GB712097A - Improvements in the coking or cracking of oils, pitches and the like - Google Patents
Improvements in the coking or cracking of oils, pitches and the likeInfo
- Publication number
- GB712097A GB712097A GB25589/50A GB2558950A GB712097A GB 712097 A GB712097 A GB 712097A GB 25589/50 A GB25589/50 A GB 25589/50A GB 2558950 A GB2558950 A GB 2558950A GB 712097 A GB712097 A GB 712097A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- coke
- pitch
- coking
- heating
- 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
- 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)
Abstract
712,097. Coking pitch and like substances ; carbonization furnaces. RUTGERSWERKEAKT.-GES. Oct. 20, 1950 [Oct. 31, 1949], No. 25589/50. Classes 51 (2), 55 (1) and 55 (2) In a process for the coking of pitches, tar, coke-forming oils and like substances, the substance, preferably preheated, is led into a coking chamber heated to at least 1000‹ C. in the form of a stream or streams spaced from the side walls of the chamber. In the apparatus shown in Fig. 1 oils or pitches are injected through a nozzle 3 into a highly heated chamber 1 which is surrounded by a jacket 8, leaving an annular gap 10 through which heating gases are circulated. Gaseous products from the process are withdrawn through a pipe 14 and coke through a worm 21. The heating gases are fed to the annular gap 10 through a pipe 5, a channel 4 and passages 11, the passages 11 being of varying size to distribute the heating gases evenly in the annular gap. The flue gases leave by a pipe 18, tiles 16 with orifices 17 of various sizes being inserted between the pipe 18 and the annular gap 10 to assist in obtaining even heating of the chamber 1. In a modified apparatus shown in Fig. 2 the oil or pitch is injected downwardly into a chamber 23 through a series of nozzles 30, gaseous products are led off through an outlet 34 and coke is withdrawn by bucket wheels 36. Heating gases are admitted directly to the chamber through a series of burners 28 and pass together with the gaseous products from the coking of the oil or pitch into an annular flue 31 connecting with the outlet 34, a series of calibrated openings 32 securing even distribution of the heating gases within the chamber. The heating may be supported by partial combustion of the oil or pitch within the chamber or the injection of the oil or pitch into the chamber may be interrupted periodically while the temperature of the chamber is raised by the introduction of heating gases. Any residual volatile matter in the coke may be removed by a further heat treatment and a coke with a graphitic structure may be obtained. Specification 712,096 and U.S.A. Specification 1.909,587 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE712097X | 1949-10-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB712097A true GB712097A (en) | 1954-07-21 |
Family
ID=6621601
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB25589/50A Expired GB712097A (en) | 1949-10-31 | 1950-10-20 | Improvements in the coking or cracking of oils, pitches and the like |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB712097A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106198133A (en) * | 2016-06-23 | 2016-12-07 | 中国石油大学(华东) | The device and method that quickly preparation simulation pipe is burnt |
-
1950
- 1950-10-20 GB GB25589/50A patent/GB712097A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106198133A (en) * | 2016-06-23 | 2016-12-07 | 中国石油大学(华东) | The device and method that quickly preparation simulation pipe is burnt |
CN106198133B (en) * | 2016-06-23 | 2018-11-20 | 中石油华东设计院有限公司 | The quickly device and method of preparation simulation pipe coke |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE1543122C3 (en) | Process for the production of unsaturated hydrocarbons containing mainly acetylene and ethylene | |
WO2008034424A1 (en) | Method of thermochemical processing of carbonaceous raw materials | |
US3060003A (en) | Process and apparatus for producing carbon black | |
US2659663A (en) | Process for producing carbon black | |
US2270245A (en) | Charcoal activating furnace | |
US1825374A (en) | Method of coking petroleum residues from the distillation of petroleum oils | |
GB712097A (en) | Improvements in the coking or cracking of oils, pitches and the like | |
US2074061A (en) | Production of sulphur dioxide | |
US11168263B2 (en) | Apparatus and method for preparing ethylene and/or acetylene using hydrocarbon | |
US3192127A (en) | Coking retort oven firing method | |
US1639356A (en) | Process of making activated carbon | |
ES416245A1 (en) | Process and apparatus for burning gas and vapor mixture produced in the purification of coke gas ovens | |
US2255406A (en) | Coking retort oven | |
GB1010344A (en) | Process and apparatus for heat treatment of material which yields oxidizable volatile matter under heat | |
US1944872A (en) | Method of coking heavy petroleum residues or the like | |
US2597233A (en) | Manufacture of carbon black | |
US2597992A (en) | Apparatus for production of carbon black | |
US2870087A (en) | Cracking process | |
DE536045C (en) | Process for smoldering fuels, especially those with a high ash content | |
DE508815C (en) | Gas generating plant for the production of carburized water gas from coal | |
DE933983C (en) | Process for smoldering bituminous substances | |
SU68951A2 (en) | The method of heat treatment of hydrocarbon and other liquids | |
GB309253A (en) | Improvements in low-temperature carbonisation for fuels and in apparatus therefor | |
SU69698A1 (en) | Device for continuous coking of petroleum and petroleum products | |
US1856801A (en) | Distilling petroleum residuum |