GB365945A - Improvements in the recovery of sulphuric acid from the acid sludge of oil refineries - Google Patents
Improvements in the recovery of sulphuric acid from the acid sludge of oil refineriesInfo
- Publication number
- GB365945A GB365945A GB15746/31A GB1574631A GB365945A GB 365945 A GB365945 A GB 365945A GB 15746/31 A GB15746/31 A GB 15746/31A GB 1574631 A GB1574631 A GB 1574631A GB 365945 A GB365945 A GB 365945A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sulphuric acid
- ammonium sulphate
- acid
- sludge
- ammonia
- 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
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
- C01B17/90—Separation; Purification
- C01B17/92—Recovery from acid tar or the like, e.g. alkylation acids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Fertilizers (AREA)
Abstract
Ammonium sulphate; calcium phosphates.--Sulphuric acid is recovered from acid sludge obtained in the refining of petroleum &c. by treating the sludge with an aqueous sulphuric acid solution of ammonium sulphate in such an amount that the ammonia content of the resultant mixture is at least 0,8 mols. per mol. of sulphuric acid whereby the carbonaceous and resinous materials in the sludge are caused to coagulate and are separated. Preferably 0,8-1,2 mols. of ammonia per mol. of sulphuric acid is used, the operating temperature being such that all the ammonium sulphate or <PICT:0365945/III/1> bisulphate formed remains in solution. The resulting sulphuric acid ammonium sulphate liquor may be used to treat rock phosphate preferably after its acid content has been increased by the addition of strong sulphuric acid. The resulting superphosphate may be neutralized by the addition of liquid ammonia to obtain a fertilizer. Anhydrous liquid ammonia is sprayed from a nozzle 2 and sulphuric acid or sulphuric acid ammonium sulphate liquor obtained in the process is sprayed from a lower nozzle 6 into a packed tower 1. The resulting aqueous sulphuric acid solution of ammonium sulphate passes continuously to a mixing vessel 8 to which acid sludge is also supplied continuously by way of conduit 9. The vessel 8 is provided with cooling coils 11. The liquid overflows from the mixing vessel through a conduit 10 into a settling tank 5 where resinous and carbonaceous material is removed by skimming. A portion of the residual solution is returned by a pump 7 and conduits 4 to the spray 6 of the tower 1. The sulphuric acid ammonium sulphate liquor not thus recirculated is withdrawn through a conduit 13. If the packing in the tower 1 becomes clogged it may be flushed with water from a conduit 14.ALSO:Sulphuric acid is recovered from acid sludge obtained in the refining of petroleum &c. by treating the sludge with an aqueous sulphuric acid solution of ammonium sulphate in such an amount that the ammonia content of the resultant mixture is at least 0,8 mol. per mol. of sulphuric acid whereby the carbonaceous and resinous materials in the sludge are caused to coagulate and are separated. Preferably 0,8-1,2 mols. of ammonia per mol. of sulphuric acid is used, the operating temperature being such that all the ammonium sulphate or bisulphate formed remains in solution. The resulting sulphuric acid ammonium sulphate liquor may be used to treat rock phosphate preferably after its acid content has been increased by the addition of strong sulphuric acid. The resulting superphosphate may be neutralized by the addition of liquid ammonia to obtain a fertilizer.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US365945XA | 1930-05-31 | 1930-05-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB365945A true GB365945A (en) | 1932-01-28 |
Family
ID=21889478
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB15746/31A Expired GB365945A (en) | 1930-05-31 | 1931-05-29 | Improvements in the recovery of sulphuric acid from the acid sludge of oil refineries |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB365945A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE749076C (en) * | 1940-10-15 | 1945-01-15 | Process for the production of water- and oil-soluble mineral oil products | |
US2418203A (en) * | 1946-11-14 | 1947-04-01 | Stauffer Chemical Co | Manufacture of superphosphate fertilizers |
US2468329A (en) * | 1944-08-21 | 1949-04-26 | Union Oil Co | Method for treatment of soils for agricultural purposes |
US2659659A (en) * | 1950-12-07 | 1953-11-17 | Standard Oil Dev Co | Ammonium sulfate production |
US2754190A (en) * | 1954-02-18 | 1956-07-10 | Exxon Research Engineering Co | Process for making phosphate fertilizer admixed with a sulfonated oil |
US2898207A (en) * | 1954-03-02 | 1959-08-04 | Minerals & Chemicals Corp Of A | Acidulation of phosphate |
-
1931
- 1931-05-29 GB GB15746/31A patent/GB365945A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE749076C (en) * | 1940-10-15 | 1945-01-15 | Process for the production of water- and oil-soluble mineral oil products | |
US2468329A (en) * | 1944-08-21 | 1949-04-26 | Union Oil Co | Method for treatment of soils for agricultural purposes |
US2418203A (en) * | 1946-11-14 | 1947-04-01 | Stauffer Chemical Co | Manufacture of superphosphate fertilizers |
US2659659A (en) * | 1950-12-07 | 1953-11-17 | Standard Oil Dev Co | Ammonium sulfate production |
US2754190A (en) * | 1954-02-18 | 1956-07-10 | Exxon Research Engineering Co | Process for making phosphate fertilizer admixed with a sulfonated oil |
US2898207A (en) * | 1954-03-02 | 1959-08-04 | Minerals & Chemicals Corp Of A | Acidulation of phosphate |
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