GB129992A - Process of and Apparatus for Recovering Bitumens from Shale and the like. - Google Patents
Process of and Apparatus for Recovering Bitumens from Shale and the like.Info
- Publication number
- GB129992A GB129992A GB17777/19A GB1777719A GB129992A GB 129992 A GB129992 A GB 129992A GB 17777/19 A GB17777/19 A GB 17777/19A GB 1777719 A GB1777719 A GB 1777719A GB 129992 A GB129992 A GB 129992A
- Authority
- GB
- United Kingdom
- Prior art keywords
- light oil
- discharged
- extracting
- pipe
- shale
- 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
- 239000003921 oil Substances 0.000 abstract 5
- 239000010426 asphalt Substances 0.000 abstract 2
- 239000000470 constituent Substances 0.000 abstract 2
- 239000000295 fuel oil Substances 0.000 abstract 2
- 239000012188 paraffin wax Substances 0.000 abstract 2
- 239000007787 solid Substances 0.000 abstract 2
- 239000004927 clay Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 230000008021 deposition Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000002480 mineral oil Substances 0.000 abstract 1
- 238000000197 pyrolysis Methods 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
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
- C10C3/00—Working-up pitch, asphalt, bitumen
- C10C3/007—Working-up pitch, asphalt, bitumen winning and separation of asphalt from mixtures with aggregates, fillers and other products, e.g. winning from natural asphalt and regeneration of waste asphalt
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/04—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Analytical Chemistry (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
129,992. Ryan, H. D. March 28, 1918, [Convention date]. Mineral oils, extracting; paraffin wax, extracting.-In extracting bitumen, paraffin wax, and other constituents from shale &c., the latter is digested with heavy oil at a temperature too low to effect destructive distillation, and the hot digest or solution is separated from solid residual matter and discharged into a bath of light oil, in order to prevent the deposition of bitumen on cooling. The shale is fed by a screw conveyer 3 to a retort 2 containing a cylindrical screen 5 rotating in a bath of heavy oil 14 at a temperature of about 600 F. ; volatile constituents escape to a condensing coil 50, and refractory solid matter is discharged from an outlet 11. The solution flows through a pipe 16 into a conical tank 17 containing gasolene. Volatilized light oil escapes to a condenser 32 and is returned to the tank through a pipe 21, and the solution meeting an upward current of light oil is carried into tanks 36, 37, 38; these tanks contain heating coils 39, and light oil is again driven off to the condenser 32. Part of the digest is returned to the retort through a pipe 46 and the remainder is withdrawn through pipes 42 for further treatment. Clay &c. is discharged from the tank 17 and conveyed through a heated chamber 25 for the recovery of light oil.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US225344A US1327572A (en) | 1918-03-28 | 1918-03-28 | Process of recovering bituminous matter from shale |
Publications (1)
Publication Number | Publication Date |
---|---|
GB129992A true GB129992A (en) | 1920-11-16 |
Family
ID=22844508
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB17777/19A Expired GB129992A (en) | 1918-03-28 | 1919-07-16 | Process of and Apparatus for Recovering Bitumens from Shale and the like. |
Country Status (3)
Country | Link |
---|---|
US (1) | US1327572A (en) |
FR (1) | FR501524A (en) |
GB (1) | GB129992A (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2457457A (en) * | 1942-02-13 | 1948-12-28 | Alais & Froges & Camarque Cie | Methods for treating bituminous shales |
US2431677A (en) * | 1945-06-08 | 1947-12-02 | Harry D Brown | Process for the recovery of oil from shales |
US2489700A (en) * | 1945-08-04 | 1949-11-29 | Clarence H Dragert | Recovery of values from rock asphalt and like material |
US2489701A (en) * | 1945-08-04 | 1949-11-29 | Clarence H Dragert | Recovery of values from rock asphalt and like material |
US2487788A (en) * | 1945-09-05 | 1949-11-15 | Us Interior | Processing oil shale |
US2471107A (en) * | 1945-12-28 | 1949-05-24 | Standard Oil Dev Co | Recovery of hydrocarbon oil |
US2524859A (en) * | 1946-07-30 | 1950-10-10 | Foster Wheeler Corp | Treatment of rock asphalt, oil shales, and like material |
US2772209A (en) * | 1953-07-01 | 1956-11-27 | Exxon Research Engineering Co | Recovery of oil from bituminous sands |
US3068167A (en) * | 1959-11-16 | 1962-12-11 | Cities Service Res & Dev Co | Screen separation of tar sand |
US4130474A (en) * | 1974-04-21 | 1978-12-19 | Shoilco, Inc. | Low-temperature oil shale and tar sand extraction process |
CA1162899A (en) * | 1981-02-11 | 1984-02-28 | Jan Kruyer | Rotative grizzly for oil sand separation |
US4533460A (en) * | 1984-09-14 | 1985-08-06 | Union Oil Company Of California | Oil shale extraction process |
US4695373A (en) * | 1985-01-23 | 1987-09-22 | Union Oil Company Of California | Extraction of hydrocarbon-containing solids |
US4798668A (en) * | 1986-01-31 | 1989-01-17 | Union Oil Company Of California | Extraction of hydrocarbon-containing solids |
US5091076A (en) * | 1989-11-09 | 1992-02-25 | Amoco Corporation | Acid treatment of kerogen-agglomerated oil shale |
-
1918
- 1918-03-28 US US225344A patent/US1327572A/en not_active Expired - Lifetime
-
1919
- 1919-07-09 FR FR501524A patent/FR501524A/en not_active Expired
- 1919-07-16 GB GB17777/19A patent/GB129992A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US1327572A (en) | 1920-01-06 |
FR501524A (en) | 1920-04-16 |
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