GB847840A - Process of manufacturing coke - Google Patents
Process of manufacturing cokeInfo
- Publication number
- GB847840A GB847840A GB1220857A GB1220857A GB847840A GB 847840 A GB847840 A GB 847840A GB 1220857 A GB1220857 A GB 1220857A GB 1220857 A GB1220857 A GB 1220857A GB 847840 A GB847840 A GB 847840A
- Authority
- GB
- United Kingdom
- Prior art keywords
- coke
- temperature
- needle
- coal
- produced
- 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
- 239000000571 coke Substances 0.000 title abstract 7
- 238000000034 method Methods 0.000 title abstract 5
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 239000010426 asphalt Substances 0.000 abstract 3
- 239000003245 coal Substances 0.000 abstract 3
- 238000004939 coking Methods 0.000 abstract 3
- 239000000463 material Substances 0.000 abstract 3
- 239000011280 coal tar Substances 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 2
- 239000011295 pitch Substances 0.000 abstract 2
- 239000002904 solvent Substances 0.000 abstract 2
- 239000011269 tar Substances 0.000 abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 1
- 239000011230 binding agent Substances 0.000 abstract 1
- 238000009835 boiling Methods 0.000 abstract 1
- 238000005119 centrifugation Methods 0.000 abstract 1
- 238000007701 flash-distillation Methods 0.000 abstract 1
- 235000013312 flour Nutrition 0.000 abstract 1
- 238000002309 gasification Methods 0.000 abstract 1
- 239000010439 graphite Substances 0.000 abstract 1
- 229910002804 graphite Inorganic materials 0.000 abstract 1
- 239000003973 paint Substances 0.000 abstract 1
- 239000002006 petroleum coke Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 239000011343 solid material Substances 0.000 abstract 1
- 239000011299 tars and pitches Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
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
- C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
- Working-Up Tar And Pitch (AREA)
Abstract
Coke, which is suitable for the production of graphite electrodes, and which, when crushed to a fine size, shows a needle-like structure, is produced by removing from a high boiling liquefiable coal-derived bitumen the components which readily form an insoluble phase upon heating, coking the remaining residuum at a temperature between 400 DEG C. and 500 DEG C. under conditions substantially free from temperature gradients until the material solidifies and heating the resulting solid material at a temperature between 500 DEG C. and 600 DEG C. to complete the coking. Suitable coal-derived bitumens are coal gasification tars, coke oven tars, water gas tars and pitches derived therefrom. The insoluble phase may be removed by several methods. In one method, a charging stock of coal tar which contains up to 25% of matter substantially insoluble therein is heated to a temperature below 400 DEG C. and filtered at between 150 DEG and 250 DEG C. In another method a coal tar is flash distilled at atmospheric or sub-atmospheric pressure. In another embodiment bitumen is preheated in a pipe coil to a temperature of 400 DEG -600 DEG C., and then continuously passed to a flash distillation zone from which vapours are taken overhead and coked to form the needle-like coke. In another form the pitch or similar material has added thereto a solvent such as a paint thinner, to reduce its viscosity and the material is subsequently filtered. According to another method the bitumen with or without a solvent is treated to a centrifugation operation followed by recovery and coking of the comparatively solid-free fraction. The needle-like coke when calcined may be mixed with a binder such as electrode pitch and with coke flour produced from needle-like coke or from commercially produced petroleum coke and extruded or moulded into the desired configuration, the electrodes so produced being baked at a temperature up to 1200 DEG C. The baked pieces may be subsequently graphitised at temperatures between 2500 DEG C. and 3000 DEG C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1220857A GB847840A (en) | 1957-04-15 | 1957-04-15 | Process of manufacturing coke |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1220857A GB847840A (en) | 1957-04-15 | 1957-04-15 | Process of manufacturing coke |
Publications (1)
Publication Number | Publication Date |
---|---|
GB847840A true GB847840A (en) | 1960-09-14 |
Family
ID=10000316
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1220857A Expired GB847840A (en) | 1957-04-15 | 1957-04-15 | Process of manufacturing coke |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB847840A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4104150A (en) * | 1974-07-17 | 1978-08-01 | Bergwerksverband Gmbh | Process for the production of coke from pitch |
US4116815A (en) * | 1977-06-21 | 1978-09-26 | Nittetsu Chemical Industrial Co., Ltd. | Process for preparing needle coal pitch coke |
FR2464920A1 (en) * | 1979-09-06 | 1981-03-20 | Mitsubishi Chem Ind | PROCESS FOR PRODUCING A CARBON-BASED PRODUCT FROM A HOT-TYPE HYDROCARBON SOURCE |
US4289604A (en) * | 1976-04-03 | 1981-09-15 | Bergwerksverband Gmbh | Method of producing an isotropic coke |
US4292170A (en) * | 1977-07-28 | 1981-09-29 | The Lummus Company | Removal of quinoline insolubles from coal derived fractions |
-
1957
- 1957-04-15 GB GB1220857A patent/GB847840A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4104150A (en) * | 1974-07-17 | 1978-08-01 | Bergwerksverband Gmbh | Process for the production of coke from pitch |
US4289604A (en) * | 1976-04-03 | 1981-09-15 | Bergwerksverband Gmbh | Method of producing an isotropic coke |
US4116815A (en) * | 1977-06-21 | 1978-09-26 | Nittetsu Chemical Industrial Co., Ltd. | Process for preparing needle coal pitch coke |
US4292170A (en) * | 1977-07-28 | 1981-09-29 | The Lummus Company | Removal of quinoline insolubles from coal derived fractions |
FR2464920A1 (en) * | 1979-09-06 | 1981-03-20 | Mitsubishi Chem Ind | PROCESS FOR PRODUCING A CARBON-BASED PRODUCT FROM A HOT-TYPE HYDROCARBON SOURCE |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
GB1290234A (en) | ||
US3692663A (en) | Process for treating tars | |
US4072599A (en) | Carbon electrodes having stabilized binders derived from the entire organic fraction of bituminous coal | |
US4292170A (en) | Removal of quinoline insolubles from coal derived fractions | |
JPH0256393B2 (en) | ||
GB1481800A (en) | Production of coke | |
US4405439A (en) | Removal of quinoline insolubles from coal derived fractions | |
GB847840A (en) | Process of manufacturing coke | |
US3761387A (en) | Process for producing an electrode pitch which can be easily graphitized | |
GB963435A (en) | Improved method for obtaining metallurgical coke from poorly-coking coals | |
US2916432A (en) | Utilization of low-temperature tars | |
US2983665A (en) | Utilization of low-temperature tars | |
SU448650A3 (en) | Method for producing needle coke | |
US3035932A (en) | Electrode binder pitch | |
US2970953A (en) | Carbonization of lignite | |
US2964460A (en) | Liquid carbon black feedstock | |
Jastrzebski et al. | Research on high-quality pitch-based materials | |
GB1494311A (en) | Process for the production of liquid fuels of low ash content | |
GB829196A (en) | Improvements in or relating to process for producing a needle-like coke | |
GB789663A (en) | Improvements in or relating to production of denser graphite | |
CA1063960A (en) | Binder pitch from petroleum-base stock | |
US1224788A (en) | Process of securing combustible fluids from carbonaceous solids. | |
GB2065696A (en) | Process for the coking quality of coals having unsatisfactory properties | |
DE2064695C3 (en) | Process for the production of an anisotropic and easily graphitizable coke | |
GB964574A (en) | Production of ash-free coke from coal |