US2397859A - Liquid fuel and method of producing same - Google Patents

Liquid fuel and method of producing same Download PDF

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Publication number
US2397859A
US2397859A US479951A US47995143A US2397859A US 2397859 A US2397859 A US 2397859A US 479951 A US479951 A US 479951A US 47995143 A US47995143 A US 47995143A US 2397859 A US2397859 A US 2397859A
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United States
Prior art keywords
oil
fuel
hydrocarbon
acid
finely divided
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US479951A
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Arthur B Hersberger
Kenneth M Thompson
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Atlantic Richfield Co
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Atlantic Refining Co
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Priority to US479951A priority Critical patent/US2397859A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/32Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/322Coal-oil suspensions

Definitions

  • coal or the like in a fine state of division is suspended inhydrecarbon oil, and such suspension is stabilized b the incorporation of a small amount of an acidic compound such as an organic or inorganic acid or derivative thereof.
  • an acidic compound such as an organic or inorganic acid or derivative thereof.
  • oleum, or sulfur trioxide may also be ,utillud as stabilizing agents.
  • the quantity of acid stabilizer used may range from about 0.1% to 5% based upon the total composite fuel produced. quantities and thereafter incorporating this mixture in hydrocarbon' oil of the nature of fuel oil,
  • bituminous materials which may be uti-- of the orderv of 0.5% to 1.5% being preferred.
  • the pulverizing of the bituminous material and the addition of the acid stabilizer thereto may be carried out in a suitable apparatus such as of coal or petroleum.
  • the hydrocarbon oils a grinder or ball mill or Raymond mill, and the which may be employed as the liquid mediav are exemplified by relatively high boiling distillates of crackedor uncracked petroleum, oal tar, petroleum tar, residues from the polymerization of hydrocarbon gases and oils, oils or oil fractions from the destructive hydrogenation of coal or petroleum, and heavy residual oils from the refining of petroleum.
  • the bituminous materials are pulverized to pass 100 mesh, and preferably 200 mesh, it having been found that the finer the state of division, the more readily. the suspension is stabilized.
  • the proportion of pulverized bitu-" minous material to oil may vary from-about 10% to 60% by weight of the oil, a ratio of 40 parts may also be produced by first distributing the stabilizer in the oil and thereafter incorporating the finely divided bituminous material, or by admixing the bituminous material, stabilizer, and oil simultaneously.
  • a ratio of 40 parts may also be produced by first distributing the stabilizer in the oil and thereafter incorporating the finely divided bituminous material, or by admixing the bituminous material, stabilizer, and oil simultaneously.
  • the methodflrstde scribed above is Preferred.
  • bituminous material to parts ofoil being 40 preferred.
  • the stabilizing agents which may be employed include sulfuric acid of from to con-.- centration, a concentration of, from 93% to 98% being preferred.
  • Spent sulfuricacid from the treatment of hydrocarbon oils which has been Our invention maybe further illustrated bythe followingexamples, which, however, are not to be construed as limiting the scope thereof.
  • the acid stabilizing agent was distributed uniformly through the pulverized coal 45 by thorough milling in a ball mill. The resultin recovered and reconcentrated may be used, as
  • the sludge orsludge acids may the sludge orsludge acids in which the sulfuric acid has-a concentration of'at least 80%.
  • the stability of the composite fuel was determined bypermitting samples to stand in a quiescent. state and noting the number of days required to obtain settlement of 30% of the coal initially incorporated in the oil.
  • this stabilizer is preferred since it is relatively inexpensive and readily available.
  • a method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil which consists in incorporating a small quantityof petroleum sulfuric acid sludge in said finely.
  • a method of producing a stable suspension offinely divided bituminous fuel in hydrocarbon oil which consists in intimately mixing said finely divided bituminous fuel with said hydrocarbon oil and from 0.5 per centto 1.5 per cent of an acid from the group consisting of sulfuric acid, bydro-' carbon sulfonic acids, and phosphoric acid to stabilize said fuel in said oil.
  • a method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil which consists in incorporating a small quan- 3.
  • a liquid fuel consisting of a sulfuric acidstabilized suspension of finely divided bituminous fuel in hydrocarbon oil.
  • 4.'A liquid fuel consisting of a suspension of finely divided bituminous fuel in hydrocarbon oil and a small quantity of sulfuric acid sufficient to stabilize said suspension.
  • a liquid fuel consisting of a suspension of finely divided coal in hydrocarbon oil and from 0.1% to 5% of sulfuric acid incorporated in said suspension.
  • a liquid fuel consisting of a suspension of. finely divided coal in hydrocarbon oil and from 0.5% to 1.5% of sulfuric acid incorporated in said suspension.
  • a liquid fuel consisting of asuspension of finely divided bituminous fuel in hydrocarbon oil, 6
  • a method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil which consists in incorporating a small quantityof acid from the group consisting of sulfuric acid, hydrocarbon sulfonic acids, and phosphoric acid in said hydrocarbon oil, and dispersing said finely divided bituminous fuel in said hydrocarbon oil.
  • a method of producing .a stable suspension of finely divided bituminous fuelin hydrocarbon oil which consists in .pulverizing saidfuelin the presence of a small quantity of an acid from the group consisting of sulfuric acid, hydrocarbon sulfonic acids, and phosphoric acid, and dispersing said finely divided bituminous fuel-in-hydrocarbon oil.
  • a method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil which consists in incorporatinga small quantity of sulfuric. acid in said finely divided bitu- 16.
  • a liquid fuel consisting of a suspension of finely divided coal in hydrocarbon oil and from 0.1% to 5% of a petroleum sulfuric acid sludge incorporated in'said suspension.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

' medium.
I Patented Apr. 1946 I UNITED STATES PATENT OFFICE 2,397,859 mourn rum. Ami sm'rnon or raonncmo Arthur B. Bersbei-ger, Drexel Hill, and Kenneth M. Thompson, Aidan, Pa., asslgnors Atlantic Refining Company, Philadelphia, 7a., a corporation of Pennsylvania No Drawing. Application March 20,1943,
Serial No. 479,951
in the manufacture of composite fuel from coal and oil, such fuel being of the type in which coal or other bituminous material, in a fine state of division, is maintained in suspension in an oil In accordance with the presentinventiom coal or the like in a fine state of division is suspended inhydrecarbon oil, and such suspension is stabilized b the incorporation of a small amount of an acidic compound such as an organic or inorganic acid or derivative thereof. In producing the suspension, it has been found that most satisfactory resultsare obtained by pulverizing the coal or other bituminous material in the presence of a small amount of the acidic stabilizing agent,
Cl. 44-51) used in the polymerization of hydrocarbons "such as gaseous oleflns, or which has been useddn the alkylation of isoparamns with olefins or aromatics with olenns,-and which ma contain hydrocarbon sulfates or phosphates may be suitably employed in accordance with this invention. Organic sulfohicacids or sulfuric acid sludges containing sulfonic acids resulting from the treatment of hydrocarbon oils with sulfuric acid,-
oleum, or sulfur trioxide may also be ,utillud as stabilizing agents. The quantity of acid stabilizer used may range from about 0.1% to 5% based upon the total composite fuel produced. quantities and thereafter incorporating this mixture in hydrocarbon' oil of the nature of fuel oil,
' The bituminous materials which may be uti-- of the orderv of 0.5% to 1.5% being preferred.
In producing the suspension of bituminous material in oil, we have found that most satisfactory results are obtained by adding to the bituminous material during the pulverizing operation, the desired quantity of acid stabilizer so that such m stabilizer may be thoroughly distributed in and over the surfaces of the bituminous particles.
-' The pulverizing of the bituminous material and the addition of the acid stabilizer thereto may be carried out in a suitable apparatus such as of coal or petroleum. The hydrocarbon oils a grinder or ball mill or Raymond mill, and the which may be employed as the liquid mediav are exemplified by relatively high boiling distillates of crackedor uncracked petroleum, oal tar, petroleum tar, residues from the polymerization of hydrocarbon gases and oils, oils or oil fractions from the destructive hydrogenation of coal or petroleum, and heavy residual oils from the refining of petroleum. The bituminous materials are pulverized to pass 100 mesh, and preferably 200 mesh, it having been found that the finer the state of division, the more readily. the suspension is stabilized. The proportion of pulverized bitu-" minous material to oil may vary from-about 10% to 60% by weight of the oil, a ratio of 40 parts may also be produced by first distributing the stabilizer in the oil and thereafter incorporating the finely divided bituminous material, or by admixing the bituminous material, stabilizer, and oil simultaneously. However, the methodflrstde scribed aboveis Preferred.
of bituminous material to parts ofoil being 40 preferred. y
The stabilizing agents which may be employed include sulfuric acid of from to con-.- centration, a concentration of, from 93% to 98% being preferred. Spent sulfuricacid from the treatment of hydrocarbon oils which has been Our invention maybe further illustrated bythe followingexamples, which, however, are not to be construed as limiting the scope thereof. In these examples, the acid stabilizing agent was distributed uniformly through the pulverized coal 45 by thorough milling in a ball mill. The resultin recovered and reconcentrated may be used, as
may the sludge orsludge acids in which the sulfuric acid has-a concentration of'at least 80%.
mixture was dispersed in a hydrocarbon fuel oil having a Furol viscosity of 56 seconds at 122' F. and an A. P. I. gravity of 14'. by feeding the mixture into the oil with vigorous agitation until Sulfuric acid or phosphoric acid which has been so a homogeneous suspension was obtained. A puland the amount of acid stabilizer used was based of sulfuric acid, hydrocarbon sulfonic acids, and
phosphoric acid.
upon the total compositefuel, i. ,e., coal plus oil.
The stability of the composite fuel was determined bypermitting samples to stand in a quiescent. state and noting the number of days required to obtain settlement of 30% of the coal initially incorporated in the oil.
' Stability Coal Weight,
mam Acid stabilizer percent Tem O Days 150/200 None"-.. 77 7. 5 150/200 Sulionic acids from gas Oil acid sludge 1. 77 12. 150/200 Sulfuric acid (98% conc.) 1. 0 77 65. 0 200/250 None 120 4. 5 200/250 Sulfonic acids from gas oil acid sludge 0. 5 120 9.0 200/250 Diiso ropyl benzene sulion c acids 0. 5 120 25.0 200/250 Sulfuric acid sludge from manufacture of medicinal white oil 1. 5 120 62. 0 200/250 Sulfuric acid (98% conc.) 0. 5 120 I 34. 5 200/250 ----do l. 5 120 68. 0
tration, and this stabilizer is preferred since it is relatively inexpensive and readily available.
We claim: f 1. A method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil, which consists in incorporating a small quantity of a-sulfonic acid in said finely divided bituminuous fuel, and dispersing'said fuel-in hydrocarbon oil. v
= 2. A method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil, which consists in incorporating a small quantityof petroleum sulfuric acid sludge in said finely.
divided bituminous fuel, anddispersing said fuel in hydrocarbon oil.
8. A'method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil,
which consists in intimately mixing said finely divided bituminous fuel with said hydrocarbon oil and a small but sufilcient quantity of an acid from the group consisting of sulfuric acid, hydrocarbon divided bituminous fuel with said hydrocarbon 10. A method of producing a stable suspension offinely divided bituminous fuel in hydrocarbon oil, which consists in intimately mixing said finely divided bituminous fuel with said hydrocarbon oil and from 0.5 per centto 1.5 per cent of an acid from the group consisting of sulfuric acid, bydro-' carbon sulfonic acids, and phosphoric acid to stabilize said fuel in said oil.
11. A method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil, which consists in incorporating a small quan- 3. A liquid fuel consisting of a sulfuric acidstabilized suspension of finely divided bituminous fuel in hydrocarbon oil. 4.'A liquid fuel consisting of a suspension of finely divided bituminous fuel in hydrocarbon oil and a small quantity of sulfuric acid sufficient to stabilize said suspension.
- 5. A liquid fuel consisting of a suspension of finely divided coal in hydrocarbon oil and from 0.1% to 5% of sulfuric acid incorporated in said suspension.
6. A liquid fuel consisting of a suspension of. finely divided coal in hydrocarbon oil and from 0.5% to 1.5% of sulfuric acid incorporated in said suspension.
7. A liquid fuel consisting of asuspension of finely divided bituminous fuel in hydrocarbon oil, 6
tity of an acid from the group consisting of sulfuric acid, hydrocarbon sulfonic acids, and phosphoric acid in said finely divided bituminous fuel. 'and dispersing said fuel in hydrocarbon oil.
' 12. A method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil, which consists in incorporating a small quantityof acid from the group consisting of sulfuric acid, hydrocarbon sulfonic acids, and phosphoric acid in said hydrocarbon oil, and dispersing said finely divided bituminous fuel in said hydrocarbon oil.
.13. A method of producing .a stable suspension of finely divided bituminous fuelin hydrocarbon oil, which consists in .pulverizing saidfuelin the presence of a small quantity of an acid from the group consisting of sulfuric acid, hydrocarbon sulfonic acids, and phosphoric acid, and dispersing said finely divided bituminous fuel-in-hydrocarbon oil.
14. A method of producing a stable suspension of finely divided bituminous fuel in hydrocarbon oil, which consists in incorporatinga small quantity of sulfuric. acid in said finely divided bitu- 16. A liquid fuel consisting of a suspension of finely divided coal in hydrocarbon oil and from 0.1% to 5% of a petroleum sulfuric acid sludge incorporated in'said suspension.
ARTHUR B. 'HERSHBERGER. KENNETH M. THOMPSON.
US479951A 1943-03-20 1943-03-20 Liquid fuel and method of producing same Expired - Lifetime US2397859A (en)

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Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2913469A (en) * 1956-08-07 1959-11-17 Nat Lead Co Organotitanium compounds and process of preparation
US3907134A (en) * 1974-02-27 1975-09-23 Carbonoyl Company Water-free liquid fuel slurry and method of producing same
US3961913A (en) * 1974-03-29 1976-06-08 Combustion Equipment Associates, Inc. Process for treating organic wastes and product thereof
JPS5347405A (en) * 1976-10-13 1978-04-27 Nippon Oil & Fats Co Ltd Dispersed fuel composition
US4101293A (en) * 1977-03-30 1978-07-18 Reichhold Chemicals, Inc. Stabilizing emulsifiers
JPS5411910A (en) * 1977-06-30 1979-01-29 Nippon Oil & Fats Co Ltd Production of dispersed fuel
US4149855A (en) * 1978-06-08 1979-04-17 Suntech, Inc. Stabilized coal-oil slurry and process
US4149854A (en) * 1978-06-08 1979-04-17 Suntech, Inc. Stabilized coal-oil slurry and process
JPS5474806A (en) * 1977-11-29 1979-06-15 Lion Corp Dispersing agent of coal in oil
JPS5474805A (en) * 1977-11-29 1979-06-15 Lion Corp Dispersing agent containing aliphatic alcohol for finely pulverized coal in oil
US4187078A (en) * 1976-10-13 1980-02-05 Nippon Oil And Fats Company, Limited Coal dispersing oil
US4195975A (en) * 1978-04-17 1980-04-01 Dai-Ich Kogyo Seiyaku Co., Ltd. Stabilized fuel slurry
US4288232A (en) * 1979-12-19 1981-09-08 Basf Wyandotte Corporation Ester containing fuel composition
US4304573A (en) * 1980-01-22 1981-12-08 Gulf & Western Industries, Inc. Process of beneficiating coal and product
US4358293A (en) * 1981-01-29 1982-11-09 Gulf & Western Manufacturing Co. Coal-aqueous mixtures
JPS5891796A (en) * 1982-08-13 1983-05-31 Nippon Oil & Fats Co Ltd Dispersed fuel composition
US4406664A (en) * 1980-01-22 1983-09-27 Gulf & Western Industries, Inc. Process for the enhanced separation of impurities from coal and coal products produced therefrom
JPS5951985A (en) * 1983-07-28 1984-03-26 Dai Ichi Kogyo Seiyaku Co Ltd Additive for mixture of slack coal and oil
US4526585A (en) * 1981-05-28 1985-07-02 The Standard Oil Company Beneficiated coal, coal mixtures and processes for the production thereof
US4536372A (en) * 1980-01-22 1985-08-20 The Standard Oil Company Apparatus for beneficiating coal
US4564369A (en) * 1981-05-28 1986-01-14 The Standard Oil Company Apparatus for the enhanced separation of impurities from coal
US4583990A (en) * 1981-01-29 1986-04-22 The Standard Oil Company Method for the beneficiation of low rank coal
US4623359A (en) * 1984-08-20 1986-11-18 Texaco Inc. Aqueous slurries of solid carbonaceous fuel
US20080148626A1 (en) * 2006-12-20 2008-06-26 Diamond Qc Technologies Inc. Multiple polydispersed fuel emulsion
US20100043277A1 (en) * 2006-12-18 2010-02-25 Diamond Qc Technologies Inc. Polydispersed composite emulsions

Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2913469A (en) * 1956-08-07 1959-11-17 Nat Lead Co Organotitanium compounds and process of preparation
US3907134A (en) * 1974-02-27 1975-09-23 Carbonoyl Company Water-free liquid fuel slurry and method of producing same
US3961913A (en) * 1974-03-29 1976-06-08 Combustion Equipment Associates, Inc. Process for treating organic wastes and product thereof
US4187078A (en) * 1976-10-13 1980-02-05 Nippon Oil And Fats Company, Limited Coal dispersing oil
JPS5347405A (en) * 1976-10-13 1978-04-27 Nippon Oil & Fats Co Ltd Dispersed fuel composition
JPS5543034B2 (en) * 1976-10-13 1980-11-04
US4101293A (en) * 1977-03-30 1978-07-18 Reichhold Chemicals, Inc. Stabilizing emulsifiers
JPS5411910A (en) * 1977-06-30 1979-01-29 Nippon Oil & Fats Co Ltd Production of dispersed fuel
JPS6035959B2 (en) * 1977-06-30 1985-08-17 日本油脂株式会社 Dispersed fuel manufacturing method
JPS5474806A (en) * 1977-11-29 1979-06-15 Lion Corp Dispersing agent of coal in oil
JPS5474805A (en) * 1977-11-29 1979-06-15 Lion Corp Dispersing agent containing aliphatic alcohol for finely pulverized coal in oil
JPS5543035B2 (en) * 1977-11-29 1980-11-04
JPS5543036B2 (en) * 1977-11-29 1980-11-04
US4195975A (en) * 1978-04-17 1980-04-01 Dai-Ich Kogyo Seiyaku Co., Ltd. Stabilized fuel slurry
US4149854A (en) * 1978-06-08 1979-04-17 Suntech, Inc. Stabilized coal-oil slurry and process
US4149855A (en) * 1978-06-08 1979-04-17 Suntech, Inc. Stabilized coal-oil slurry and process
US4288232A (en) * 1979-12-19 1981-09-08 Basf Wyandotte Corporation Ester containing fuel composition
US4304573A (en) * 1980-01-22 1981-12-08 Gulf & Western Industries, Inc. Process of beneficiating coal and product
US4406664A (en) * 1980-01-22 1983-09-27 Gulf & Western Industries, Inc. Process for the enhanced separation of impurities from coal and coal products produced therefrom
US4412843A (en) * 1980-01-22 1983-11-01 Gulf & Western Industries, Inc. Beneficiated coal, coal mixtures and processes for the production thereof
US4536372A (en) * 1980-01-22 1985-08-20 The Standard Oil Company Apparatus for beneficiating coal
US4358293A (en) * 1981-01-29 1982-11-09 Gulf & Western Manufacturing Co. Coal-aqueous mixtures
US4583990A (en) * 1981-01-29 1986-04-22 The Standard Oil Company Method for the beneficiation of low rank coal
US4564369A (en) * 1981-05-28 1986-01-14 The Standard Oil Company Apparatus for the enhanced separation of impurities from coal
US4526585A (en) * 1981-05-28 1985-07-02 The Standard Oil Company Beneficiated coal, coal mixtures and processes for the production thereof
JPS6010074B2 (en) * 1982-08-13 1985-03-14 日本油脂株式会社 Dispersed fuel composition
JPS5891796A (en) * 1982-08-13 1983-05-31 Nippon Oil & Fats Co Ltd Dispersed fuel composition
JPS6027718B2 (en) * 1983-07-28 1985-07-01 第一工業製薬株式会社 Additive for pulverized coal-oil mixture
JPS5951985A (en) * 1983-07-28 1984-03-26 Dai Ichi Kogyo Seiyaku Co Ltd Additive for mixture of slack coal and oil
US4623359A (en) * 1984-08-20 1986-11-18 Texaco Inc. Aqueous slurries of solid carbonaceous fuel
US20100043277A1 (en) * 2006-12-18 2010-02-25 Diamond Qc Technologies Inc. Polydispersed composite emulsions
US20080148626A1 (en) * 2006-12-20 2008-06-26 Diamond Qc Technologies Inc. Multiple polydispersed fuel emulsion

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