GB236420A - Process of distilling carbonaceous material such as oil-shale - Google Patents
Process of distilling carbonaceous material such as oil-shaleInfo
- Publication number
- GB236420A GB236420A GB2244524A GB2244524A GB236420A GB 236420 A GB236420 A GB 236420A GB 2244524 A GB2244524 A GB 2244524A GB 2244524 A GB2244524 A GB 2244524A GB 236420 A GB236420 A GB 236420A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gases
- retort
- returned
- liquid
- separating tank
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B1/00—Retorts
- C10B1/02—Stationary retorts
- C10B1/04—Vertical retorts
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
236,420. Fairbrother, H., (Jackson Research Corporation). Sept. 23, 1924. Coking processes.-In the destructive distillation of oil shale the material is heated to a temperature of from 500 to 600‹ C. in a vertical retort 1 having a perforated bottom 5 forming a gas-collecting chamber 6 from which liquid and vapour are withdrawn to a separating tank 8 in which the liquid is retained. The gases and vapours pass to a condenser 10 and second separating tank 12, the remaining gases which may be preheated being returned by a fan 14 and pipe 17 to the top of the retort. Additional inert gases may be supplied to the gases returned to the retort, and the gases, dry and of low vapour tension, assist in the recovery of a large proportion of volatile oils and in prevention of cracking taking place in the retort.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2244524A GB236420A (en) | 1924-09-23 | 1924-09-23 | Process of distilling carbonaceous material such as oil-shale |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2244524A GB236420A (en) | 1924-09-23 | 1924-09-23 | Process of distilling carbonaceous material such as oil-shale |
Publications (1)
Publication Number | Publication Date |
---|---|
GB236420A true GB236420A (en) | 1925-07-09 |
Family
ID=10179464
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2244524A Expired GB236420A (en) | 1924-09-23 | 1924-09-23 | Process of distilling carbonaceous material such as oil-shale |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB236420A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0054506A2 (en) * | 1980-12-12 | 1982-06-23 | Sidérurgie Maritime (Maritieme Staalnijverheid) SIDMAR S.A. | Method and apparatus for the continuous manufacture of metallurgical coke |
-
1924
- 1924-09-23 GB GB2244524A patent/GB236420A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0054506A2 (en) * | 1980-12-12 | 1982-06-23 | Sidérurgie Maritime (Maritieme Staalnijverheid) SIDMAR S.A. | Method and apparatus for the continuous manufacture of metallurgical coke |
EP0054506A3 (en) * | 1980-12-12 | 1983-01-26 | Sidérurgie Maritime (Maritieme Staalnijverheid) SIDMAR S.A. | Method and apparatus for the continuous manufacture of metallurgical coke |
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