US1673491A - Process of cracking mineral crude oils - Google Patents

Process of cracking mineral crude oils Download PDF

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Publication number
US1673491A
US1673491A US192494A US19249427A US1673491A US 1673491 A US1673491 A US 1673491A US 192494 A US192494 A US 192494A US 19249427 A US19249427 A US 19249427A US 1673491 A US1673491 A US 1673491A
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US
United States
Prior art keywords
cracking
crude oils
mineral crude
cracking mineral
aluminum
Prior art date
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
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US192494A
Inventor
Jr Henry Blumenberg
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.)
A M BULEY
Original Assignee
A M BULEY
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by A M BULEY filed Critical A M BULEY
Priority to US192494A priority Critical patent/US1673491A/en
Application granted granted Critical
Publication of US1673491A publication Critical patent/US1673491A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/08—Halides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used

Definitions

  • HENRI BLUMENBERG an, or MOAPA, NEVADA, nssrenon TO A. IBULEY, or Los ANGELES, CALIFORNIA.
  • PROCESS 0 CRAGKING' MINERAL CRUDE OILS.
  • My invention relates to a process of cracking mineral crude oils to produce a lngh yield of motor fuel, using aluminum chloro sulphate (AlClSOQ as a catalyzingagent.
  • AlClSOQ aluminum chloro sulphate
  • a The aluminum chloro sulphate is superior to aluminumchloride now largely used for this purpose for the reason that it is less expensive and but slightly hygroscopic while aluminum chloride is intensely so.
  • a process of cracking crude mineral oils comprising adding aluminum' chloro sulphate to crude mineral oil, heating the Oll to cracking temperature, distilling the oil; and condensing the distillate.
  • a process of cracking crude mineral oils comprising adding aluminum .chloro sulphate from 2 to 5 percent by weighttc crude mineral oil, .heatingthe oil to crack ing temperature, distilling the oil, and con densing the distillate.

Description

Patented June 12, 1 928.
. UNITED STATES PATENT OFFICE.
HENRI BLUMENBERG, an, or MOAPA, NEVADA, nssrenon TO A. IBULEY, or Los ANGELES, CALIFORNIA. i
PROCESS 0] CRAGKING' MINERAL CRUDE OILS.
Io Drawing.
My invention relates to a process of cracking mineral crude oils to produce a lngh yield of motor fuel, using aluminum chloro sulphate (AlClSOQ as a catalyzingagent. a The aluminum chloro sulphate is superior to aluminumchloride now largely used for this purpose for the reason that it is less expensive and but slightly hygroscopic while aluminum chloride is intensely so.
My invention consists in the steps and process hereinafter described and claimed.
I add from two (2) to. five (5) percent of aluminum chloro sulphate, by weight, to
the crude mineral oil to be cracked, the
Application filed May 18,
1927. Serial No. 192,494..
and fractionating of the same to produce motor fuel.
The yield of the motor fuel or gasoline obtained in my cracking process compares favorably with those using aluminum chloride. I
Various changes may be made in the steps ofthe process Without departing from the splrit of my invention as claimed. I
I claim:
1. A process of cracking crude mineral oils comprising adding aluminum' chloro sulphate to crude mineral oil, heating the Oll to cracking temperature, distilling the oil; and condensing the distillate.
2. A process of cracking crude mineral oils comprising adding aluminum .chloro sulphate from 2 to 5 percent by weighttc crude mineral oil, .heatingthe oil to crack ing temperature, distilling the oil, and con densing the distillate.
In testimony whereof I have signed name to this specification.
nanny BLUMENBERG, JR.
US192494A 1927-05-18 1927-05-18 Process of cracking mineral crude oils Expired - Lifetime US1673491A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US192494A US1673491A (en) 1927-05-18 1927-05-18 Process of cracking mineral crude oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US192494A US1673491A (en) 1927-05-18 1927-05-18 Process of cracking mineral crude oils

Publications (1)

Publication Number Publication Date
US1673491A true US1673491A (en) 1928-06-12

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US192494A Expired - Lifetime US1673491A (en) 1927-05-18 1927-05-18 Process of cracking mineral crude oils

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