US4123355A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Simultaneous treatment of SO2 containing stack gases and waste water
Assignee: National Aeronautics and Space Administration
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Filing: 1977-11-21
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Granted: 1978-10-31
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Expires: 1997-11-21
Abstract
Abstract A process for simultaneously removing sulfur dioxide from stack gases and the like and purifying waste water such as derived from domestic sewage in which a portion of the gas stream and a portion of the waste water, the latter containing dissolved iron and having an acidic pH, are contacted in a closed loop gas-liquid scrubbing zone to effect absorption of the sulfur dioxide into the waste water. A second portion of the gas stream and a second portion of the waste water are controlled in an open loop gas-liquid scrubbing zone, the second portion of the waste water containing a lesser amount of iron than the first portion of the waste water, contacting in the open loop scrubbing zone being sufficient to acidify the waste water which is then treated to remove solids originally present.
Inventors
- 👤 with respect to an invention of Frosch Robert A. Administrator of the National Aeronautics and Space Administration
- 👤 Jerry C. Poradek
- 👤 Dwight D. Collins
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 13:12
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501; C; C02; C02F; C02F1/00; C02F1/58; C02F1/62; C02F1/64; C02F1/645; C02F2103/00; C02F2103/18
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
277 words
A process for the simultaneous treatment of a sulfur dioxide containing gas stream and waste water of the type derived from domestic sewage comprising: introducing a first portion of said gas stream and a first portion of said waste water into a first gas-liquid scrubbing zone, said first portion of said waste water containing from about 500 to about 1200 parts per million iron and having a pH of from about 1.5 to about 3, the temperature in said first scrubbing zone being from about 120° to about 160° F., contacting said first portion of said gas stream and said first portion of said waste water in said first scrubbing zone to absorb SO 2 into said waste water, the contact time in said scrubbing zone being sufficient to permit substantial oxidation of absorbed SO 2 , said waste water being recycled through said first scrubbing zone, introducing a second portion of said gas stream, a portion of said recirculating waste water from said first scrubbing zone, and a second portion of said waste water into a second gas-liquid scrubbing zone, said second portion of said waste water in said second scrubbing zone containing from about 50 to about 200 parts per million iron, contacting said second portion of said gas stream with said second portion of said waste water in said second scrubbing zone to absorb SO 2 into said second portion of said waste water and acidify said second portion of said waste water, removing said acidified waste water from said second scrubbing zone, and treating said acidified waste water removed from said second scrubbing zone to remove solids originally present in said waste water.
Claim 2
Dependent Claim
277 words
A process for the simultaneous treatment of a sulfur dioxide containing gas stream and waste water of the type derived from domestic sewage comprising: introducing a first portion of said gas stream and a first portion of said waste water into a first gas-liquid scrubbing zone, said first portion of said waste water containing from about 500 to about 1200 parts per million iron and having a pH of from about 1.5 to about 3, the temperature in said first scrubbing zone being from about 120° to about 160° F., contacting said first portion of said gas stream and said first portion of said waste water in said first scrubbing zone to absorb SO 2 into said waste water, the contact time in said scrubbing zone being sufficient to permit substantial oxidation of absorbed SO 2 , said waste water being recycled through said first scrubbing zone, introducing a second portion of said gas stream, a portion of said recirculating waste water from said first scrubbing zone, and a second portion of said waste water into a second gas-liquid scrubbing zone, said second portion of said waste water in said second scrubbing zone containing from about 50 to about 200 parts per million iron, contacting said second portion of said gas stream with said second portion of said waste water in said second scrubbing zone to absorb SO 2 into said second portion of said waste water and acidify said second portion of said waste water, removing said acidified waste water from said second scrubbing zone, and treating said acidified waste water removed from said second scrubbing zone to remove solids originally present in said waste water.
Claim 3
Dependent Claim
25 words
The process of claim 1 including adding an alkaline material to the gas contacted waste water from said first scrubbing zone to adjust the pH.
Claim 4
Dependent Claim
45 words
The process of claim 2 wherein the portion of the treated, gas contacted waste water being recycled through said first scrubbing zone introduced into said second scrubbing zone is such as to maintain the desired iron content of said second portion of said waste water.
Claim 5
Dependent Claim
12 words
The process of claim 2 wherein said alkaline material comprises calcium oxide.
Claim 6
Dependent Claim
15 words
The process of claim 4 wherein said calcium oxide is in the form of lime.
Claim 7
Dependent Claim
17 words
The process of claim 4 including removing precipitated calcium sulfate from said treated, gas contacted waste water.
Claim 8
Dependent Claim
43 words
The process of claim 1 wherein said first portion of said gas stream and said first portion of said waste water are contacted by passing said first portion of said gas stream in counterflow relation to said first portion of said waste water.
Claim 9
Dependent Claim
19 words
The process of claim 1 wherein the pH of said first portion of said waste water is about 2.0.
Claim 10
Dependent Claim
19 words
The process of claim 1 wherein said contact time in said first scrubbing zone is greater than 25 seconds.
Claim 11
Dependent Claim
19 words
The process of claim 1 wherein said contacting in said first scrubbing zone is conducted in a packed column.
Claim 12
Dependent Claim
21 words
The process of claim 1 including aerating said acidified, waste water from said second scrubbing zone prior to removing said solids.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-10-30 | 1982-05-01 | 1982-10-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-30 | 1986-05-01 | 1986-10-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-30 | 1990-05-01 | 1990-10-31 | $7700.00 | Window Closed / Lapsed |