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GB992820A - Process for the hydrogenative cracking of hydrocarbon oils - Google Patents

Process for the hydrogenative cracking of hydrocarbon oils

Info

Publication number
GB992820A
GB992820A GB1309063A GB1309063A GB992820A GB 992820 A GB992820 A GB 992820A GB 1309063 A GB1309063 A GB 1309063A GB 1309063 A GB1309063 A GB 1309063A GB 992820 A GB992820 A GB 992820A
Authority
GB
United Kingdom
Prior art keywords
hydrogel
support
solution
alkali metal
catalyst
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
GB1309063A
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.)
SHELL INT RESEARCH
Shell Internationale Research Maatschappij BV
Original Assignee
SHELL INT RESEARCH
Shell Internationale Research Maatschappij BV
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 SHELL INT RESEARCH, Shell Internationale Research Maatschappij BV filed Critical SHELL INT RESEARCH
Publication of GB992820A publication Critical patent/GB992820A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • B01J37/22Halogenating
    • B01J37/26Fluorinating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02Boron or aluminium; Oxides or hydroxides thereof
    • B01J21/04Alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12Silica and alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/755Nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/78Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
    • 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
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation

Landscapes

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

Abstract

Hydrocarbon oils are cracked by contacting the oil in presence of hydrogen at elevated temperatures and pressures with a catalyst comprising fluorine preferably 0.1 to 5.0% by weight based on the catalyst and at least one metal of the iron group of the Periodic Table intimately associated with an acid acting support comprising at least one refractory oxide, the intimate association of the metal with the support having been achieved by contacting the support in hydrogel form with a solution of the said metals or metals, fluorine having been incorporated into the support while the support is in the hydrogel form. The support comprises silica and at least one of the following: alumina, magnesia, zirconia and boria. Preferably the supports comprises by weight 50% to 90% of silica and 50% to 10% alumina. The catalyst contains 0.1% to 14% by weight of the iron group metal e.g. nickel and cobalt. The catalysts may be prepared by contacting the hydrogel with a solution of the metal or metals the pH of the solution being 4 to 7. The hydrogel may be prepared by (1) mixing aqueous solutions of an alkali metal aluminate and an alkali metal silicate, adjusting the pH to 7 with mineral acid, aging and then washing the hydrogel to remove alkali metal ions; (2) adding mineral acid to an alkali metal silicate solution to adjust the pH to 2, adding an aluminium salt, adjusting the pH to 7 and washing the hydrogel formed. The hydrogel may be washed with ammonium nitrate solution to remove alkali metal ions. The fluorine is incorporated into the hydrogel by adding hydrofluoric acid or a water soluble fluoride, e.g. ammonium or sodium fluoride, to the aluminate solution used to prepare the hydrogel. The hydrogel is finally washed, dried and calcined at 427 DEG to 649 DEG C. The hydrogenation takes place at 260 DEG to 454 DEG C., 10.5 to 210 atmos. gauge, a L.H.S.V. of 0.2 to 10.0 litres of oil per hour per litre of catalyst and a hydrogen to oil mol. ratio of 5: 1 to 50: 1. The hydrocarbon feed boils above the gasoline boiling range e.g. 232 DEG to 510 DEG C. and may be pretreated by mild hydrogenation to remove coke forming constituents and to reduce the sulphur and nitrogen contents.
GB1309063A 1962-04-04 1963-04-02 Process for the hydrogenative cracking of hydrocarbon oils Expired GB992820A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US18494762A 1962-04-04 1962-04-04

Publications (1)

Publication Number Publication Date
GB992820A true GB992820A (en) 1965-05-19

Family

ID=22678962

Family Applications (2)

Application Number Title Priority Date Filing Date
GB1308963A Expired GB1007282A (en) 1962-04-04 1963-04-02 Hydrogenative cracking of hydrocarbon oils
GB1309063A Expired GB992820A (en) 1962-04-04 1963-04-02 Process for the hydrogenative cracking of hydrocarbon oils

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GB1308963A Expired GB1007282A (en) 1962-04-04 1963-04-02 Hydrogenative cracking of hydrocarbon oils

Country Status (6)

Country Link
BE (2) BE630485A (en)
CH (1) CH442258A (en)
DE (2) DE1200990C2 (en)
DK (1) DK113792B (en)
GB (2) GB1007282A (en)
NL (3) NL143617B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1064025A (en) * 1964-08-27 1967-04-05 British Petroleum Co Improvements relating to hydrocatalytic cracking
SE312322B (en) * 1964-09-01 1969-07-14 Shell Int Research
GB1077312A (en) * 1964-09-28 1967-07-26 Phillips Petroleum Co Hydrocracking of high boiling range hydrocarbons

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE13369C (en) * E. LANGEN in Cöln a. Rh Continuous acting liquid-vaginal centrifuge with float
US2946738A (en) * 1957-07-01 1960-07-26 Phillips Petroleum Co Hydrocracking a gas oil with a presulfided catalyst consisting of oxides of vanadium, cobalt and molybdenum on gamma alumina

Also Published As

Publication number Publication date
BE630590A (en)
DE1200990B (en) 1975-05-22
NL143617B (en) 1974-10-15
CH442258A (en) 1967-08-31
DE1199421B (en) 1965-08-26
BE630485A (en)
NL291101A (en)
DK113792B (en) 1969-04-28
GB1007282A (en) 1965-10-13
DE1200990C2 (en) 1975-05-22
NL291100A (en)

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