GB1077008A - Improvements in the production of ammonium bisulphite for use in sulphite pulp manufacture - Google Patents
Improvements in the production of ammonium bisulphite for use in sulphite pulp manufactureInfo
- Publication number
- GB1077008A GB1077008A GB2527663A GB2527663A GB1077008A GB 1077008 A GB1077008 A GB 1077008A GB 2527663 A GB2527663 A GB 2527663A GB 2527663 A GB2527663 A GB 2527663A GB 1077008 A GB1077008 A GB 1077008A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ammonia
- ammonium
- tower
- solution
- bisulphite
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/22—Sulfites of ammonium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Physical Water Treatments (AREA)
- Gas Separation By Absorption (AREA)
Abstract
Sulphur dioxide and/or ammonia from scrubbed gases obtained in the production of ammonium bisulphate by scrubbing sulphur dioxide-containing gas with an aqueous solution of ammonia are removed by contacting with an approximately equimolar solution of ammonium sulphite and ammonium bisulphite. The gas which may contain 16-18% SO2 from burning S in air, is passed at 10 into a packed tower, whence ammonium bisulphite is withdrawn at 12. Ammonia solution or ammonia plus water enters the tower at 11 and effluent gases pass at 13 to a packed recovery tower where they meet a countercurrent of solution of equimolar ammonium sulphite and ammonium bisulphite of pH 6.1, which is recycled from pump tank 17 to the recovery tower at 15. To ensure maintenance of pH 6.1 ammonia may be added at 19 or the So2 or ammonia input to first tower may be varied. Part of the solution is withdrawn at 22 to the acid tank or to the acid tower.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2527663A GB1077008A (en) | 1963-06-25 | 1963-06-25 | Improvements in the production of ammonium bisulphite for use in sulphite pulp manufacture |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2527663A GB1077008A (en) | 1963-06-25 | 1963-06-25 | Improvements in the production of ammonium bisulphite for use in sulphite pulp manufacture |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1077008A true GB1077008A (en) | 1967-07-26 |
Family
ID=10225098
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2527663A Expired GB1077008A (en) | 1963-06-25 | 1963-06-25 | Improvements in the production of ammonium bisulphite for use in sulphite pulp manufacture |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1077008A (en) |
-
1963
- 1963-06-25 GB GB2527663A patent/GB1077008A/en not_active Expired
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