US4002565A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Waste-water process
Assignee: Chevron USA Inc
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Filing: 1975-08-25
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Granted: 1977-01-11
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Expires: 1995-08-25
Abstract
Abstract Waste water containing dissolved acid-gas and ammonia impurities is processed for the separate recovery of the acid gas, ammonia and recycle water. In a further aspect, a purified pyrolysis gas is produced by treating a raw pyrolysis gas product stream utilizing the aforementioned recycle water and a pair of coupled acid-gas-absorber and acid-gas-stripper columns.
Inventors
- 👤 Thomas R. Farrell
- 👤 Robert J. Klett
- 👤 James A. Craig
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 08:26
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1418; B01D53/1425; B01D53/1456; C; C01; C01C; C01C1/00; C01C1/02; C01C1/10; C02; C02F; C02F1/00; C02F1/58; C02F1/586; C10; C10K; C10K1/00; C10K1/08
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
275 words
A process for separating acid gas and ammonia from waste water having an appreciable content thereof and for the production of recycle water, comprising the steps: 1. producing a first recycle water stream and an effluent gas stream comprising acid gas, ammonia and water vapor by passing said waste water into an acid gas-ammonia stripping column, said column being maintained at a bottoms temperature in the range from about 93° to 149° C and at a pressure in the range from about 1 to 5 atmospheres absolute, said first stream having an acid gas and ammonia content which is less than 15 percent of the content thereof for said waste water; 2. separately withdrawing said first recycle water stream and said effluent gas stream from said acid-gas ammonia stripping column; 3. Producing a liquid aqueous concentrate of ammonia and acid gas by decreasing the temperature of said effluent gas stream, said temperature decrease being an amount in the range from about 55° to 110° C. 4. producing an effluent acid-gas stream and an aqueous bottoms stream by passing said concentrate into a primary acid-gas stripping column, said column being maintained at superatmospheric pressure acid-gas stripping conditions; 5. separately withdrawing said acid-gas stream and said bottoms stream from said acid-gas stripping column; and 6. producing an effluent gas stream comprising ammonia and a second recycle water stream by passing said bottoms stream into an ammonia stripping column, said column being maintained at superatmospheric pressure ammonia stripping conditions, said second stream having an acid gas and ammonia content which is less than 15 percent of the content thereof for said bottoms stream from said acid-gas stripping column.
Claim 2
Dependent Claim
275 words
A process for separating acid gas and ammonia from waste water having an appreciable content thereof and for the production of recycle water, comprising the steps: 1. producing a first recycle water stream and an effluent gas stream comprising acid gas, ammonia and water vapor by passing said waste water into an acid gas-ammonia stripping column, said column being maintained at a bottoms temperature in the range from about 93° to 149° C and at a pressure in the range from about 1 to 5 atmospheres absolute, said first stream having an acid gas and ammonia content which is less than 15 percent of the content thereof for said waste water; 2. separately withdrawing said first recycle water stream and said effluent gas stream from said acid-gas ammonia stripping column; 3. Producing a liquid aqueous concentrate of ammonia and acid gas by decreasing the temperature of said effluent gas stream, said temperature decrease being an amount in the range from about 55° to 110° C. 4. producing an effluent acid-gas stream and an aqueous bottoms stream by passing said concentrate into a primary acid-gas stripping column, said column being maintained at superatmospheric pressure acid-gas stripping conditions; 5. separately withdrawing said acid-gas stream and said bottoms stream from said acid-gas stripping column; and 6. producing an effluent gas stream comprising ammonia and a second recycle water stream by passing said bottoms stream into an ammonia stripping column, said column being maintained at superatmospheric pressure ammonia stripping conditions, said second stream having an acid gas and ammonia content which is less than 15 percent of the content thereof for said bottoms stream from said acid-gas stripping column.
Claim 3
Dependent Claim
36 words
A process as in claim 1 characterized in that said waste water and a scrubbed pyrolysis gas are generated by scrubbing a raw pyrolysis gas with at least a portion of said first recycle water stream.
Claim 4
Dependent Claim
30 words
A process as in claim 2 characterized in that a portion of said bottoms from the primary acid-gas-stripping column is added to said first recycle stream prior to said scrubbing.
Claim 5
Dependent Claim
17 words
A process as in claim 2 characterized in that said pyrolysis gas is obtained by pyrolyzing coal.
Claim 6
Dependent Claim
107 words
A process as in claim 4 characterized in that (1) said scrubbed pyrolysis gas is obtained by passing crude pyrolysis gas to a gas scrubber column, scrubbing said crude gas with said recycle water, said scrubber column being operated at an acid gas-to-ammonia mol ratio in the range 0.2 to 2, withdrawing the resulting scrubbed gas at a temperature of about 49° C and at a pressure of at least 4.4 atmospheres absolute, and (2) said acid gas-ammonia stripping column is maintained at a temperature in the range 115° C to 132° C and at a pressure in the range from about 1.68 to 2.7 atmospheres absolute.
Claim 7
Dependent Claim
33 words
A process as in claim 5 characterized in that said acid gas-to-ammonia mol ratio is in the range 0.65 to 1.5 and said resulting scrubbed gas pressure is at least 5.8 atmospheres absolute.
Claim 8
Dependent Claim
21 words
A process as in claim 2 characterized in that said acid gas comprises a mixture of hydrogen sulfide and carbon dioxide.
Claim 9
Dependent Claim
39 words
A process as in claim 2 characterized in that said acid-gas and ammonia contents for said first and second recycle stream is less than 2 percent of said waste water and bottoms stream from said acid-gas stripping column, respectively.
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) | 1980-01-11 | 1980-07-12 | 1981-01-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-11 | 1984-07-12 | 1985-01-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-11 | 1988-07-12 | 1989-01-11 | $7700.00 | Window Closed / Lapsed |