GB597895A - Processing acid sludge resulting from the acid refining of petroleum products - Google Patents
Processing acid sludge resulting from the acid refining of petroleum productsInfo
- Publication number
- GB597895A GB597895A GB6422/45A GB642245A GB597895A GB 597895 A GB597895 A GB 597895A GB 6422/45 A GB6422/45 A GB 6422/45A GB 642245 A GB642245 A GB 642245A GB 597895 A GB597895 A GB 597895A
- Authority
- GB
- United Kingdom
- Prior art keywords
- steam
- atmosphere
- acid
- distillation
- sludge resulting
- 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
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/312—Preparation
- C01B32/318—Preparation characterised by the starting materials
- C01B32/33—Preparation characterised by the starting materials from distillation residues of coal or petroleum; from petroleum acid sludge
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
- Treatment Of Sludge (AREA)
Abstract
Acid sludge resulting from the treatment of a petroleum distillate with sulphuric acid is converted into an active carbon by distillation at 400-750 DEG F. whereby a black oily carbonaceous residue is obtained, which is thereafter heated at 1,000-1,500 DEG F. in an atmosphere of steam for further carbonization, and for activation. The distillation may be effected in a rotary kiln, a stationary kiln with internal rotating paddles, or a multiple hearth furnace, out of contact with air or combustion gases, for 1/2 to 3 hours, sulphur dioxide being evolved. The second stage may be carried out in a multiple hearth furnace. The carbonised product, which may be ground, is then heated to between 1600 DEG and 1800 DEG F. for 1/2 to 1 hour in an atmosphere of steam, while being agitated, to complete activation. In both heating stages, steam is preferably supplied superheated at a pressure below 5 pounds/sq. in. gauge, and in amounts between 1 and 5 pounds per pound of carbonised material per hour. The activated product is then cooled in an atmosphere of steam to below 500 DEG F.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US597895XA | 1944-02-14 | 1944-02-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB597895A true GB597895A (en) | 1948-02-05 |
Family
ID=22025227
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB6422/45A Expired GB597895A (en) | 1944-02-14 | 1945-03-14 | Processing acid sludge resulting from the acid refining of petroleum products |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB597895A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2635709A (en) * | 1949-08-22 | 1953-04-21 | Standard Oil Dev Co | Adsorption of olefins by petroleum coke |
-
1945
- 1945-03-14 GB GB6422/45A patent/GB597895A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2635709A (en) * | 1949-08-22 | 1953-04-21 | Standard Oil Dev Co | Adsorption of olefins by petroleum coke |
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