US1704956A - Process for treating oil shale - Google Patents

Process for treating oil shale Download PDF

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US1704956A
US1704956A US735355A US73535524A US1704956A US 1704956 A US1704956 A US 1704956A US 735355 A US735355 A US 735355A US 73535524 A US73535524 A US 73535524A US 1704956 A US1704956 A US 1704956A
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shale
spent
preheater
oil shale
treating oil
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US735355A
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Milon J Trumble
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/06Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of oil shale and/or or bituminous rocks
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S208/00Mineral oils: processes and products
    • Y10S208/951Solid feed treatment with a gas other than air, hydrogen or steam

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  • My invention relates to the art of treating oil shale, and is particularly applicable to the destructive distillation of oil shale by means of superheated steam.
  • the annexed drawing is a diagrammatic representation partly in section of an apparatus adapted to carry on my process.
  • this apparatus I employ a preheater 1 which is placed in a spent shale receiver 2 and which is adapted to deliver shale into a retort 3.
  • a dephlegmator 4 and a primary condenser 5 are provided, also a suction fan 6 and a secondary condenser 7.
  • the preheater 1 consists of a tight shell 11 having a perforated top 12 and a discharge spout 13.
  • the spent shale receiver surrounds t 1e preheater and consists of a shell 21 having a filling neck 22 (hereinafter referred to as means for charging) closed by a cover 23.
  • a discharge spout 24 (hereinafter referred to as means for delivering shale from said heater to said retort) extends downwardly and is closed by a cover 25.
  • Walls forming an air preheating cham ber 26 surround the spout 24,-the admission 4 of air tothe chamber 26 being controlled by a valve 27. Air is taken from the top of the air chamber 26 through a plurality of pipes 28 and is discharged into the spent shale receiver through slots 29, in the pipes 28.
  • the retort 3 is provided with a filling neck 31 closed by a cover 32 and with a discharge spout 33 provided with a cover 34.
  • the discharge spout 33 is so placed that it can readily discharge into a skip 35 which can be elevated as by a chain or rope 35 connected with a bail 35 to discharge into the filling neck 22 of the spent shale receiver 21 (and which is hereinafter referred to as means for delivering spent shale .from said preheater to said retort).
  • the same skip (preferably provided with a fairly tight cover, not shown,to smother any flames spontaneously produced by momentary exposure of the hot spent shale, preferably handled above its ignition point, to the air) can be used to fill the preheater 1, if desired.
  • the covers 32 and 34 can be made pressuretight and superheated steam maybe discharged into the interior of the retort 3 vided with an inlet pipe 61 which extends from and connects to the discharge spout 13 of the preheater 1, vapors being discharged from the pipe 6 into the condenser .7, which 1s of any standard type ofconstruction.
  • the apparatus being charged with shale the covers 32 and 34 are closed and superheated steam is delivered through the nozzle 36 into the mass of shale in the retort 3.
  • the steam is preferably at or above 1000 degrees Fahrenheit and it acts upon the shale to raise it to a comparatively high temperature and to drive off the volatiles therethrough, these volatiles passing through the pipe 38 to the dephlegmator 4, and through the pipe 43 to the condenser 5.
  • the condensates produced is one of the commercial products ofthe plant.
  • the plate 17 prevents shale from clogging the openings 39 inthe perforated top 12.
  • the spent shale at a high tempora ture completely surrounds the preheater 1 andtends to produce a preliminary distillation therein.
  • Air being delivered through the valves 27 to the air heating chamber" 26 is "then injected into the spent shale in the spent shale receiver 2, through the openings 29 in the pipe 28.
  • $pent shale ordinarily contains considerable quantities of free carbon or tar
  • a combustion is set i up. which further elevates the temperature of the spent shale and serves to heat the preheater 1.
  • the gases of'combustion are also .drawn under the plate 17 and through the openings 39, downwardly through the raw shale in the preheater 1, by means of the pump 6 and the pipe 61. During the passage of the hot vapors through the shale, considerable distillations take place therefrom,
  • my invention comv lprises the novel conception of utilizing the ot spent shale to preheat the raw shale before subjecting it to distillation in the retort 3. It also provides a novel conception' of accomplishing this preheating partly by ing the raw shale by passing hot spent shale in heat exchanging relationship, but out of contact with a body of the raw shale; distilling a body of the preheated shale by contacting therewith high] superheated steam; recovering volatile'pro ucts thus produced;

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

Man-ch12, 1929 J, UM L 1,704,956
PROCESS FOR TREATING OIL SHADE I Filed Sept. 1924 GOA/0544555.
A94- w 44-4 r511- Smse 1/44 [XI/W701? M4 04 J. 790M545" Mam/:2.
Patented Mar. 12, 1929.
UNITED STATES IILON J. TRUM'BLE, H LOS ANGELES, CALIFORNIA.
rnocnss r011 TREATING on. SHALE.
Application filed September 2, 1924' Serial No. 735,355.
My invention relates to the art of treating oil shale, and is particularly applicable to the destructive distillation of oil shale by means of superheated steam. v I
It is a well known fact that oil shale, in its natural state, contains substances which can .be Converted into-volatile hydrocarbons by the application of heatand pressure. It is an ob- 'ect of-my invention to provide an. apparatus y which this conversion can be accomplished.
Further objects and advantages of the mvcntion will be made evident hereinafter.
The annexed drawing is a diagrammatic representation partly in section of an apparatus adapted to carry on my process. In this apparatus I employ a preheater 1 which is placed in a spent shale receiver 2 and which is adapted to deliver shale into a retort 3. A dephlegmator 4 and a primary condenser 5 are provided, also a suction fan 6 and a secondary condenser 7.
In the form of apparatus shown, the preheater 1 consists of a tight shell 11 having a perforated top 12 and a discharge spout 13. A
filling neck 14 (hereinafter referred to as means for charging) is provided with a cover 15 and the discharge spout 13 is provided with a cover 16. A shield 17 is placed above the perforations in the to '12. The spent shale receiver surrounds t 1e preheater and consists of a shell 21 having a filling neck 22 (hereinafter referred to as means for charging) closed by a cover 23. A discharge spout 24 (hereinafter referred to as means for delivering shale from said heater to said retort) extends downwardly and is closed by a cover 25. Walls forming an air preheating cham ber 26 surround the spout 24,-the admission 4 of air tothe chamber 26 being controlled by a valve 27. Air is taken from the top of the air chamber 26 through a plurality of pipes 28 and is discharged into the spent shale receiver through slots 29, in the pipes 28.
' The retort 3 is provided with a filling neck 31 closed by a cover 32 and with a discharge spout 33 provided with a cover 34. The discharge spout 33 is so placed that it can readily discharge into a skip 35 which can be elevated as by a chain or rope 35 connected with a bail 35 to discharge into the filling neck 22 of the spent shale receiver 21 (and which is hereinafter referred to as means for delivering spent shale .from said preheater to said retort). The same skip (preferably provided with a fairly tight cover, not shown,to smother any flames spontaneously produced by momentary exposure of the hot spent shale, preferably handled above its ignition point, to the air) can be used to fill the preheater 1, if desired. The covers 32 and 34 can be made pressuretight and superheated steam maybe discharged into the interior of the retort 3 vided with an inlet pipe 61 which extends from and connects to the discharge spout 13 of the preheater 1, vapors being discharged from the pipe 6 into the condenser .7, which 1s of any standard type ofconstruction.
The method of operation of my invention is as follows:
The apparatus being charged with shale, the covers 32 and 34 are closed and superheated steam is delivered through the nozzle 36 into the mass of shale in the retort 3. The steam is preferably at or above 1000 degrees Fahrenheit and it acts upon the shale to raise it to a comparatively high temperature and to drive off the volatiles therethrough, these volatiles passing through the pipe 38 to the dephlegmator 4, and through the pipe 43 to the condenser 5. The condensates produced is one of the commercial products ofthe plant.
The preheater 1, being filled with raw shale, is given a preliminar treatment by means of hot spent shale in t e spent. shale receiver 2, the spent shale receiver having been charged by means of the skip 35 from the retort 3. The plate 17 prevents shale from clogging the openings 39 inthe perforated top 12. The spent shale at a high tempora ture completely surrounds the preheater 1 andtends to produce a preliminary distillation therein. Air being delivered through the valves 27 to the air heating chamber" 26 is "then injected into the spent shale in the spent shale receiver 2, through the openings 29 in the pipe 28. v
$pent shale ordinarily contains considerable quantities of free carbon or tar, and
p by the injection of air, a combustion is set i up. which further elevates the temperature of the spent shale and serves to heat the preheater 1. The gases of'combustion are also .drawn under the plate 17 and through the openings 39, downwardly through the raw shale in the preheater 1, by means of the pump 6 and the pipe 61. During the passage of the hot vapors through the shale, considerable distillations take place therefrom,
the products being condensed in the condenser 7.
It will be noted that my invention comv lprises the novel conception of utilizing the ot spent shale to preheat the raw shale before subjecting it to distillation in the retort 3. It also provides a novel conception' of accomplishing this preheating partly by ing the raw shale by passing hot spent shale in heat exchanging relationship, but out of contact with a body of the raw shale; distilling a body of the preheated shale by contacting therewith high] superheated steam; recovering volatile'pro ucts thus produced;
shale during the maintenance of the men, tioned heat exchanging relationship.
2. In the destructive distillation of oil shale, a process which comprises: preheating the raw shale by passing hot spent shale and burning residual carbon from said spent in heat-exchanging relationship, but out of contact with a body of the raw shale; dis" tilling a body of the preheated shale by contacting therewith highly superheated steam;
recovering volatile products thus produced;
and burning residual carbon from said spent shale during the maintenance of the mentioned heat exchanging relationship and pass- 5 ing the resultant roducts through said raw s ale.
In testimony whereof, I have hereunto set of combustion my hand at'Los Angeles, California, this 26th day of August, 1924.
MILON J. TRUMBLE.
US735355A 1924-09-02 1924-09-02 Process for treating oil shale Expired - Lifetime US1704956A (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434815A (en) * 1943-10-30 1948-01-20 Union Oil Co Method and apparatus for educting oil from oil shale by use of superheated steam
US2441386A (en) * 1943-10-30 1948-05-11 Union Oil Co Method and apparatus for educting oil from shale by utilizing hot spent shale
US2466593A (en) * 1944-01-17 1949-04-05 Union Oil Co Multiple stage shale eduction process
US2534051A (en) * 1946-11-22 1950-12-12 Standard Oil Dev Co Method for fluidized low-temperature carbonization of coal
US2550432A (en) * 1944-08-10 1951-04-24 Standard Oil Dev Co Process for recovery of hydrocarbon oil from shale
US2622059A (en) * 1948-02-28 1952-12-16 Consolidation Coal Co Low-temperature carbonization of coal
US2689212A (en) * 1946-02-19 1954-09-14 Svenska Maskinverken Ab Process and device for destructive distillation
US2697688A (en) * 1949-11-30 1954-12-21 Standard Oil Dev Co Distillation of oil-bearing minerals
US2725347A (en) * 1952-08-29 1955-11-29 Universal Oil Prod Co Process and apparatus for distilling solid carbonaceous materials
US2768937A (en) * 1952-05-08 1956-10-30 Henry F H Wigton Distillation of volatile matters of carbonaceous materials
US4060479A (en) * 1974-10-21 1977-11-29 Eduardo Da Costa Barcellos Process for obtaining oil, gas, sulfur and other products from oil shale
US20070180770A1 (en) * 2005-07-28 2007-08-09 Flory Edward C Integrated tilt/sash lock assembly

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434815A (en) * 1943-10-30 1948-01-20 Union Oil Co Method and apparatus for educting oil from oil shale by use of superheated steam
US2441386A (en) * 1943-10-30 1948-05-11 Union Oil Co Method and apparatus for educting oil from shale by utilizing hot spent shale
US2466593A (en) * 1944-01-17 1949-04-05 Union Oil Co Multiple stage shale eduction process
US2550432A (en) * 1944-08-10 1951-04-24 Standard Oil Dev Co Process for recovery of hydrocarbon oil from shale
US2689212A (en) * 1946-02-19 1954-09-14 Svenska Maskinverken Ab Process and device for destructive distillation
US2534051A (en) * 1946-11-22 1950-12-12 Standard Oil Dev Co Method for fluidized low-temperature carbonization of coal
US2622059A (en) * 1948-02-28 1952-12-16 Consolidation Coal Co Low-temperature carbonization of coal
US2697688A (en) * 1949-11-30 1954-12-21 Standard Oil Dev Co Distillation of oil-bearing minerals
US2768937A (en) * 1952-05-08 1956-10-30 Henry F H Wigton Distillation of volatile matters of carbonaceous materials
US2725347A (en) * 1952-08-29 1955-11-29 Universal Oil Prod Co Process and apparatus for distilling solid carbonaceous materials
US4060479A (en) * 1974-10-21 1977-11-29 Eduardo Da Costa Barcellos Process for obtaining oil, gas, sulfur and other products from oil shale
US20070180770A1 (en) * 2005-07-28 2007-08-09 Flory Edward C Integrated tilt/sash lock assembly

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