GB1090728A - Pyrolysis of coal - Google Patents
Pyrolysis of coalInfo
- Publication number
- GB1090728A GB1090728A GB2208/66A GB220866A GB1090728A GB 1090728 A GB1090728 A GB 1090728A GB 2208/66 A GB2208/66 A GB 2208/66A GB 220866 A GB220866 A GB 220866A GB 1090728 A GB1090728 A GB 1090728A
- Authority
- GB
- United Kingdom
- Prior art keywords
- coal
- stage
- stages
- beds
- sub
- 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
- C10B49/08—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 in dispersed form
- C10B49/10—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 in dispersed form according to the "fluidised bed" technique
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Coal is distilled at low pressure, i.e. at up to 500 p.s.i.g., in at least three fludized bed stages in succession, the beds being at successively higher temperatures. In the first stage the coal is heated at a temperature below its fusion temperature, e.g. at 600 DEG to 650 DEG F., until 1 to 10% b.w. of the dry coal has been removed as volatiles, in the absence of added O2 and of oily vapours from the coal in the succeeding beds; in the second stage, which may comprise two beds in series at different temperatures (see Figs. 1, 2 (not shown)), the coal is heated at a temperature below its fusion temperature (a total range of 700 DEG to 1050 DEG F. is mentioned) in the absence of added O2 for a time sufficient to remove nearly all volatiles condensible to oily liquids; and in the final stage, the coal is substantially devolatilized e.g. at 1500 DEG to 1800 DEG F., air or O2 being supplied to fluidize and partially combust the coal. The first stage is fluidized by hot inert (e.g. flue) gas, which heats the coal, but the second stage may be fluidized by distillation gases from stage 3 or by an inert gas. External heating may be applied to both stages. Some recycling of the char from the later sub-stages of sta to the earlier sub-stages may be carried out (see Fig. 2) to prevent agglomeration, and the vapours from the top of stage 2 and from stage 1 are delivered to a condenser. Residence time in all the stages and sub-stages may be 1 to 30 minutes. Three specific examples are described.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US426812A US3375175A (en) | 1965-01-21 | 1965-01-21 | Pyrolysis of coal |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1090728A true GB1090728A (en) | 1967-11-15 |
Family
ID=23692298
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2208/66A Expired GB1090728A (en) | 1965-01-21 | 1966-01-18 | Pyrolysis of coal |
Country Status (2)
Country | Link |
---|---|
US (1) | US3375175A (en) |
GB (1) | GB1090728A (en) |
Families Citing this family (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3988236A (en) * | 1969-06-05 | 1976-10-26 | Union Carbide Corporation | Process for the continuous hydrocarbonization of coal |
US4358344A (en) * | 1970-07-23 | 1982-11-09 | Occidental Petroleum Corporation | Process for the production and recovery of fuel values from coal |
US3968052A (en) * | 1971-02-11 | 1976-07-06 | Cogas Development Company | Synthesis gas manufacture |
US4108731A (en) * | 1973-11-29 | 1978-08-22 | Centro Sperimentale Metallurgico S.P.A. | Coke production |
DE2429993C3 (en) * | 1974-06-22 | 1984-01-05 | Krupp-Koppers Gmbh, 4300 Essen | Method for generating electrical energy |
US3966634A (en) * | 1974-09-23 | 1976-06-29 | Cogas Development Company | Gasification method |
US3966633A (en) * | 1974-09-23 | 1976-06-29 | Cogas Development Company | Waste water processing |
US3988237A (en) * | 1974-12-27 | 1976-10-26 | Union Carbide Corporation | Integrated coal hydrocarbonization and gasification of char |
US4139416A (en) * | 1975-01-21 | 1979-02-13 | Centro Sperimentale Metallurgico S.P.A. | Carbonaceous material with high characteristics of surface area and activity and process for producing the same |
IT1046993B (en) * | 1975-02-19 | 1980-09-10 | Centro Speriment Metallurg | PROCESS PERFECTED FOR THE PRODUCTION OF COKE FORMATO |
US4597257A (en) * | 1976-09-23 | 1986-07-01 | L. & C. Steinmuller Gmbh | Plant for preparing and hydrolyzing fossil fuels to prepare products low in sulfur content, and employment of these products for a combined generation of the electric current and gas |
DE2715536C2 (en) * | 1977-04-07 | 1982-07-15 | Bergwerksverband Gmbh | Method and device for recovering waste heat from coke ovens |
US4213826A (en) * | 1978-10-02 | 1980-07-22 | Cogas Development Company | Fluidized coal carbonization |
DE2941392A1 (en) * | 1979-10-12 | 1981-04-23 | FMC Corp., 19103 Philadelphia, Pa. | Conversion of coal to gas and liq. products - with by=product recycle to char gasifier |
US4338184A (en) * | 1979-10-26 | 1982-07-06 | Exxon Research & Engineering Co. | Coal conversion in the presence of added alkali metal compounds |
US4313816A (en) * | 1980-08-25 | 1982-02-02 | Exxon Research & Engineering Co. | Staged temperature coal conversion process |
US4322283A (en) * | 1980-09-04 | 1982-03-30 | Exxon Research & Engineering Co. | Coal conversion in the presence of added hydrogen sulfide |
US4303415A (en) * | 1980-09-29 | 1981-12-01 | Lubille Energy Development Co., Ltd. | Gasification of coal |
US4563197A (en) * | 1982-02-16 | 1986-01-07 | The United States Of America As Represented By The Department Of Energy | Process for the production of ethylene and other hydrocarbons from coal |
DD237762A3 (en) * | 1984-01-30 | 1986-07-30 | Schwermasch Liebknecht Veb K | METHOD AND APPARATUS FOR MULTI-STAGE TREATMENT OF ORGANIC SHOOTERS |
US5232679A (en) * | 1989-05-22 | 1993-08-03 | Jha Mahesh C | Process for production of value-added coproducts from coal and other carbonaceous materials |
PT2336274E (en) * | 1999-04-07 | 2013-09-25 | Ivanhoe Htl Petroleum Ltd | Rapid thermal processing of heavy oil feedstocks |
US20090014689A1 (en) * | 2007-07-09 | 2009-01-15 | Range Fuels, Inc. | Methods and apparatus for producing syngas and alcohols |
BRPI0812602A2 (en) * | 2007-07-09 | 2019-09-24 | Range Fuels Inc | "Method for the production of one or more c2-C4 alcohols, method for the production of a cn + m alcohol, method for the purification of one or more alcohols, method for the production of a purified alcohol and apparatus for producing a purified alcohol" |
US20100038288A1 (en) * | 2008-08-12 | 2010-02-18 | MR&E, Ltd. | Refining coal-derived liquid from coal gasification, coking, and other coal processing operations |
US8394240B2 (en) * | 2009-07-14 | 2013-03-12 | C2O Technologies, Llc | Process for treating bituminous coal by removing volatile components |
US8470134B2 (en) * | 2009-07-14 | 2013-06-25 | C2O Technologies, Llc | Process for treating coal by removing volatile components |
WO2012037454A2 (en) | 2010-09-16 | 2012-03-22 | Rinker Franklin G | Coal processing with added biomass and volatile control |
US8968520B2 (en) | 2011-06-03 | 2015-03-03 | National Institute Of Clean And Low-Carbon Energy (Nice) | Coal processing to upgrade low rank coal having low oil content |
US9005322B2 (en) | 2011-07-12 | 2015-04-14 | National Institute Of Clean And Low-Carbon Energy (Nice) | Upgrading coal and other carbonaceous fuels using a lean fuel gas stream from a pyrolysis step |
US9074138B2 (en) | 2011-09-13 | 2015-07-07 | C2O Technologies, Llc | Process for treating coal using multiple dual zone steps |
CN103958398B (en) | 2011-09-27 | 2016-01-06 | 国际热化学恢复股份有限公司 | Synthetic gas cleaning system and method |
CN104955921B (en) | 2013-01-09 | 2017-09-15 | C2O技术发展公司 | Handle method of the coal to improve the recovery of condensable coal derived liquid |
US9707532B1 (en) | 2013-03-04 | 2017-07-18 | Ivanhoe Htl Petroleum Ltd. | HTL reactor geometry |
US9327320B1 (en) | 2015-01-29 | 2016-05-03 | Green Search, LLC | Apparatus and method for coal dedusting |
US10286431B1 (en) * | 2016-03-25 | 2019-05-14 | Thermochem Recovery International, Inc. | Three-stage energy-integrated product gas generation method |
US10364398B2 (en) | 2016-08-30 | 2019-07-30 | Thermochem Recovery International, Inc. | Method of producing product gas from multiple carbonaceous feedstock streams mixed with a reduced-pressure mixing gas |
EP4257660A3 (en) * | 2021-01-06 | 2024-01-03 | GIDARA Energy B.V. | Process and apparatus for producing synthesis gas through thermochemical conversion of biomass and waste materials |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2955077A (en) * | 1955-11-30 | 1960-10-04 | Consolidation Coal Co | Fluidized carbonization process for agglomerative coals |
US3047472A (en) * | 1959-01-09 | 1962-07-31 | Consolidation Coai Company | Size separation, preoxidation and fluidized low temperature carbonization of coal |
US3076751A (en) * | 1959-08-27 | 1963-02-05 | United Eng & Constructors Inc | Process for the low temperature carbonization of bituminous coal |
-
1965
- 1965-01-21 US US426812A patent/US3375175A/en not_active Expired - Lifetime
-
1966
- 1966-01-18 GB GB2208/66A patent/GB1090728A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US3375175A (en) | 1968-03-26 |
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