GB953781A - Destructive distillation of coal - Google Patents
Destructive distillation of coalInfo
- Publication number
- GB953781A GB953781A GB2820/62A GB282062A GB953781A GB 953781 A GB953781 A GB 953781A GB 2820/62 A GB2820/62 A GB 2820/62A GB 282062 A GB282062 A GB 282062A GB 953781 A GB953781 A GB 953781A
- Authority
- GB
- United Kingdom
- Prior art keywords
- coal
- coke
- solids
- outlet
- oxygen
- 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
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
- C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
- C10B49/06—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated according to the moving bed type
-
- 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
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
- C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
<PICT:0953781/C3/1> A continuous process for the destructive distillation of coal comprises passing the coal progressively upwardly through a vertical treatment zone, introducing an oxygen-containing gas (air) into the coal at an intermediate location 42a to flow co-currently with the coal, establishing a combustion front 50 of limited vertical extent in the coal tending to move counter-current thereto, oxygen being consumed in the front to provide an oxygen-free zone behind the front through which the coal passes, directing hot gases, e.g. the products of combustion, through the coal leaving the front 50 to maintain distillation temperatures, removing evolved products (coal tar, coke-oven gases, combustion products) at 44 separately from the coke, and cooling the coke, e.g. by water quenching at 47, before discharge. The position of the front 50 is stabilized by regulating the input of air at 42 and by establishing a balance between the coal input and solids output. The temperature of the front 50 and the rate of coal feed, of coal movement, and of solids removal, may be automatically controlled. Recycled coke oven gas may be included in the air delivered, and the coal, which moves upwardly, may be preheated at 41, e.g. by recycled gas. The retort 34 is surrounded by an insulating chamber 40 having a water jacket 43. Rapid, intermittent charging takes place at the inlet 37 (see Division F4). In two further embodiments, coal passes downwardly and breakers, e.g. rolls, are included near the bottom of the retort, see Figs. 2, 4 (not shown), and the outlet corresponding to 44 has a baffle to prevent entry of solids. Temperatures of 1100 DEG F. to 2000 DEG F. are mentioned for the front 50, and gases flow away from the front to the outlet 44 by virtue of an exhaust pump in the outlet line or by making a high pressure in the bottom of the chamber 40 by suitably sealing the solids outlet.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US84809A US3141834A (en) | 1961-01-25 | 1961-01-25 | Process for continuous destructive distillation and carbonization of coal |
Publications (1)
Publication Number | Publication Date |
---|---|
GB953781A true GB953781A (en) | 1964-04-02 |
Family
ID=22187341
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2820/62A Expired GB953781A (en) | 1961-01-25 | 1962-01-25 | Destructive distillation of coal |
Country Status (2)
Country | Link |
---|---|
US (1) | US3141834A (en) |
GB (1) | GB953781A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3271268A (en) * | 1963-01-21 | 1966-09-06 | Marathon Oil Co | Process of calcining coke |
DE2805244A1 (en) * | 1978-02-08 | 1979-08-09 | Metallgesellschaft Ag | METHOD AND DEVICE FOR COOLING DUSTY OR FINE-GRAINED SOLIDS |
US4967673A (en) * | 1988-12-16 | 1990-11-06 | Gunn Robert D | Counterflow mild gasification process and apparatus |
DE10206922B4 (en) * | 2002-02-19 | 2010-08-26 | Herhof Verwaltungsgesellschaft Mbh | Pyrolysis shaft furnace and use of a pyrolysis shaft furnace |
EP2413032B1 (en) * | 2010-07-27 | 2016-01-06 | MS-Technologie GmbH | Shaft furnace for carbonization of organic solid fuels |
CN106833702A (en) * | 2017-03-31 | 2017-06-13 | 神木县三江煤化工有限责任公司 | Fine coal low-temperature carbonization system and method and coal low-temperature carbonization system |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1781766A (en) * | 1922-09-09 | 1930-11-18 | Gas Res Co | Method of and apparatus for generating combustible gas and coke |
US1536696A (en) * | 1923-09-17 | 1925-05-05 | Wallace George Wightman | Process of carbonizing |
US1772189A (en) * | 1924-07-15 | 1930-08-05 | Consolidation Coal Products Co | Method of producing carbonized briquettes |
US1669024A (en) * | 1924-11-06 | 1928-05-08 | Internat Coal Carbonization Co | Carbonization of coal |
GB468405A (en) * | 1936-03-25 | 1937-07-05 | Arthur Robert Griggs | Improvements in the carbonisation of coal and the like carbonaceous material |
US2501153A (en) * | 1947-01-21 | 1950-03-21 | Union Oil Co | Shale oil eduction |
US2723225A (en) * | 1951-09-13 | 1955-11-08 | Socony Mobil Oil Co Inc | Shale retorting method and apparatus |
US2954329A (en) * | 1958-06-19 | 1960-09-27 | Union Oil Co | Eduction apparatus |
-
1961
- 1961-01-25 US US84809A patent/US3141834A/en not_active Expired - Lifetime
-
1962
- 1962-01-25 GB GB2820/62A patent/GB953781A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US3141834A (en) | 1964-07-21 |
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