GB686181A - Process and installation for the production of finely divided coke from bituminous fuel - Google Patents
Process and installation for the production of finely divided coke from bituminous fuelInfo
- Publication number
- GB686181A GB686181A GB31422/49A GB3142249A GB686181A GB 686181 A GB686181 A GB 686181A GB 31422/49 A GB31422/49 A GB 31422/49A GB 3142249 A GB3142249 A GB 3142249A GB 686181 A GB686181 A GB 686181A
- Authority
- GB
- United Kingdom
- Prior art keywords
- retort
- fuel
- finely divided
- bituminous
- coke
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
686,181. Coking bituminous fuels. KOPPERS CO., Inc. Dec. 7, 1949 [Dec. 7, 1948], No. 31422/49. Class 55 (i). Finely divided coke is obtained from bituminous uels such as pitch, asphalt, mineral oil residues and bituminous coal by injecting the fuel in a finely divided state suspended in a cold carrier gas containing free oxygen into a heated retort and surrounding the fuel suspension with a veil of hot gases simultaneously introduced into the retort so that the fuel particles are coked to such a degree before reaching the walls of the retort that the residue finally collected does not agglomerate. The heated gases may be waste combustion products and a temperature of between 1200-1500‹C is maintained in the retort. A fuel gas may also be obtained by using pure oxygen as the cold carrier gas. In apparatus described the finely divided fuel is mixed with air or oxygen at the bottom of hoppers 1 and introduced into the retort 5 by the lines 4 and nozzles 6. Hot combustion gases from burners 10 are fed in through the annular spaces 9 and the coke produced is withdrawn from the base of the retort 5 through the line 18. Hot gases and entrained coke particles leaving the retort pass through a waste-heat boiler 21 and then through an electrostatic precipitator 26, finally leaving by the line 29.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH686181X | 1948-12-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB686181A true GB686181A (en) | 1953-01-21 |
Family
ID=4528877
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31422/49A Expired GB686181A (en) | 1948-12-07 | 1949-12-07 | Process and installation for the production of finely divided coke from bituminous fuel |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB686181A (en) |
-
1949
- 1949-12-07 GB GB31422/49A patent/GB686181A/en not_active Expired
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