GB1122134A - Improvements in or relating to shaped coke manufacture - Google Patents
Improvements in or relating to shaped coke manufactureInfo
- Publication number
- GB1122134A GB1122134A GB2300/67A GB230067A GB1122134A GB 1122134 A GB1122134 A GB 1122134A GB 2300/67 A GB2300/67 A GB 2300/67A GB 230067 A GB230067 A GB 230067A GB 1122134 A GB1122134 A GB 1122134A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sand
- gas
- reactor
- coke
- coal
- 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
- C10B49/16—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 moving solid heat-carriers in divided form
- C10B49/20—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 moving solid heat-carriers in divided form in dispersed form
- C10B49/22—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 moving solid heat-carriers in divided form in dispersed form according to the "fluidised bed" technique
-
- 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
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/08—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form in the form of briquettes, lumps and the like
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
- F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
- F28C3/16—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material forming a bed, e.g. fluidised, on vibratory sieves
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Coke Industry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
In a method of continuously making shaped coke articles by means of a circulating granular heat carrier, e g sand, shaped coal articles (briquettes) and hot sand are charged into the upper end of a reactor 1 and passed downwardly therethrough with the articles embedded in the sand, the coke being separated at the bottom at 7 from the sand and cooled at 9, and the sand being simultaneously reheated and recycled pneumatically to the top of the reactor at 14. The upper portion 2 of the charge in the reactor is maintained as a fluidized bed using the distillation gases as fluidizing gas, the cross-section of the reactor and the ratio of sand to <PICT:1122134/C4-C5/1> coal being selected accordingly. Pulses of a gas introduced at 5 periodically force the coke and sand over a weir 6 on to a screen 7, the sand returning via a tube 8 and a fluidized bed 12 to a riser 14 supplied with gases from a combustion chamber 15. Fuel gas may be supplied at 16 to burn coke in the sand with excess oxygen in the gases. Cooling at 9 is by a gas cooled indirectly at 11. Hot gas from 9 may alternatively be directed to the coal hopper 22 to preheat or swell the coal, as illustrated. Gas, e.g. steam, may be introduced at 3.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB0085477 | 1966-01-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1122134A true GB1122134A (en) | 1968-07-31 |
Family
ID=6982925
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2300/67A Expired GB1122134A (en) | 1966-01-20 | 1967-01-16 | Improvements in or relating to shaped coke manufacture |
Country Status (5)
Country | Link |
---|---|
US (1) | US3444048A (en) |
BE (1) | BE692933A (en) |
DE (1) | DE1571639A1 (en) |
FR (1) | FR1508687A (en) |
GB (1) | GB1122134A (en) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3671401A (en) * | 1970-07-09 | 1972-06-20 | Cons Coal Co | Method of calcining and desulfurizing carbonaceous contiguous bed of agglomerates with particulate heat carriers |
US3717440A (en) * | 1970-08-20 | 1973-02-20 | Climax Chem | Solid-liquid contacting apparatus |
US3896026A (en) * | 1973-09-27 | 1975-07-22 | Texaco Inc | Methods and apparatus for forming a dense phase catalyst transfer system |
US4077847A (en) * | 1975-08-11 | 1978-03-07 | Occidental Petroleum Corporation | Solid waste disposal system |
US4088541A (en) * | 1975-08-11 | 1978-05-09 | Occidental Petroleum Corporation | Apparatus for pyrolyzing organic solid waste |
US4078973A (en) * | 1976-07-12 | 1978-03-14 | Occidental Petroleum Corporation | Loop pyrolysis process for organic solid wastes |
US4147593A (en) * | 1976-07-21 | 1979-04-03 | Occidental Petroleum Corporation | Flash pyrolysis of organic solid waste employing ash recycle |
US4158385A (en) * | 1977-12-09 | 1979-06-19 | Vandenhoeck J | Energy recovery and storage system |
US4575948A (en) * | 1979-09-07 | 1986-03-18 | Consolidated Natural Gas Service Company, Inc. | Pneumatic transport and heat exchange systems |
US9441887B2 (en) * | 2011-02-22 | 2016-09-13 | Ensyn Renewables, Inc. | Heat removal and recovery in biomass pyrolysis |
US10041667B2 (en) | 2011-09-22 | 2018-08-07 | Ensyn Renewables, Inc. | Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same |
US10400175B2 (en) | 2011-09-22 | 2019-09-03 | Ensyn Renewables, Inc. | Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material |
CN103571511B (en) * | 2012-07-30 | 2015-03-25 | 中国石油化工集团公司 | Powder coal dry distillation method and device |
CN103571510B (en) * | 2012-07-30 | 2015-03-25 | 中国石油化工集团公司 | Powder coal dry distillation method and device |
CN104178184B (en) * | 2013-05-23 | 2016-09-14 | 中石化洛阳工程有限公司 | The fluidized bed dry distillation method and apparatus of coal dust |
CN103666509B (en) * | 2013-12-02 | 2015-04-22 | 北京市工业设计研究院 | Solid heat carrier dry distillation furnace |
MY193949A (en) | 2016-12-29 | 2022-11-02 | Ensyn Renewables Inc | Demetallization Of Liquid Biomass |
RU2697472C1 (en) * | 2019-03-13 | 2019-08-14 | Сергей Айдынович Адыгезалов | Method of thermo-oxidative coking and device for its implementation |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2131702A (en) * | 1936-10-24 | 1938-09-27 | Nat Fuels Corp | Coal processing |
US2480670A (en) * | 1942-05-02 | 1949-08-30 | Standard Oil Dev Co | Two-zone fluidized destructive distillation process |
DE1135419B (en) * | 1952-09-26 | 1962-08-30 | Metallgesellschaft Ag | Process for degassing or gasifying fuels by means of carbonaceous, fine-grained heat carriers |
US2741549A (en) * | 1952-11-01 | 1956-04-10 | Exxon Research Engineering Co | Conversion of carbonaceous solids into volatile products |
US2743216A (en) * | 1954-09-17 | 1956-04-24 | Exxon Research Engineering Co | Calcination of fluid coke utilizing shot |
US2984602A (en) * | 1957-12-11 | 1961-05-16 | Oil Shale Corp | Method and apparatus for stripping oil from oil shale |
US2879208A (en) * | 1958-05-19 | 1959-03-24 | Fluor Corp | Shale oil recovery method and apparatus |
US3140240A (en) * | 1960-07-21 | 1964-07-07 | Consolidation Coal Co | Process for carbonizing coal |
US3117064A (en) * | 1961-07-03 | 1964-01-07 | Consolidation Coal Co | Shock heater |
-
1966
- 1966-01-20 DE DE19661571639 patent/DE1571639A1/de not_active Withdrawn
-
1967
- 1967-01-16 GB GB2300/67A patent/GB1122134A/en not_active Expired
- 1967-01-19 US US610451A patent/US3444048A/en not_active Expired - Lifetime
- 1967-01-20 BE BE692933D patent/BE692933A/xx unknown
- 1967-01-20 FR FR91877A patent/FR1508687A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
BE692933A (en) | 1967-07-20 |
US3444048A (en) | 1969-05-13 |
DE1571639A1 (en) | 1970-03-05 |
FR1508687A (en) | 1968-01-05 |
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