US2287511A - Asphalt manufacture - Google Patents

Asphalt manufacture Download PDF

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Publication number
US2287511A
US2287511A US197680A US19768038A US2287511A US 2287511 A US2287511 A US 2287511A US 197680 A US197680 A US 197680A US 19768038 A US19768038 A US 19768038A US 2287511 A US2287511 A US 2287511A
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United States
Prior art keywords
air
asphalt
penetration
temperature
blowing
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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 - Lifetime
Application number
US197680A
Inventor
Robert E Burk
Charles H Whitacre
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Co
Original Assignee
Standard Oil Co
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Filing date
Publication date
Priority claimed from US112348A external-priority patent/US2179208A/en
Application filed by Standard Oil Co filed Critical Standard Oil Co
Priority to US197680A priority Critical patent/US2287511A/en
Application granted granted Critical
Publication of US2287511A publication Critical patent/US2287511A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C3/00Working-up pitch, asphalt, bitumen
    • C10C3/02Working-up pitch, asphalt, bitumen by chemical means reaction
    • C10C3/023Working-up pitch, asphalt, bitumen by chemical means reaction with inorganic compounds

Definitions

  • the stock to be worked up, a heavy petroleum oil residue, which we designate the residuum, is in accordance with the invention heated with air, and a small or catalytic-amount of a polymerizing catalyst.
  • the temperature of treatment may be 225-450 F. Desirably, the material is suitably stirred or agitated.
  • the time of treatment is short, as for instance 20 to 300 minutes.
  • catalysts we employ halides, as ferric chloride, aluminum bromide, aluminum chloride, aluminum iodide, halides similarly of copper, tin, zinc, antimony, arsenic, boron, titanium, etc., hydroxides of sodium, potassium, etc., calcium oxides, sodium carbonate, metallic sodium, in small amounts.
  • Particularly desirable catalysts are the halides of aluminum, copper, tin, zinc, antimony, arsenic, titanium, boron fluoride, etc.
  • the petroleum residuum first to an air-blowing, maintaining the temperature at about 450 F. for about 600 minutes, the material being agitated by the injected air or other suitable means, and then the air-blowing is discontinued and the polymerizing catalyst is incorporated, e. g. 0.5 per cent AlCls at a temperature of about 250 F. and the heating is maintained at 300400 F. for 20 to 30 minutes.
  • Such air-blowing stage can be operated to some desired penetration standard, as for instance 92 penetration at 77 F., and then the polymerization treatment is applied.
  • the product has a penetration of at 77 F. and ductility 16 at 39 F. and 72.5 at 77 F.
  • a petroleum residuum is air-blown first, and then is heated with 0.9 per cent of boron fluoride in a BF3 ether mixture at a temperature of 400 F. for 15 minutes.
  • the product has a melting point of 140 F., ductility at 38 F. 4, and at 77 F. 21, penetration at 32 F, 19, and at 77 F. 47, and at 115 F. 146, and a susceptibility coefficient of 2.
  • the petroleum residuum is similarly first air-blown as above, and then is heated with 0.5 per cent of FeClz at 400 F. for 30 minutes.
  • the product has a melting point of F., ductility at 39 F. 4, and at 77 F. 30, penetration at 32 F. 17, and at 77 F. 51, and at 115 F. 192, and susceptibility factor 3.4.
  • Asphalts produced according to the present invention have particularly shiny black surfaces, and are not buttery or short in consistency as has been the characteristic of high melting point asphalts from blended stocks. They also have higher melting points at a given penetration, say 77 F., than a customary asphalt, and better susceptibility coefficients.
  • a process of making asphalt which comprises heating with temperature rise to 350-400 F. and thickening a petroleum residuum in the absence of injected air to asphalt-consistency with a small amount of an aluminum chloride catalyst.
  • a process of making asphalt which comprises air-blowing a petroleum residuum in the absence of an added catalyst, then thickening the material in the absence of injected air to asphalt-consistency by heating with temperature rise to 350-400 F. with a small amount of a halide of aluminum.
  • a process of making asphalt which comprises air-blowing a petroleum residuum in the absence ofan added catalyst, then in the absence of injected air thickening the material to asphalt-consistency by heating with temperature rise to 350-400 F. with a small amount of an aluminum chloride catalyst.

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Working-Up Tar And Pitch (AREA)

Description

Patented June 23, 1942 ASPHALT MANUFACTURE Robert E. Burk and Charles H. Whitacre, Cleveland, Ohio, assignors to The Standard Oil Qompany, Cleveland, Ohio, a corporation of Ohio No Drawing. Original application November 23,
1936, Serial No. 112,348. Divided and this application March 23, 1938, Serial No. 197,680
3 Claims.
In manufacturing asphalt, it has been the custom to blow the petroleum residuum with air, and maintain the temperature at about 300-500 F. The procedure is very tedious, requiring a long duration of action in order to bring the material to useable characteristics of high melting point and low penetration. Although enormous quantities of oxygen are brought into relation with the hydrocarbon material, there is not a great increase in the oxy gen content, and the action is largely a dehydrogenation and conjoining of hydrocarbon molecules. We have now found that particularly effective action in thickening up the material todesirable penetration and melting point can be obtained without the cumbersome and time-consuming air-blowing, and the entire operating can be completed in a fraction of the time heretofore necessary, the products being also superior.
To the accomplishment of the foregoing and related ends, the invention, then comprises the features hereinafter fully described, and particularly pointed out in the claims, the following description setting forth in detail certain illustrative embodiments of the invention, these being indicative however, of but a few of the various ways in which the principle of the invention may be employed.
The stock to be worked up, a heavy petroleum oil residue, which we designate the residuum, is in accordance with the invention heated with air, and a small or catalytic-amount of a polymerizing catalyst. The temperature of treatment may be 225-450 F. Desirably, the material is suitably stirred or agitated. The time of treatment is short, as for instance 20 to 300 minutes. As catalysts, we employ halides, as ferric chloride, aluminum bromide, aluminum chloride, aluminum iodide, halides similarly of copper, tin, zinc, antimony, arsenic, boron, titanium, etc., hydroxides of sodium, potassium, etc., calcium oxides, sodium carbonate, metallic sodium, in small amounts. Particularly desirable catalysts are the halides of aluminum, copper, tin, zinc, antimony, arsenic, titanium, boron fluoride, etc.
In some instances, it is desirable to subject the petroleum residuum first to an air-blowing, maintaining the temperature at about 450 F. for about 600 minutes, the material being agitated by the injected air or other suitable means, and then the air-blowing is discontinued and the polymerizing catalyst is incorporated, e. g. 0.5 per cent AlCls at a temperature of about 250 F. and the heating is maintained at 300400 F. for 20 to 30 minutes. Such air-blowing stage can be operated to some desired penetration standard, as for instance 92 penetration at 77 F., and then the polymerization treatment is applied.
As an example: A petroleum residuum having initially a penetration of 200 at 77 F., is heated with 1.5 per cent of ferric chloride at a temperature of 350 F., for 60 minutes. The product has a penetration of at 77 F. and ductility 16 at 39 F. and 72.5 at 77 F.
As another example: A petroleum residuum is air-blown first, and then is heated with 0.9 per cent of boron fluoride in a BF3 ether mixture at a temperature of 400 F. for 15 minutes. The product has a melting point of 140 F., ductility at 38 F. 4, and at 77 F. 21, penetration at 32 F, 19, and at 77 F. 47, and at 115 F. 146, and a susceptibility coefficient of 2.
As another example: The petroleum residuum is similarly first air-blown as above, and then is heated with 0.5 per cent of FeClz at 400 F. for 30 minutes. The product has a melting point of F., ductility at 39 F. 4, and at 77 F. 30, penetration at 32 F. 17, and at 77 F. 51, and at 115 F. 192, and susceptibility factor 3.4.
Asphalts produced according to the present invention have particularly shiny black surfaces, and are not buttery or short in consistency as has been the characteristic of high melting point asphalts from blended stocks. They also have higher melting points at a given penetration, say 77 F., than a customary asphalt, and better susceptibility coefficients.
This application is a division of our application Ser. No. 112,348, filed Nov. 23, 1936 Other modes of applying the principle of the invention may be employed, change being made as regards the details described, provided the features stated in any of the following claims, or the equivalent of such, be employed.
We therefore particularly point out and distinctly claim as our invention:
1. A process of making asphalt, which comprises heating with temperature rise to 350-400 F. and thickening a petroleum residuum in the absence of injected air to asphalt-consistency with a small amount of an aluminum chloride catalyst.
2. A process of making asphalt, which comprises air-blowing a petroleum residuum in the absence of an added catalyst, then thickening the material in the absence of injected air to asphalt-consistency by heating with temperature rise to 350-400 F. with a small amount of a halide of aluminum.
3. A process of making asphalt, which comprises air-blowing a petroleum residuum in the absence ofan added catalyst, then in the absence of injected air thickening the material to asphalt-consistency by heating with temperature rise to 350-400 F. with a small amount of an aluminum chloride catalyst.
ROBERT E. BURK. CHARLES H. WHITACRE.
US197680A 1936-11-23 1938-03-23 Asphalt manufacture Expired - Lifetime US2287511A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US197680A US2287511A (en) 1936-11-23 1938-03-23 Asphalt manufacture

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US112348A US2179208A (en) 1936-11-23 1936-11-23 Manufacture of improved asphalts
US197680A US2287511A (en) 1936-11-23 1938-03-23 Asphalt manufacture

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US2287511A true US2287511A (en) 1942-06-23

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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2478654A (en) * 1944-10-27 1949-08-09 Louvroil Montbard Aulnoye Plastic bituminous material and method of making the same
US2776932A (en) * 1953-05-06 1957-01-08 Standard Oil Co Process for oxidizing asphalts
US3093610A (en) * 1959-12-04 1963-06-11 Lubrizol Corp Asphaltic products
US3258418A (en) * 1963-03-21 1966-06-28 Phillips Petroleum Co Production of high penetration and high softening point asphalt
US3373101A (en) * 1964-01-24 1968-03-12 Union Oil Co Friedel-crafts catalyst plus bitumen to produce pitch of increased beta resin content
US4202755A (en) * 1978-11-03 1980-05-13 Witco Chemical Corp. Catalytic method for making pitch
EP0053041A2 (en) * 1980-11-24 1982-06-02 Ashland Oil, Inc. Processes for producing high grade asphaltic materials from low grade bituminous materials and products resulting therefrom
US4456524A (en) * 1982-04-02 1984-06-26 Ashland Oil, Inc. Process for enhancing catalytic response of asphalt oxidation catalyst
US4456523A (en) * 1980-11-24 1984-06-26 Ashland Oil, Inc. Processes for producing high grade asphaltic materials from low grade bituminous materials and products resulting therefrom
US4639307A (en) * 1984-08-31 1987-01-27 Chevron Research Company Method for producing industrial asphalts
US4659389A (en) * 1984-02-16 1987-04-21 Ashland Oil, Inc. Method and composition of asphaltic roofing fluxes
US4931163A (en) * 1985-10-04 1990-06-05 Osaka Gas Co, Ltd. Pitch fluoride
US5611910A (en) * 1995-06-02 1997-03-18 Owens-Corning Fiberglas Technology, Inc. Method for reducing sulfur emissions in processing air-blown asphalt
WO1997029168A1 (en) * 1996-02-12 1997-08-14 Owens Corning Method for reducing sulfur-oxide emissions from an asphalt air-blowing process
US8901211B2 (en) 2011-05-27 2014-12-02 Building Materials Investment Corporation Preparation of industrial asphalt
US10633540B2 (en) 2016-10-13 2020-04-28 Building Materials Investment Corporation Preparation of blown polymer modified asphalt
US11053391B2 (en) 2016-10-06 2021-07-06 Building Materials Investment Corporation Polymer modified asphalt for industrial applications

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2478654A (en) * 1944-10-27 1949-08-09 Louvroil Montbard Aulnoye Plastic bituminous material and method of making the same
US2776932A (en) * 1953-05-06 1957-01-08 Standard Oil Co Process for oxidizing asphalts
US3093610A (en) * 1959-12-04 1963-06-11 Lubrizol Corp Asphaltic products
US3258418A (en) * 1963-03-21 1966-06-28 Phillips Petroleum Co Production of high penetration and high softening point asphalt
US3373101A (en) * 1964-01-24 1968-03-12 Union Oil Co Friedel-crafts catalyst plus bitumen to produce pitch of increased beta resin content
US4202755A (en) * 1978-11-03 1980-05-13 Witco Chemical Corp. Catalytic method for making pitch
EP0053041A2 (en) * 1980-11-24 1982-06-02 Ashland Oil, Inc. Processes for producing high grade asphaltic materials from low grade bituminous materials and products resulting therefrom
EP0053041A3 (en) * 1980-11-24 1982-08-04 Ashland Oil, Inc. Processes for producing high grade asphaltic materials from low grade bituminous materials and products resulting therefrom
US4456523A (en) * 1980-11-24 1984-06-26 Ashland Oil, Inc. Processes for producing high grade asphaltic materials from low grade bituminous materials and products resulting therefrom
US4456524A (en) * 1982-04-02 1984-06-26 Ashland Oil, Inc. Process for enhancing catalytic response of asphalt oxidation catalyst
US4659389A (en) * 1984-02-16 1987-04-21 Ashland Oil, Inc. Method and composition of asphaltic roofing fluxes
US4639307A (en) * 1984-08-31 1987-01-27 Chevron Research Company Method for producing industrial asphalts
US4931163A (en) * 1985-10-04 1990-06-05 Osaka Gas Co, Ltd. Pitch fluoride
US5611910A (en) * 1995-06-02 1997-03-18 Owens-Corning Fiberglas Technology, Inc. Method for reducing sulfur emissions in processing air-blown asphalt
US6383464B1 (en) 1995-06-02 2002-05-07 Owens Corning Fiberglas Technology, Inc. Method for reducing sulfur-oxide emissions from an asphalt air-blowing process
WO1997029168A1 (en) * 1996-02-12 1997-08-14 Owens Corning Method for reducing sulfur-oxide emissions from an asphalt air-blowing process
US8901211B2 (en) 2011-05-27 2014-12-02 Building Materials Investment Corporation Preparation of industrial asphalt
US9493654B2 (en) 2011-05-27 2016-11-15 Building Materials Investment Corporation Preparation of industrial asphalt
US11053391B2 (en) 2016-10-06 2021-07-06 Building Materials Investment Corporation Polymer modified asphalt for industrial applications
US12077668B2 (en) 2016-10-06 2024-09-03 Bmic Llc Polymer modified asphalt for industrial applications
US10633540B2 (en) 2016-10-13 2020-04-28 Building Materials Investment Corporation Preparation of blown polymer modified asphalt

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