GB337581A - Improvements in or relating to the distillation of tar or oil - Google Patents
Improvements in or relating to the distillation of tar or oilInfo
- Publication number
- GB337581A GB337581A GB1823129A GB1823129A GB337581A GB 337581 A GB337581 A GB 337581A GB 1823129 A GB1823129 A GB 1823129A GB 1823129 A GB1823129 A GB 1823129A GB 337581 A GB337581 A GB 337581A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pitch
- tank
- tar
- wilton
- condensers
- 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)
- Working-Up Tar And Pitch (AREA)
- Industrial Gases (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
337,581. Wilton, T. O., and Chemical Engineering & Wilton's Patent Furnace Co., Ltd. June 13, 1929.Addition to 307,577. Hydrocarbons, distilling.-In the process for distilling tar described in the parent Specification more intimate admixture of the crude tar and the pitch from the process is obtained by introducing them side by side through pipes yinto the constant level tank b. The mixture is then fed to the heating coils f, g and vapour box from which vapours pass to condensers k, l, while the pitch is returned through a pipe o to the tank b. When the pitch has reached the required consistency a proportion is tapped off through a valve q and led to a still r where the residual volatile constituents' are removed by straining and condensed in a condenser t. The vapours evolved from the box j at the commencement of the process are condensed separately in a condenser n. Vacuum may be applied to any of the separating tanks v of the condensers. The crude tar from a storage tank a is preheated by the pitch in an exchanger e and fed to the tank b through a constant level device c. Specifications 26910/07 and 127,700 are referred to.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB1823129A GB337581A (en) | 1928-01-10 | 1929-06-13 | Improvements in or relating to the distillation of tar or oil |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB84928A GB307577A (en) | 1928-01-10 | 1928-01-10 | Improvements in and relating to processes and plants for the distillation of tar |
| GB1823129A GB337581A (en) | 1928-01-10 | 1929-06-13 | Improvements in or relating to the distillation of tar or oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB337581A true GB337581A (en) | 1930-11-13 |
Family
ID=10108894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB1823129A Expired GB337581A (en) | 1928-01-10 | 1929-06-13 | Improvements in or relating to the distillation of tar or oil |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB337581A (en) |
-
1929
- 1929-06-13 GB GB1823129A patent/GB337581A/en not_active Expired
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1524192A (en) | Method for dehydrating organic liquids | |
| GB337581A (en) | Improvements in or relating to the distillation of tar or oil | |
| US1318657A (en) | Method of and apparatus for distillation. | |
| US2132137A (en) | Treating hydrocarbon oils | |
| US2008578A (en) | Light hydrocarbon distillation | |
| GB318897A (en) | Distillation of tar | |
| US2007146A (en) | Removal of naphthenic acids from hydrocarbon oils | |
| US1982091A (en) | Conversion of petroleum oils | |
| US1878932A (en) | Motor fuel process | |
| GB368838A (en) | Improvements relating to the distillation of hydrocarbons and apparatus therefor | |
| US2017820A (en) | Mineral oil distillation | |
| US1809167A (en) | Method of condensing gasoline vapors | |
| US1935967A (en) | Treating hydrocarbon oils | |
| US1814042A (en) | Process for transformation of petroleum hydrocarbons into gasoline | |
| US1854835A (en) | Treating hydrocarbon oils | |
| US1326073A (en) | Almer mcduffie mcafee | |
| DE617594C (en) | Process for the production of knock-resistant motor fuels from high-boiling hydrocarbons | |
| US1868738A (en) | Process of destructively distilling bitumen | |
| US1897618A (en) | Recovering condensable vapors from incondensable gas | |
| DE587313C (en) | Process for splitting hydrocarbon oils | |
| GB422971A (en) | An improved process and apparatus for cracking hydrocarbons | |
| GB319224A (en) | Method of and means for cracking oils | |
| GB424645A (en) | Improvements in or relating to the distillation of tar and the cracking of oil | |
| GB239841A (en) | Method and apparatus for the continuous distillation of tar and like substances and for the continuous rectifying of their by-products | |
| GB512371A (en) | Process for the fractionation of mixtures of hydrocarbons or other liquids |