GB510110A - Improvements in and relating to catalysts for use in cracking hydrocarbons - Google Patents

Improvements in and relating to catalysts for use in cracking hydrocarbons

Info

Publication number
GB510110A
GB510110A GB19332/38A GB1933238A GB510110A GB 510110 A GB510110 A GB 510110A GB 19332/38 A GB19332/38 A GB 19332/38A GB 1933238 A GB1933238 A GB 1933238A GB 510110 A GB510110 A GB 510110A
Authority
GB
United Kingdom
Prior art keywords
catalysts
hydrocarbon
catalyst
conversion
pills
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
Application number
GB19332/38A
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 Development Co
Original Assignee
Standard Oil Development Co
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 Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB510110A publication Critical patent/GB510110A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04Oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • B01J37/0018Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)

Landscapes

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

Abstract

510,110. Catalysts for cracking oils. STANDARD OIL DEVELOPMENT CO. June 29, 1938, No. 19332. Convention date, Oct. 22, 1937. [Classes 1 (i) and 32] Catalysts, for the conversion of high-boiling hydrocarbons into lower boiling hydrocarbons suitable as motor fuels of high octane number, such as Fuller's earth, bentonites, zeolites &c., are prepared by mixing the finely divided catalytic material with a small amount of a finely divided 'solid polycyclic hydrocarbon, e.g., anthracene or naphthalene, moistening the mass with a small amount of water, moulding into small compact masses, e.g., pills, pellets, tablets &c., and then heating, prior to their use as catalysts, to a temperature sufficient to boil off the hydrocarbon without leaving any decomposition products on the catalyst. The catalyst and hydrocarbon may be mixed in the proportion of 1-20 parts hydrocarbon to 99-90 parts of clay, increased pressure in the moulding operation requiring a greater proportion of hydrocarbon. Preferably, the mixture is formed into 10-12 mm. pills which are reground to 10 mesh and reformed into 4 mm. pills. The conversion process is carried out at about 850‹F and the catalyst is regenerated by oxidation ; the catalyst prepared as above requires a shorter time for regeneration. Examples describe the conversion of a West Texas gas oil using catalysts prepared as above, showing the yield in successive cycles, and also the conversion and regeneration times. Comparison is made between such catalysts and compressed catalysts not made with such hydrocarbons.
GB19332/38A 1937-10-22 1938-06-29 Improvements in and relating to catalysts for use in cracking hydrocarbons Expired GB510110A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US510110XA 1937-10-22 1937-10-22

Publications (1)

Publication Number Publication Date
GB510110A true GB510110A (en) 1939-07-27

Family

ID=21968818

Family Applications (1)

Application Number Title Priority Date Filing Date
GB19332/38A Expired GB510110A (en) 1937-10-22 1938-06-29 Improvements in and relating to catalysts for use in cracking hydrocarbons

Country Status (1)

Country Link
GB (1) GB510110A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2460811A (en) * 1944-08-26 1949-02-08 Shell Dev Process for preparing pellfted ironoxide type catalysts

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2460811A (en) * 1944-08-26 1949-02-08 Shell Dev Process for preparing pellfted ironoxide type catalysts

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