GB320211A - Improvements in the manufacture and production of olefines and other hydrocarbons and in apparatus therefor - Google Patents
Improvements in the manufacture and production of olefines and other hydrocarbons and in apparatus thereforInfo
- Publication number
- GB320211A GB320211A GB2639728A GB2639728A GB320211A GB 320211 A GB320211 A GB 320211A GB 2639728 A GB2639728 A GB 2639728A GB 2639728 A GB2639728 A GB 2639728A GB 320211 A GB320211 A GB 320211A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- gases
- benzines
- coking
- hopper
- 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
- 238000004519 manufacturing process Methods 0.000 title 2
- 229930195733 hydrocarbon Natural products 0.000 title 1
- 150000002430 hydrocarbons Chemical class 0.000 title 1
- 239000007789 gas Substances 0.000 abstract 5
- 238000010438 heat treatment Methods 0.000 abstract 3
- 239000000463 material Substances 0.000 abstract 3
- 238000004939 coking Methods 0.000 abstract 2
- 239000011148 porous material Substances 0.000 abstract 2
- 239000002893 slag Substances 0.000 abstract 2
- 239000011269 tar Substances 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- BIJOYKCOMBZXAE-UHFFFAOYSA-N chromium iron nickel Chemical compound [Cr].[Fe].[Ni] BIJOYKCOMBZXAE-UHFFFAOYSA-N 0.000 abstract 1
- 239000000571 coke Substances 0.000 abstract 1
- 239000000470 constituent Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 230000001066 destructive effect Effects 0.000 abstract 1
- 238000010410 dusting Methods 0.000 abstract 1
- 238000005984 hydrogenation reaction Methods 0.000 abstract 1
- 239000011261 inert gas Substances 0.000 abstract 1
- 239000002480 mineral oil Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 abstract 1
- 239000004482 other powder Substances 0.000 abstract 1
- 239000008262 pumice Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/02—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Coke Industry (AREA)
Abstract
320,211. Johnson, J. Y., (I. G. Farbenindustrie Akt.-Ges.). Sept. 14, 1928. Addition to 301,775, [Class 55 (i), Coking &c.]. Oil gas.-Gaseous and easily condensible olefines, benzines and aromatic hydrocarbons are obtained from tars, mineral oils, asphalts, or residues from destructive hydrogenation by impregnating granular porous materials such as pumice, slag, or coke with these products and passing the impregnated material quickly through a chamber maintained at red heat and quickly separating and cooling the resulting gas obtained in the manner described in the parent Specification. The carbon deposited on the porous material may be gasified in the manner described in Specification 214,544, (Class 55 (i), Coking &c.], and the gases employed for heating the reaction chamber. Slag impregnated with tar is fed from a hopper F by a conveyer B into a Cowper stove heated by a hot blast from a conduit A. Gases are drawn off through an outlet D and cooled for recovery of the benzines &c. An inert gas is blown by a fan E into the hopper F to prevent hot gases from the chamber below causing the pieces of material to stick together. These pieces may also be prevented from sticking together by dusting with ash or other powder. If the residues contain larger quantities of solid carbonaceous constituents they may be briquetted and passed in this form through the heating chamber. An alternative heating chamber comprising an externally heated nickel-chromium-iron tube through which the material falls, or an inclined revolving tube furnace may be used.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB2639728A GB320211A (en) | 1928-09-14 | 1928-09-14 | Improvements in the manufacture and production of olefines and other hydrocarbons and in apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB2639728A GB320211A (en) | 1928-09-14 | 1928-09-14 | Improvements in the manufacture and production of olefines and other hydrocarbons and in apparatus therefor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB320211A true GB320211A (en) | 1929-10-10 |
Family
ID=10242997
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB2639728A Expired GB320211A (en) | 1928-09-14 | 1928-09-14 | Improvements in the manufacture and production of olefines and other hydrocarbons and in apparatus therefor |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB320211A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE753849C (en) * | 1935-11-01 | 1951-11-08 | Bataafsche Petroleum | Process for the production of higher molecular weight olefins by splitting paraffin-containing hydrocarbon mixtures in the vapor phase |
| US4507517A (en) * | 1983-10-31 | 1985-03-26 | Chevron Research Company | Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a boron compound containing catalyst |
| US4567311A (en) * | 1983-10-31 | 1986-01-28 | Chevron Research Company | Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a silicon compound-containing catalyst |
| US4599474A (en) * | 1983-10-31 | 1986-07-08 | Chevron Research Company | Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a metal-containing catalyst |
-
1928
- 1928-09-14 GB GB2639728A patent/GB320211A/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE753849C (en) * | 1935-11-01 | 1951-11-08 | Bataafsche Petroleum | Process for the production of higher molecular weight olefins by splitting paraffin-containing hydrocarbon mixtures in the vapor phase |
| US4507517A (en) * | 1983-10-31 | 1985-03-26 | Chevron Research Company | Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a boron compound containing catalyst |
| US4567311A (en) * | 1983-10-31 | 1986-01-28 | Chevron Research Company | Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a silicon compound-containing catalyst |
| US4599474A (en) * | 1983-10-31 | 1986-07-08 | Chevron Research Company | Conversions of low molecular weight hydrocarbons to higher molecular weight hydrocarbons using a metal-containing catalyst |
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