ES401056A1 - Method of preparing a hydrorefining catalyst - Google Patents

Method of preparing a hydrorefining catalyst

Info

Publication number
ES401056A1
ES401056A1 ES401056A ES401056A ES401056A1 ES 401056 A1 ES401056 A1 ES 401056A1 ES 401056 A ES401056 A ES 401056A ES 401056 A ES401056 A ES 401056A ES 401056 A1 ES401056 A1 ES 401056A1
Authority
ES
Spain
Prior art keywords
approximately
support material
preparing
solution
temperature
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
ES401056A
Other languages
Spanish (es)
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products 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 Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of ES401056A1 publication Critical patent/ES401056A1/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
    • B01J37/08Heat treatment
    • B01J37/10Heat treatment in the presence of water, e.g. steam
    • 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
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652Chromium, molybdenum or tungsten
    • 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
    • B01J23/84Catalysts 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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • 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
    • B01J23/84Catalysts 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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/88Molybdenum
    • B01J23/883Molybdenum and nickel
    • 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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

Landscapes

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

Abstract

A method of preparing a hydrorefin catalyst comprising: (a) impregnating a refractory inorganic oxide support material with an aqueous solution of a soluble compound of a Group VI B metal and a Group VIII metal at the same time as running rapid evaporation of water from said solution, the volume ratio of impregnating solution to support material being approximately 0.5: 1 to 2: 1; (b) partially calcining the impregnated support material for approximately 1/2 hour at least at a temperature of approximately 100 to 427ºC; and (c) calcining the material from step (b) at a temperature of about 621ºC for about 1 to about 4 hours in an atmosphere comprising at least about 25% steam. (Machine-translation by Google Translate, not legally binding)
ES401056A 1971-03-25 1972-03-22 Method of preparing a hydrorefining catalyst Expired ES401056A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12811471A 1971-03-25 1971-03-25

Publications (1)

Publication Number Publication Date
ES401056A1 true ES401056A1 (en) 1975-07-16

Family

ID=22433707

Family Applications (1)

Application Number Title Priority Date Filing Date
ES401056A Expired ES401056A1 (en) 1971-03-25 1972-03-22 Method of preparing a hydrorefining catalyst

Country Status (14)

Country Link
JP (1) JPS5229717B1 (en)
AU (1) AU459131B2 (en)
BR (1) BR7201734D0 (en)
CA (1) CA986496A (en)
DE (1) DE2214207B2 (en)
ES (1) ES401056A1 (en)
FR (1) FR2130711B1 (en)
GB (1) GB1379847A (en)
IT (1) IT952359B (en)
NL (1) NL161371C (en)
PL (1) PL83329B1 (en)
SE (1) SE384802B (en)
YU (1) YU34627B (en)
ZA (1) ZA721900B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53149412U (en) * 1977-04-30 1978-11-24
FR2424577A1 (en) * 1978-02-24 1979-11-23 Scholtes Ets Eugen Convector heaters network temp. controller - has programmable clock monitoring changeover with master control circuit operating with individual heater controllers
US6958309B2 (en) * 2002-08-01 2005-10-25 Conocophillips Company Hydrothermal pretreatment for increasing average pore size in a catalyst support

Also Published As

Publication number Publication date
FR2130711B1 (en) 1977-08-05
BR7201734D0 (en) 1973-06-14
IT952359B (en) 1973-07-20
JPS5229717B1 (en) 1977-08-03
GB1379847A (en) 1975-01-08
NL161371C (en) 1980-02-15
NL7203877A (en) 1972-09-27
ZA721900B (en) 1972-12-27
PL83329B1 (en) 1975-12-31
FR2130711A1 (en) 1972-11-03
YU34627B (en) 1979-12-31
NL161371B (en) 1979-09-17
AU4025872A (en) 1973-09-27
AU459131B2 (en) 1975-02-28
DE2214207A1 (en) 1972-10-12
SE384802B (en) 1976-05-24
CA986496A (en) 1976-03-30
YU74072A (en) 1979-07-10
DE2214207B2 (en) 1976-04-15

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