GB301775A - Improvements in the production of gases rich in olefines from bituminous coals - Google Patents
Improvements in the production of gases rich in olefines from bituminous coalsInfo
- Publication number
- GB301775A GB301775A GB2301727A GB2301727A GB301775A GB 301775 A GB301775 A GB 301775A GB 2301727 A GB2301727 A GB 2301727A GB 2301727 A GB2301727 A GB 2301727A GB 301775 A GB301775 A GB 301775A
- Authority
- GB
- United Kingdom
- Prior art keywords
- coal
- gases
- tube
- olefines
- heated
- 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
- C10B51/00—Destructive distillation of solid carbonaceous materials by combined direct and indirect heating
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
301,775. Johnson, J. Y., (I. G. Farbenindustrie Akt.-Ges.). Sept. 1, 1927. Coking processes.-A gas rich in olefines is produced from bituminous coals, such as brown coal, by heatingthe pulverized or granulated coal rapidly to about 800‹ C. and then rapidly cooling the gas and coke. This may be done by passing the coal quickly through the reaction chamber with the assistance of gases such as superheated steam and cooling the products in an adjacent chamber. By passing a solid inert substance such as sand or metal fragments through the reaction chamber either with the coal, or separately therefrom the deposition of coal and coke may be prevented. Wet coal should be dried before use so as to avoid the water gas reaction. The tar obtained may be returned to the process either by injection into the reaction vessel or by impregnating pumice with the tar and feeding the pumice with the coal. Suitable apparatus comprises a vertical pipe 5 metres long and 50 m.m. in diameter constructed of nickel-chromiumiron alloy and heated externally by hot gases, or electrically to about 800‹ C., the powdered charge falling through this tube. The gases obtained include 19 per cent Cn H2n and homologues of ethylene which may be absorbed in active charcoal which, on subsequent treatment with steam, gives a colourless liquid containing amylene, benzine and the like and boils between 30‹ and 100‹ C. Hot sand introduced through a hopper A is further heated in a tube B by a furnace C and together with powdered brown coal from a hopper E is dropped through a heated tube D.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2301727A GB301775A (en) | 1927-09-01 | 1927-09-01 | Improvements in the production of gases rich in olefines from bituminous coals |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2301727A GB301775A (en) | 1927-09-01 | 1927-09-01 | Improvements in the production of gases rich in olefines from bituminous coals |
Publications (1)
Publication Number | Publication Date |
---|---|
GB301775A true GB301775A (en) | 1928-12-03 |
Family
ID=10188742
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2301727A Expired GB301775A (en) | 1927-09-01 | 1927-09-01 | Improvements in the production of gases rich in olefines from bituminous coals |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB301775A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE969196C (en) * | 1950-11-23 | 1958-05-08 | Ludwig Weber Dipl Kfm | Process for degassing or thermal splitting of fuels and subsequent gasification of the solid degassing or splitting residue |
DE971243C (en) * | 1951-05-31 | 1958-12-31 | Demag Ag | Process for the production of gas and tar in the production of fuel dust from solid fuels |
DE974851C (en) * | 1952-09-19 | 1961-05-18 | Ruhrgas Ag | Process for the conversion of hydrocarbon compounds |
DE977147C (en) * | 1943-08-17 | 1965-04-01 | Demag Ag | Process for smoldering or coking of lump fuels |
DE1240037B (en) * | 1957-10-02 | 1967-05-11 | Ruhrgas Ag | Process for the thermal treatment of coals |
-
1927
- 1927-09-01 GB GB2301727A patent/GB301775A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE977147C (en) * | 1943-08-17 | 1965-04-01 | Demag Ag | Process for smoldering or coking of lump fuels |
DE969196C (en) * | 1950-11-23 | 1958-05-08 | Ludwig Weber Dipl Kfm | Process for degassing or thermal splitting of fuels and subsequent gasification of the solid degassing or splitting residue |
DE971243C (en) * | 1951-05-31 | 1958-12-31 | Demag Ag | Process for the production of gas and tar in the production of fuel dust from solid fuels |
DE974851C (en) * | 1952-09-19 | 1961-05-18 | Ruhrgas Ag | Process for the conversion of hydrocarbon compounds |
DE1240037B (en) * | 1957-10-02 | 1967-05-11 | Ruhrgas Ag | Process for the thermal treatment of coals |
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