit which is supplied with ammonia containing water, using the heat content of the hot waste gases to expel the ammonia from the water, and directing the waste gases laden with the expelled ammonia from the degasifying unit into the upper portion of the tower at a level above the circuit inlet and into association with the coke oven gases for increasing the ammonia concentration in the tower and correspondingly increasing the degree of desulfurization of the coke oven gases in a controlled manner.
Claim 2
Dependent Claim
217 words
Method of desulfurizing coke oven gases, comprising directing the coke oven gases upwardly in a hydrogen sulfide scrubber tower having a lower portion, a middle portion and an upper portion, while washing the coke oven gases in a cyclic ammonia washing, wherein an ammonia cooling circuit is connected to the upper portion of the tower for circulating ammonia water into the tower, including a circuit outlet connected to the upper portion of the tower and a circuit inlet connected from the circuit outlet back to the upper portion of the tower at a level above the circuit outlet, independently separately admixing sulphur compounds containing hot waste gases from a Claus process used to produce sulfuric acid or elemental sulfur, and which hot waste gases have not been cooled, with ammonia in a degasifying unit which is supplied with ammonia containing water, using the heat content of the hot waste gases to expel the ammonia from the water, and directing the waste gases laden with the expelled ammonia from the degasifying unit into the upper portion of the tower at a level above the circuit inlet and into association with the coke oven gases for increasing the ammonia concentration in the tower and correspondingly increasing the degree of desulfurization of the coke oven gases in a controlled manner.
Claim 3
Dependent Claim
18 words
Method of claim 1 wherein the waste gases are heated prior to introduction thereof into the degasifying unit.
Claim 4
Dependent Claim
20 words
Method of claim 1 wherein the ammonia containing water is homogeneously mixed with the waste gases in the degasifying unit.
Claim 5
Dependent Claim
180 words
Device for desulfurizing coke oven gases, comprising a hydrogen sulfide scrubber tower having a lower portion, a middle portion and an upper portion, an ammonia water cooling circuit connected into the tower for circulating ammonia containing water into the upper portion of the tower, including a circuit outlet connected to the upper portion of the tower and a circuit inlet connected from the circuit outlet back to the upper portion of the tower at a level above the circuit outlet, a degasifying unit alongside the tower and having a unit inlet for sulfur compounds containing hot waste gases from a Claus process which are circulated through the degasifying unit and a unit outlet for the hot waste gases laden with ammonia which is connected to the upper portion of the tower at a level above the ammonia water cooling circuit inlet, and means for circulating an ammoniated liquor to the degasifying unit to permit the hot waste gases to expel the ammonia therefrom for passage therewith in gaseous form from the unit outlet to the upper portion of the tower.
Claim 6
Dependent Claim
180 words
Device for desulfurizing coke oven gases, comprising a hydrogen sulfide scrubber tower having a lower portion, a middle portion and an upper portion, an ammonia water cooling circuit connected into the tower for circulating ammonia containing water into the upper portion of the tower, including a circuit outlet connected to the upper portion of the tower and a circuit inlet connected from the circuit outlet back to the upper portion of the tower at a level above the circuit outlet, a degasifying unit alongside the tower and having a unit inlet for sulfur compounds containing hot waste gases from a Claus process which are circulated through the degasifying unit and a unit outlet for the hot waste gases laden with ammonia which is connected to the upper portion of the tower at a level above the ammonia water cooling circuit inlet, and means for circulating an ammoniated liquor to the degasifying unit to permit the hot waste gases to expel the ammonia therefrom for passage therewith in gaseous form from the unit outlet to the upper portion of the tower.
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) | 1989-02-10 | 1989-08-12 | 1990-02-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-02-10 | 1993-08-12 | 1994-02-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-02-10 | 1997-08-12 | 1998-02-11 | $7700.00 | Window Closed / Lapsed |