GB531288A - Process for the generation of synthesis gas with the simultaneous recovery of aromatic hydrocarbons - Google Patents
Process for the generation of synthesis gas with the simultaneous recovery of aromatic hydrocarbonsInfo
- Publication number
- GB531288A GB531288A GB20704/39A GB2070439A GB531288A GB 531288 A GB531288 A GB 531288A GB 20704/39 A GB20704/39 A GB 20704/39A GB 2070439 A GB2070439 A GB 2070439A GB 531288 A GB531288 A GB 531288A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- outlet
- distillates
- generation
- aromatic hydrocarbons
- 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
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
531,288. Gas manufacture. DIDIER-WERKE AKT.-GES. July 17, 1939, No. 20704. Convention date, Aug. 27, 1938. [Class 55 (i)] In a process for the generation of synthesis gas for the production of motor fuel and other synthetic products, solid fuels for example lignite, brown coal, or peat are carbonized in continuously operated retorts, being charged into a preheating chamber 8, the distillates from an upper zone a flowing downwards to a roof-shaped offtake 11 from the underside of which they pass to an outlet 13. The temperature of the lower part of zone a is 500‹C. to 600‹C., and that of the highest temperature zone b is from 800‹C. to 1000‹C., an offtake 14 from this zone leading to an outlet 16 into which water gas from the lowest zone c also passes. The low temperature distillates from outlet 13, after removal of light oils and benzol, are mixed with the carbon-monoxide and hydrogen from outlet 16. These mixed gases are converted into liquid fuels to which anti-knock properties are given by admixture with a portion of the aromatic hydrocarbons recovered from the low temperature distillates.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE531288X | 1938-08-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB531288A true GB531288A (en) | 1941-01-01 |
Family
ID=6554889
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB20704/39A Expired GB531288A (en) | 1938-08-27 | 1939-07-17 | Process for the generation of synthesis gas with the simultaneous recovery of aromatic hydrocarbons |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB531288A (en) |
-
1939
- 1939-07-17 GB GB20704/39A patent/GB531288A/en not_active Expired
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