GB681737A - Process for the continuous distillation of tars - Google Patents
Process for the continuous distillation of tarsInfo
- Publication number
- GB681737A GB681737A GB7791/50A GB779150A GB681737A GB 681737 A GB681737 A GB 681737A GB 7791/50 A GB7791/50 A GB 7791/50A GB 779150 A GB779150 A GB 779150A GB 681737 A GB681737 A GB 681737A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- tar
- withdrawn
- line
- naphthalene
- 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
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/04—Working-up tar by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0681737/III/1> In the continuous distillation of tar, especially coal tar, using a heater, flash-eyaporator and fractionating-column connected in series, a liquid side-stream is withdrawn from the column and recirculated, together with fresh tar, to the heater, flash-evaporator and column. The process obviates the decomposition of components of high molecular weight, in tars having a high content of pitch. Water-free tar is passed through conduit 1 into coil 3 wherein it is heated under pressure. The heated tar is then introduced into evaporation-chamber 5 which is maintained at sub-atmospheric pressure. The vapours, evolved in chamber 5, pass into tray-column 6, while the residue is withdrawn through line 7. A fraction rich in naphthalene is withdrawn from the column through line 9. A washing oil fraction containing a minor amount of naphthalene, is withdrawn from the column through line 13, and is returned to the tar feed-tank through conduit 14. The discharge from the base of the column, taken-off through line 10, is free from naphthalene; this discharge may be added to the residue withdrawn through line 7. The process may be carried out using a series of flash-evaporation stages each of which is associated with a column.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE681737X | 1949-12-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB681737A true GB681737A (en) | 1952-10-29 |
Family
ID=6597011
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7791/50A Expired GB681737A (en) | 1949-12-15 | 1950-03-28 | Process for the continuous distillation of tars |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB681737A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2221221A (en) * | 1988-07-29 | 1990-01-31 | Amoco Corp | Recovering diesel from crude oil |
US5116485A (en) * | 1988-07-29 | 1992-05-26 | Krisa Thomas E | Apparatus and method for recovering diesel-quality fuel from produced crude oil |
CN102161902A (en) * | 2011-03-21 | 2011-08-24 | 上海同特化工科技有限公司 | Coal tar deep processing technology based on four mixed fractions |
CN104673347A (en) * | 2014-12-05 | 2015-06-03 | 莱芜钢铁集团有限公司 | Secondary evaporator series production device in tar distillation and application thereof |
-
1950
- 1950-03-28 GB GB7791/50A patent/GB681737A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2221221A (en) * | 1988-07-29 | 1990-01-31 | Amoco Corp | Recovering diesel from crude oil |
GB2221221B (en) * | 1988-07-29 | 1992-03-18 | Amoco Corp | Apparatus and method for recovering diesel-quality fuel from produced crude oil |
US5116485A (en) * | 1988-07-29 | 1992-05-26 | Krisa Thomas E | Apparatus and method for recovering diesel-quality fuel from produced crude oil |
CN102161902A (en) * | 2011-03-21 | 2011-08-24 | 上海同特化工科技有限公司 | Coal tar deep processing technology based on four mixed fractions |
CN104673347A (en) * | 2014-12-05 | 2015-06-03 | 莱芜钢铁集团有限公司 | Secondary evaporator series production device in tar distillation and application thereof |
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