GB191029935A - Improved Process for the Recovery of Bye-products formed during the Dry-distillation or Gasification of Coal. - Google Patents
Improved Process for the Recovery of Bye-products formed during the Dry-distillation or Gasification of Coal.Info
- Publication number
- GB191029935A GB191029935A GB191029935DA GB191029935A GB 191029935 A GB191029935 A GB 191029935A GB 191029935D A GB191029935D A GB 191029935DA GB 191029935 A GB191029935 A GB 191029935A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gases
- saturator
- tar
- distillation
- sulphate
- 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
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/001—Purifying combustible gases containing carbon monoxide working-up the condensates
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Industrial Gases (AREA)
Abstract
29,935. Coke Oven Construction Co., and Marr, J. Dec. 23. Drawings to Specification. Ammonia; ammonium sulphate.-In order to avoid the production of effluent liquors during the treatment of distillation gases, the liquor obtained by cooling the gases to effect a complete separation of the tar, is evaporated to dryness after the separation of the tar and the vapours are passed to an ammonium-sulphate saturator. In carrying out the process, the gases are cooled to 15-35‹ C. to separate the whole of the tar and practically all the water, and, after the separation of the benzole if desired and without reheating, the resulting gases are passed into an ammonium-sulphate saturator. The vapours produced by the evaporation of the ammoniacal liquor, as referred to above, are treated in a separate saturator, care being taken that their temperature is maintained so high that condensation of water is avoided. Or these gases may be mixed with a part or the whole of the main gases, and treated in the same saturator.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB191029935T | 1910-12-23 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB191029935A true GB191029935A (en) | 1911-09-28 |
Family
ID=32495793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB191029935D Expired GB191029935A (en) | 1910-12-23 | 1910-12-23 | Improved Process for the Recovery of Bye-products formed during the Dry-distillation or Gasification of Coal. |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB191029935A (en) |
-
1910
- 1910-12-23 GB GB191029935D patent/GB191029935A/en not_active Expired
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