GB364665A - Improvements in and apparatus for the continuous treatment of solid substances underpressure - Google Patents
Improvements in and apparatus for the continuous treatment of solid substances underpressureInfo
- Publication number
- GB364665A GB364665A GB2973430A GB2973430A GB364665A GB 364665 A GB364665 A GB 364665A GB 2973430 A GB2973430 A GB 2973430A GB 2973430 A GB2973430 A GB 2973430A GB 364665 A GB364665 A GB 364665A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tubes
- gases
- reagents
- hydrocarbons
- parallel
- 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
- 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
- C10G1/06—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation
- C10G1/065—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation in the presence of a solvent
-
- 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
- C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
- C10G1/083—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts in the presence of a solvent
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0364665/III/1> Apparatus for effecting chemical reactions at high temperature and pressure in liquids, vapours or gases or mixtures of these with solids comprises a sheaf of parallel pressure-bearing tubes rotating about an axis parallel to the axes of the tubes and either internally or externally heated. The reagents pass through the tubes in parallel or in series, or several sheaves may be arranged in series. The reagents may travel in the same direction or in counter-current, or reagents may be introduced or reaction products withdrawn, at intermediate points. The movement of solid or viscous materials may be effected by worm conveyers or spiral bands within the tubes; agglomeration may be prevented by rods with sharp edges, chains, or loose solid bodies. Catalysts may be mixed with the reaction substances or inserted in the tubes in the form of loose or rigid bodies or deposited on the walls of the tubes or the latter may be composed of catalytic material. Gases may be introduced through nozzles at the ends of the tubes, or alternatively the tubes may be divided into sections of successively increasing diameter and the gases introduced at the points where the diameter increases. Fig. 1 shows an embodiment of the invention suitable for the destructive hydrogenation of brown coal. The tubes A are mounted in heads B, C which rotate on rollers D, and are heated by flue gases traversing the chamber F. The coal is introduced to the head C through the tube J and the solid product is removed at M. Hydrogen at 200 atmospheres is passed in through the pipe K and hydrocarbon vapours are withdrawn at N. Other reactions to which the invention may be applied are the preparation of metal carbonyls, the condensation of unsaturated or aromatic hydrocarbons, the polymerization of acetylene, the synthesis of ammonia, the hardening of fats or oils, the oxidation of hydrocarbons to fatty acids, the synthesis of methanol, and the reduction of carbon monoxide to hydrocarbons.ALSO:<PICT:0364665/IV/1> Apparatus for effecting chemical reactions at high temperature and pressure in liquids, vapours or gases or mixtures of these with solids comprises a sheaf of parallel pressure-bearing tubes rotating about an axis parallel to the axes of the tubes and either internally or externally heated. The reagents pass through the tubes in parallel or in series, or several sheaves may be arranged in series. The reagents may travel in the same direction or in countercurrent, or reagents may be introduced or reaction products withdrawn at intermediate points. The movement of solid or viscous materials may be effected by worm conveyers or spiral bands within the tubes; agglomeration may be prevented by rods with sharp edges, chains, or loose solid bodies. Catalysts may be mixed with the reaction substances or inserted in the tubes in the form of loose or rigid bodies or deposited on the walls of the tubes or the latter may be composed of catalytic material. Gases may be introduced through nozzles at the ends of the tubes, or alternatively the tubes may be divided into sections of successively increasing diameter and the gases introduced at the points where the diameter increases. The Figure shows an embodiment of the invention suitable for the destructive hydrogenation of brown coal. The tubes A are mounted in heads B, C which rotate on rollers D, and are heated by flue gases traversing the chamber F. The coal is introduced to the head C through the tube J and the solid product is removed at M. Hydrogen at 200 atmospheres is passed through the pipe K and hydrocarbon vapours are withdrawn at N. Other reactions to which the invention may be applied are the condensation of unsaturated or aromatic hydrocarbons, the polymerization of acetylene, the oxidation of hydrocarbons to fatty acids, the synthesis of methanol, and the reduction of carbon monoxide to hydrocarbons.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2973430A GB364665A (en) | 1930-10-04 | 1930-10-04 | Improvements in and apparatus for the continuous treatment of solid substances underpressure |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2973430A GB364665A (en) | 1930-10-04 | 1930-10-04 | Improvements in and apparatus for the continuous treatment of solid substances underpressure |
Publications (1)
Publication Number | Publication Date |
---|---|
GB364665A true GB364665A (en) | 1932-01-04 |
Family
ID=10296288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2973430A Expired GB364665A (en) | 1930-10-04 | 1930-10-04 | Improvements in and apparatus for the continuous treatment of solid substances underpressure |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB364665A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2419508A (en) * | 1941-10-01 | 1947-04-22 | Socony Vacuum Oil Co Inc | Apparatus for catalytic conversion |
US2433079A (en) * | 1939-09-30 | 1947-12-23 | Standard Oil Dev Co | Catalytic isomerization process |
DE3503069A1 (en) * | 1985-01-30 | 1986-07-31 | Environment Protection Engineers Ltd., Southfield, Mich. | Indirectly heated rotating-drum reactor, the use thereof and pyrolysis process |
DE3513540A1 (en) * | 1985-04-16 | 1986-10-16 | Elino Industrie-Ofenbau Carl Hanf GmbH + Co, 5160 Düren | Reactor |
-
1930
- 1930-10-04 GB GB2973430A patent/GB364665A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2433079A (en) * | 1939-09-30 | 1947-12-23 | Standard Oil Dev Co | Catalytic isomerization process |
US2419508A (en) * | 1941-10-01 | 1947-04-22 | Socony Vacuum Oil Co Inc | Apparatus for catalytic conversion |
DE3503069A1 (en) * | 1985-01-30 | 1986-07-31 | Environment Protection Engineers Ltd., Southfield, Mich. | Indirectly heated rotating-drum reactor, the use thereof and pyrolysis process |
DE3513540A1 (en) * | 1985-04-16 | 1986-10-16 | Elino Industrie-Ofenbau Carl Hanf GmbH + Co, 5160 Düren | Reactor |
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