US2665238A - Recovery of oil from shale - Google Patents

Recovery of oil from shale Download PDF

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Publication number
US2665238A
US2665238A US236478A US23647851A US2665238A US 2665238 A US2665238 A US 2665238A US 236478 A US236478 A US 236478A US 23647851 A US23647851 A US 23647851A US 2665238 A US2665238 A US 2665238A
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United States
Prior art keywords
shale
oil
kerogen
water
temperature
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Expired - Lifetime
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US236478A
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James K Truitt
George B Arnold
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Texaco Inc
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Texaco Inc
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Priority to US236478A priority Critical patent/US2665238A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation

Definitions

  • This invention relates to the recovery of oil from oil shale and contemplates the digestion of lump shale with water under elevated temperatures and high pressures.
  • the treatment with the water reduces the shale to a soft clay consistency. It is preferable to have the shale crushed to relatively small sizes.
  • crushed shale containing maximum sizes of about 1 or 2 inches has been successfully processed with digestion periods not exceeding about six hours.
  • the method of recovering oil from oil shale containing kerogen comprises charging to a retort feed materials consisting of the shale and water in large amount approximating the weight of the shale and subjecting the material in the retort to a temperature in excess of 500 F. under a pressure in excess of 1000 lbs. per square inch to thereby effect the decomposition of the kerogen and resultant formation of oil.
  • the method of recovering oil from oil shale containing kerogen that comprises charging to a retort feed materials consisting of the shale and water in large amount approximating the weight of the shale and subjecting the material in the retort to a temperature of the order of 700 F. under a pressure of the order of 3000 lbs. per square inch to thereby effect the decomposition of the kerogen and resultant formation of oil.

Description

Patented Jan. 5, 1954 RECOVERY OF OIL FROM SHALE James K. Truitt, Wappingers Falls, and George B. Arnold, Glenham, N. Y., assignors to The Texas Company, New York, N. Y., a corporation of Delaware No Drawing. Application July 12, 1951, Serial No. 236,478
2 Claims. 1
This invention relates to the recovery of oil from oil shale and contemplates the digestion of lump shale with water under elevated temperatures and high pressures.
We have discovered that by digesting the shale with water under high temperatures and high super-atmospheric pressures the kerogen is resolved and displaced by the water. The temperature and pressure conditions to efiect resolution of the kerogen vary somewhat with the character of the shale, but in general pressures of the order of 3000 lbs. and temperatures approximating 700 F. are required to effect a substantially complete resolution of the kerogen and recovery of the oil content of the shale.
At temperatures around 500 F. and, pressures of about 1000 lbs. the water has little or no effect in resolving the kerogen but as the temperature is increased above 500 F. and as the pressure is increased above 1000 lbs, the effect of the water in resolving the kerogen becomes noticeable. The amount of oil recovered increases generally as the temperature or pressure is further increased, but pressures as high as about 3000 p. s. i. g. and temperatures at least approximating as high as 700 F. are required to effect a substantially complete recovery of the oil.
The effect of the temperature and pressure is well shown by a series of typical runs in which the oil shale was subjected to a variety of temperature-pressure conditions. The shale for these runs was crushed shale composed of material of which the largest sizes approximated A; of an inch and of smaller material including dust. The shale in each run was digested with approximately equal weight of water in a closed bomb for a period of six hours. The following table gives the temperature-pressure conditions and the recoveries of oil obtained in these particular runs:
It will be seen that while material oil recoveries were obtained under the lower temperaturepressure conditions that only run 1, which was under the most severe conditions of temperature and pressure, accomplished a sufliciently high yield of recovered oil to be considered suitable for commercial operations. In determining the data for the carbon contained in the solid residue the treated shale was extracted with benzene and then dried.
The treatment with the water reduces the shale to a soft clay consistency. It is preferable to have the shale crushed to relatively small sizes.
in order to facilitate complete penetration and displacement by the water. In our process crushed shale containing maximum sizes of about 1 or 2 inches has been successfully processed with digestion periods not exceeding about six hours.
Although a preferred embodiment of the invention has been described herein, it will be understood that various changes and modifications may be made therein, while securing to a greater or less extent some or all of the benefits of the invention, without departing from the spirit and scope thereof.
We claim:
1. The method of recovering oil from oil shale containing kerogen that comprises charging to a retort feed materials consisting of the shale and water in large amount approximating the weight of the shale and subjecting the material in the retort to a temperature in excess of 500 F. under a pressure in excess of 1000 lbs. per square inch to thereby effect the decomposition of the kerogen and resultant formation of oil.
2. The method of recovering oil from oil shale containing kerogen that comprises charging to a retort feed materials consisting of the shale and water in large amount approximating the weight of the shale and subjecting the material in the retort to a temperature of the order of 700 F. under a pressure of the order of 3000 lbs. per square inch to thereby effect the decomposition of the kerogen and resultant formation of oil.
JAMES K. TRUITT. GEORGE E. ARNOLD.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,486,243 I-Iackstaff Mar. 11, 1924 1,497,607 Streppel June 10, 1924 1,520,752 Horwitz Dec. 30, 1924 1,904,477 Krauch et a1. Apr. 18, 1933 1,936,819 Bayer Nov. 28, 1933

Claims (1)

1. THE METHOD OF RECOVERING OIL FROM OIL SHALE CONTAINING KEROGEN THAT COMPRISES CHARGING TO A RETORT FEED MATERIALS CONSISTING OF THE SHALE AND WATER IN LARGE AMOUNT APPROXIMATING THE WEIGHT OF THE SHALE AND SUBJECTING THE MATERIAL IN THE RETORT TO A TEMPERATURE IN EXCESS OF 500* F. UNDER A PRESSURE IN EXCESS OF 1000 LBS. PER SQUARE INCH TO THEREBY EFFECT THE DECOMPOSITION OF THE KEROGEN AND RESULTANT FORMATION OF OIL.
US236478A 1951-07-12 1951-07-12 Recovery of oil from shale Expired - Lifetime US2665238A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3051644A (en) * 1959-07-01 1962-08-28 Texaco Inc Method for recovering oil from oil shale
US3960702A (en) * 1974-08-08 1976-06-01 Marathon Oil Company Vapor phase water process for retorting oil shale
US4005005A (en) * 1974-05-31 1977-01-25 Standard Oil Company (Indiana) Process for recovering and upgrading hydrocarbons from tar sands
US4108760A (en) * 1974-07-25 1978-08-22 Coal Industry (Patents) Limited Extraction of oil shales and tar sands
US4161428A (en) * 1976-10-06 1979-07-17 Kraftwerk Union Aktiengesellschaft Device for recovering oil products from oil sands
US4557820A (en) * 1984-05-24 1985-12-10 The Standard Oil Company Conversion of high boiling organic materials to low boiling materials
US4559127A (en) * 1984-05-24 1985-12-17 The Standard Oil Company Conversion of high boiling organic materials to low boiling materials
WO1988002285A1 (en) * 1986-10-03 1988-04-07 Still Otto Gmbh Process for treating contaminated earth
US4840725A (en) * 1987-06-19 1989-06-20 The Standard Oil Company Conversion of high boiling liquid organic materials to lower boiling materials
WO2013070312A1 (en) * 2011-11-08 2013-05-16 Exxonmobil Upstream Research Company Processing a hydrocarbon stream using supercritical water

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1486243A (en) * 1920-04-19 1924-03-11 George C Hackstaff Process for treatment of oil shale and apparatus therefor
US1497607A (en) * 1920-06-30 1924-06-10 Firm Deutsche Erdol Ag Separating of oil from sand
US1520752A (en) * 1920-02-27 1924-12-30 Horwitz Wilhelm Process for the recovery of petroleum
US1904477A (en) * 1927-01-13 1933-04-18 Ig Farbenindustrie Ag Production of valuable organic products
US1936819A (en) * 1928-10-03 1933-11-28 Uhde Gmbh Friedrich Production of liquid products from solid or liquid carbonaceous materials

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1520752A (en) * 1920-02-27 1924-12-30 Horwitz Wilhelm Process for the recovery of petroleum
US1486243A (en) * 1920-04-19 1924-03-11 George C Hackstaff Process for treatment of oil shale and apparatus therefor
US1497607A (en) * 1920-06-30 1924-06-10 Firm Deutsche Erdol Ag Separating of oil from sand
US1904477A (en) * 1927-01-13 1933-04-18 Ig Farbenindustrie Ag Production of valuable organic products
US1936819A (en) * 1928-10-03 1933-11-28 Uhde Gmbh Friedrich Production of liquid products from solid or liquid carbonaceous materials

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3051644A (en) * 1959-07-01 1962-08-28 Texaco Inc Method for recovering oil from oil shale
US4005005A (en) * 1974-05-31 1977-01-25 Standard Oil Company (Indiana) Process for recovering and upgrading hydrocarbons from tar sands
US4108760A (en) * 1974-07-25 1978-08-22 Coal Industry (Patents) Limited Extraction of oil shales and tar sands
US3960702A (en) * 1974-08-08 1976-06-01 Marathon Oil Company Vapor phase water process for retorting oil shale
US4161428A (en) * 1976-10-06 1979-07-17 Kraftwerk Union Aktiengesellschaft Device for recovering oil products from oil sands
US4557820A (en) * 1984-05-24 1985-12-10 The Standard Oil Company Conversion of high boiling organic materials to low boiling materials
US4559127A (en) * 1984-05-24 1985-12-17 The Standard Oil Company Conversion of high boiling organic materials to low boiling materials
WO1988002285A1 (en) * 1986-10-03 1988-04-07 Still Otto Gmbh Process for treating contaminated earth
US4840725A (en) * 1987-06-19 1989-06-20 The Standard Oil Company Conversion of high boiling liquid organic materials to lower boiling materials
WO2013070312A1 (en) * 2011-11-08 2013-05-16 Exxonmobil Upstream Research Company Processing a hydrocarbon stream using supercritical water
US9505989B2 (en) 2011-11-08 2016-11-29 Exxonmobil Upstream Research Company Processing a hydrocarbon stream using supercritical water

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