US1500323A - Oil-shale extraction process - Google Patents

Oil-shale extraction process Download PDF

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US1500323A
US1500323A US468844A US46884421A US1500323A US 1500323 A US1500323 A US 1500323A US 468844 A US468844 A US 468844A US 46884421 A US46884421 A US 46884421A US 1500323 A US1500323 A US 1500323A
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retort
oil
shale
crude material
extraction process
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US468844A
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Robert W Jenkins
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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 .particularly to the process of distilling or extracting oil from ore or shale of 'an oil bearing nature.
  • An object of this invention is toprovide adequate means land methods' of controlling the temperatures necessary to extract or distill the maximum possible quantity of the desired commodity from the crude material.
  • a further object of this invention is to provide an ap aratus, for use 'with my process, that wil re aries a smaller initial outlay, cost less to mamtain than other apparatuses of a similar nature, that may be operated more ly and eifectively, minimize labor costs and also successfully handle sufiicient quantities' of crude material to yield the desired hydrocarbon commodity in suflicient quantities.
  • a further object is to provide a retort in which the process of my invention may bev carried on, having means therein for admitting the crude material, receiving the distilled product therefrom, carrying away vthe residue of the crude material and with escape ports forv relieving excessive pressures
  • igure 1 represents a diagranimatic side elevation of an apparatus adapted to be. used in the operation with my improved extraction process. i i
  • Figure 2 represents a side view through Figure 1 on line 2-2.
  • the construction illustrated in the drawings comprises a cylindrical retort or furnace generally designated by the numeral 1, formed from metal or other desirable material adapted to reasonably resist i-the deleterious effects of heat.
  • the retort 1 consists of a cylindrical body portion and of an enlarged cylindrical end portion 2 thereon concentric therewith.
  • the axis of the retort' is inclined so that the enlarged portion 2 thereof lies in close proximity to the ground or surface upon which rests the standards or frame work for supporting the said retort.
  • the exterior ofthe retort is encased with heat resisting material such as magnesia covering, asbestos or the like, to
  • Supports 3 and 4 are mounted adj acent the cylindrical. portion 1 of the retort, and a support 5 adjacent the enlarged end 2 thereof, although it would be clearly within the purview lof this invention to rearrange the supporting means shown or to vary Vthe method of supporting the retort.
  • Eachbof the supports 3, 4 and 5 are providedwith spaced, bearlng members 7 thereon between which a roller or sp'ool member 8 is rotatably mounted, and which is adapted to receive and support ⁇ annular projections 9, 10 and 11 respectively, fixed on the retort.
  • the rollers 8 ha've clepres'sed ⁇ center portions 12 and flanged ends 13 and 14.
  • a suitable gear 15 is mounted circumferentially about the retort 1 and meshes with a gear 16, fixed on a shaft 17, having the ends thereof in the bearings formed in the supports 3 and 4.
  • the shaft 17 is provided with a pulley 18 thereon connected by a belt or other suitable media to'a source of energy for rotating the same.
  • the upper end of the retort 1 is closed by a fixed cover 19 secured to a standard 21 and has a circumferentially beaded edge therearound, engaging a peripheral fiange 20 provided on the end of the retort 1.
  • the cover 19 has a ooncentric opening therein through which a substantially cylindrical casing 22 is adapted to project, the opposite end of said casing. communicating jwith aV hopper 23 adapted to Vcontain the crude material, oil bearing shale or ore.
  • Casing 22 has a suitable screw feed shaft 24 rotatably' mounted therein and supported in bearings 25 and 26 respectively at its opposite ends.
  • a pulley l27 may be used for the purpose of imparting rotative movement to the screw feed and thus progressively conveying raw material or the oil bearing shale from the hopper 23 through the casing 22 and into the retort 1.
  • the casing 22 is slightly enlarged throughout its length for the purpose to be hereinafter describedV in detail, and is also covered without with asbestos or other heat resisting material.
  • the cover 19 is also provided with a door or fly-lid 26 ivotally mounted thereon and normally aapted to remain closed and efi'ectively vseal of the interior of the retort from the atmosphere.
  • the enlarged end 2 of the ret rt isf'lined in the interior with fire-'brick or ther refractory heat resisting material, inasmuch as the destructive action occurring by directly contacting the oil bearing ore with the flame of the heating medium, takes place in the enlarged chamber 2, it becomes necessary to provide effective and lasting protection for theinterior of the retort.
  • the lower end of ⁇ the retort 2 is closed by a cover member 28,
  • peripheral flangd edge thereon over-lapping an annular lip 30 on the retort to provide substantially an airtight joint therewith.
  • the lower end of the cover 28 has 'a chute 31 extending therefrom into which ash or the dbris remaining after the ore has des- Leooaa troyed, may be discharged.
  • A. suitable endless conveyor 32 is'provided within said chute to carry awa the ash or otherwise dispose of it.
  • the caslng 2 is provided with a door 33 pivoted thereon closing an opening 34 in said casing. This dooi ⁇ or fly-lid 33 is provided for the purpose of relieving any sudden increases of pressure occurring within the retort 'occasioned by a premature combustion of the hydrocarbon vapors or gases Within the retort.
  • the cover 28 is also provided With an opening-therein through which the nozzle of an oil burner 35v projects, ⁇ said oil burning apparatus being used for the purpose of heating the interior of the retort andapplying the flamethereof in direct contact to the ore or crude material from which oil is to be distilled or extracted.
  • A-steam /smother line 38 projects through the said cover into the linterior oftheretort for co- Operating With the oil burner in increasing the temperature Within the retort and thus aiding in heating the shale or crude material and hastening the distillation.
  • This invention operatesl as follows:
  • the crude material or oil bearing shale ' is placed withinthe hopper 23 andthe screw feed 24 rotated suificiently to advance predetermined quantities of the material into the upper end of the lretort 1.
  • the oil burner would be started and the gasified fuel delivered therefrom lighted to produce a flame.
  • the pulley, 18 would be rotated and through the inter-meshing gears 15 and 16, commence revolving the retort.
  • the screw feed would then be continued in its rotation, advancing the crude material or oil bearing shale into the upper end of the retort.
  • the degree of inclination of the revolving retort is such that the material would gradually work its way toward the lowest point and would be continually agitated and turned so as to permit all parts thereof to be thoroughly heatedu
  • the ore passes into the enlarged end of the retort, it would come in direct contact with the flame of the oil burner, tending to thoroughly destroy the structure of the crude material and to drive off, distil or extract the desired commodity contained therein.
  • steam be introduced with the flame of the oil burner, thereby tending to raise the temperature of the crude material to the desired point where the hydrocarbon vapors would be given off.
  • the continuedtrevolving of thev retort would gradually pass the crude material to the lowermost edge thereof in the form of an ash or dbris which would be removed from the retort by the ash conveyor 32 or otherwise disposed of.
  • suitable condenser the condenser pipe 40is connected vwith a or undue e vacuum pump 43 used to exha'ust the -interior of the retort of its vapors of distillation and 'otherwise create a suction through the screw feed casing 22 and into'the-condenser.
  • The'vapors of distillation in passing from the retort is partially-cooled by contact with the incoming crude material and with the walls of the casing 22, somewhat smplifying the work of the 'condenser.
  • the vapor is cooled or otherwise collected in the condenser aforementioned after which it is conveyedfto suitable receiving tanks or other ready means Whereby it may be disposed of.

Description

July 8, 1924.
R. W. JENKINS OIL SHALE EXTRACTION PROCESS Filed May 12, 192] Patented July 8, 1924. i
UNITED s'rA'rEs ROBERT W. JENKINS, OF RICHMOND, CALIFORNIA..
OIL-SHALE EXTRACTION PROCESS.
Appucafin med my 12,
To all who'm, z't 'ma-y concem:
Be it known that I, ROBERT W..JENKINs, a citizen of the United States, and a resident of the city of Richmond, county of Contra Costa, State of California, have made a new and useful invention to Wit, Improvements in an Oil-Shale Extraction Process; and I do hereby declare the following to be a full, clear, concise, and exact description of the same.
This invention relates .particularly to the process of distilling or extracting oil from ore or shale of 'an oil bearing nature.
An object of this invention is toprovide adequate means land methods' of controlling the temperatures necessary to extract or distill the maximum possible quantity of the desired commodity from the crude material.
A further object of this invention is to provide an ap aratus, for use 'with my process, that wil re uire a smaller initial outlay, cost less to mamtain than other apparatuses of a similar nature, that may be operated more eficiently and eifectively, minimize labor costs and also successfully handle sufiicient quantities' of crude material to yield the desired hydrocarbon commodity in suflicient quantities.
A further object is to provide a retort in which the process of my invention may bev carried on, having means therein for admitting the crude material, receiving the distilled product therefrom, carrying away vthe residue of the crude material and with escape ports forv relieving excessive pressures Other objects and advantages, will apear as this description progresses. In this specification and the annexed drawing, the invention is illustrated in the form considered 'to be the best, but it is to be understood that the invention is not limited to such form, because it may be embodied in otherforms, and it is also to be understood that in and by the claims following the description, it is desired to cover the invention in whatsoever form it may be embodied.
In the accompanying one-sheet of drawin s,
igure 1 represents a diagranimatic side elevation of an apparatus adapted to be. used in the operation with my improved extraction process. i i
Figure 2 represents a side view through Figure 1 on line 2-2.
Various apparatuses and processes have 1921. srial No. 468,844.
been constructed for treating ore of the same character as is proposed to be utilized 1n the operation of my process. Such means and apparatuses have been at their best, in-v eflicient in operation and not commercially valuable for distilling or producing the oil in paying quantities. Furthermore the older method of treating` oil bearinz,` ore or shale consisted in heating the product externally thus indirectly tending to cook the commodity and raise the temperature thereof sufliciently to drive off the desired commodity. This manner of treatment does not extract the highest percentage of the desired product from the crude material, nor is it possible to. treat quantities of material in such a short period of time necessary for efi'icient operation. My invention consists in directly contacting `theore or crude mate- .rial to be treated withthe heat of a fiame,
used in conjunction with steam, whereby the' crude material is heated much faster than where cooked by an external heat, also serving the purpose of permitting greater quantities of the crude material to betreated in much quicker time.
In detail the construction illustrated in the drawings comprises a cylindrical retort or furnace generally designated by the numeral 1, formed from metal or other desirable material adapted to reasonably resist i-the deleterious effects of heat. The retort 1 consists of a cylindrical body portion and of an enlarged cylindrical end portion 2 thereon concentric therewith. The axis of the retort' is inclined so that the enlarged portion 2 thereof lies in close proximity to the ground or surface upon which rests the standards or frame work for supporting the said retort. The exterior ofthe retort is encased with heat resisting material such as magnesia covering, asbestos or the like, to
prevent loss of heat by radiation. Supports 3 and 4 are mounted adj acent the cylindrical. portion 1 of the retort, and a support 5 adjacent the enlarged end 2 thereof, although it would be clearly within the purview lof this invention to rearrange the supporting means shown or to vary Vthe method of supporting the retort. Eachbof the supports 3, 4 and 5 are providedwith spaced, bearlng members 7 thereon between which a roller or sp'ool member 8 is rotatably mounted, and which is adapted to receive and support `annular projections 9, 10 and 11 respectively, fixed on the retort. The rollers 8 ha've clepres'sed `center portions 12 and flanged ends 13 and 14. The outer faces of theannuluses 9, 10 and 11 contact with the inner portion of the roller 8 and the retort is guarded a ainst lateral or longitudinal disalignment y the flanges 13 and 14 enga ing the sides 'of the said annuluses 9, .10 an 11. A suitable gear 15 is mounted circumferentially about the retort 1 and meshes with a gear 16, fixed on a shaft 17, having the ends thereof in the bearings formed in the supports 3 and 4. The shaft 17 is provided with a pulley 18 thereon connected by a belt or other suitable media to'a source of energy for rotating the same. The apparatus indicated for the purpose of revolving the retort is susceptible of various modifications within the scope of this invention and it is to be understood that suitable modi: fication would' be permissible.
,The upper end of the retort 1 is closed by a fixed cover 19 secured to a standard 21 and has a circumferentially beaded edge therearound, engaging a peripheral fiange 20 provided on the end of the retort 1. The cover 19 has a ooncentric opening therein through which a substantially cylindrical casing 22 is adapted to project, the opposite end of said casing. communicating jwith aV hopper 23 adapted to Vcontain the crude material, oil bearing shale or ore. Casing 22 has a suitable screw feed shaft 24 rotatably' mounted therein and supported in bearings 25 and 26 respectively at its opposite ends. A pulley l27 may be used for the purpose of imparting rotative movement to the screw feed and thus progressively conveying raw material or the oil bearing shale from the hopper 23 through the casing 22 and into the retort 1. The casing 22 is slightly enlarged throughout its length for the purpose to be hereinafter describedV in detail, and is also covered without with asbestos or other heat resisting material. The cover 19 isalso provided with a door or fly-lid 26 ivotally mounted thereon and normally aapted to remain closed and efi'ectively vseal of the interior of the retort from the atmosphere.
The enlarged end 2 of the ret rt isf'lined in the interior with fire-'brick or ther refractory heat resisting material, inasmuch as the destructive action occurring by directly contacting the oil bearing ore with the flame of the heating medium, takes place in the enlarged chamber 2, it becomes necessary to provide effective and lasting protection for theinterior of the retort. The lower end of `the retort 2 is closed by a cover member 28,
fixed relative'to said retort and also has a,
peripheral flangd edge thereon over-lapping an annular lip 30 on the retort to provide substantially an airtight joint therewith.
The lower end of the cover 28 has 'a chute 31 extending therefrom into which ash or the dbris remaining after the ore has des- Leooaa troyed, may be discharged. A. suitable endless conveyor 32 is'provided within said chute to carry awa the ash or otherwise dispose of it. The caslng 2 is provided with a door 33 pivoted thereon closing an opening 34 in said casing. This dooi` or fly-lid 33 is provided for the purpose of relieving any sudden increases of pressure occurring within the retort 'occasioned by a premature combustion of the hydrocarbon vapors or gases Within the retort. The cover 28 is also provided With an opening-therein through which the nozzle of an oil burner 35v projects,` said oil burning apparatus being used for the purpose of heating the interior of the retort andapplying the flamethereof in direct contact to the ore or crude material from which oil is to be distilled or extracted. A-steam /smother line 38 projects through the said cover into the linterior oftheretort for co- Operating With the oil burner in increasing the temperature Within the retort and thus aiding in heating the shale or crude material and hastening the distillation.
This invention operatesl as follows:
The crude material or oil bearing shale 'is placed withinthe hopper 23 andthe screw feed 24 rotated suificiently to advance predetermined quantities of the material into the upper end of the lretort 1. i Prior to advancing the crude material, the oil burner would be started and the gasified fuel delivered therefrom lighted to produce a flame. After the temperature within the retort has reached a desired degree, the pulley, 18 would be rotated and through the inter-meshing gears 15 and 16, commence revolving the retort. p The screw feed Would then be continued in its rotation, advancing the crude material or oil bearing shale into the upper end of the retort. The degree of inclination of the revolving retort is such that the material would gradually work its way toward the lowest point and would be continually agitated and turned so as to permit all parts thereof to be thoroughly heatedu As the ore passes into the enlarged end of the retort, it would come in direct contact with the flame of the oil burner, tending to thoroughly destroy the structure of the crude material and to drive off, distil or extract the desired commodity contained therein. In order to increase the efliciency of the retort it is desirable that steam be introduced with the flame of the oil burner, thereby tending to raise the temperature of the crude material to the desired point where the hydrocarbon vapors would be given off. The continuedtrevolving of thev retort would gradually pass the crude material to the lowermost edge thereof in the form of an ash or dbris which Would be removed from the retort by the ash conveyor 32 or otherwise disposed of.
The oil bearing shale or crude material when firstl'`` introduced into the retort commences to give off its hydrocarbon vapor 'gropertiea almost instantly u n being eated. As the temperature of t e shale is gradually increased,v more'and more of the oil vapor is given oif. That the vapor of 'distillation mi ht be withdrawn from the retort and 'co ected,- a. suitable condenser the condenser pipe 40is connected vwith a or undue e vacuum pump 43 used to exha'ust the -interior of the retort of its vapors of distillation and 'otherwise create a suction through the screw feed casing 22 and into'the-condenser. The'vapors of distillation in passing from the retort is partially-cooled by contact with the incoming crude material and with the walls of the casing 22, somewhat smplifying the work of the 'condenser. The vapor is cooled or otherwise collected in the condenser aforementioned after which it is conveyedfto suitable receiving tanks or other ready means Whereby it may be disposed of.
It often happens in the process of extrac- 'tion that the vapors of distillation will come in contact with the flame of the oil burner causing a premature combustion which might be disruptive to the a paratus but wlnch is counteracted by the y-lids or explosion doors at, the opposite ends of the retort; thus any Sudden pressure increases ansion of the air within the retorfl is reheved b doors to the atmosp ere. ere a premathe ning of said ture explosion takes place and a burning of the shale follows, the smothering steam from the conduit 38 tends to make the same shortlived and thus eifectively quench the fire to permit a resuming of the process of distillation.
Having thus -described this invention, What I claim and desirel to secure by Letters Patent is:
1. The herein described process of dis- *tilling oil from oil shale, comprising progressively passing predetermined quantlties of shale into a heated retort revolving said retort to advance said shale therethrough; subjecting said shale to direct contact with the flame of a heating medium. for -distillation urposes; collecting the heated oil vapors of said shale and relieving said retort of excesspressures'.
2. The herein described process of distilling 'oil from oil shale, comprising progressively passingpredetermined quantities of shale into a heated retort; revolving said retort to advance said shale therethrough; subjecting said shale to direct contact with the flame of a heating medium for distillation purposes; introducing steam into contact with said shale to aid in distillation; collecting the heated oil Vvapors of said shale and relieving said retort of excess pressures.
' In testimony Whereof, Ii have hereunto set my hand at San Francisco, California, this 14th day of'April 1921.
ROBERT W. JENKINS.
In presence of LrNcoLN V. JOHNSON.
US468844A 1921-05-12 1921-05-12 Oil-shale extraction process Expired - Lifetime US1500323A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2664389A (en) * 1949-04-01 1953-12-29 Standard Oil Dev Co Process and apparatus for the distillation of solids
US2710280A (en) * 1951-03-21 1955-06-07 Smidth & Co As F L Method and apparatus for expelling volatile constituents from solid carbonaceous fuel
US4274344A (en) * 1979-07-16 1981-06-23 Nider William K Process for carbonizing an agricultural product
US4274342A (en) * 1979-07-16 1981-06-23 Nider William K Apparatus for carbonizing an agricultural product
USD751881S1 (en) * 2011-10-11 2016-03-22 Timothy Hicks Rescue tool

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2664389A (en) * 1949-04-01 1953-12-29 Standard Oil Dev Co Process and apparatus for the distillation of solids
US2710280A (en) * 1951-03-21 1955-06-07 Smidth & Co As F L Method and apparatus for expelling volatile constituents from solid carbonaceous fuel
US4274344A (en) * 1979-07-16 1981-06-23 Nider William K Process for carbonizing an agricultural product
US4274342A (en) * 1979-07-16 1981-06-23 Nider William K Apparatus for carbonizing an agricultural product
USD751881S1 (en) * 2011-10-11 2016-03-22 Timothy Hicks Rescue tool

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