ES8608567A1 - Un procedimiento para producir un catalizador de hidrotrata-miento - Google Patents

Un procedimiento para producir un catalizador de hidrotrata-miento

Info

Publication number
ES8608567A1
ES8608567A1 ES542525A ES542525A ES8608567A1 ES 8608567 A1 ES8608567 A1 ES 8608567A1 ES 542525 A ES542525 A ES 542525A ES 542525 A ES542525 A ES 542525A ES 8608567 A1 ES8608567 A1 ES 8608567A1
Authority
ES
Spain
Prior art keywords
silica
angstrom
hydrotreating catalyst
metal
manufacture
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
ES542525A
Other languages
English (en)
Other versions
ES542525A0 (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.)
Tonen General Sekiyu KK
Original Assignee
Toa Nenryo Kogyyo KK
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
Priority claimed from JP59081961A external-priority patent/JPS60225645A/ja
Application filed by Toa Nenryo Kogyyo KK filed Critical Toa Nenryo Kogyyo KK
Publication of ES542525A0 publication Critical patent/ES542525A0/es
Publication of ES8608567A1 publication Critical patent/ES8608567A1/es
Expired legal-status Critical Current

Links

Classifications

    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • B01J37/0205—Impregnation in several steps
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts 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
    • B01J23/84—Catalysts 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
    • B01J23/85—Chromium, molybdenum or tungsten
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/31—Density
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63—Pore volume
    • B01J35/635—0.5-1.0 ml/g
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66—Pore distribution
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining 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
    • C10G45/04—Refining 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
    • C10G45/06—Refining 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
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining 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
    • C10G45/04—Refining 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
    • C10G45/06—Refining 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
    • C10G45/08—Refining 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
    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12—Silica 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)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

PROCEDIMIENTO PARA PRODUCIR UN CATALIZADOR DE HIDROTRATAMIENTO. CONSISTE EN: A) DAR LUGAR A QUE UN SOPORTE DE ALUMINA O QUE CONTIENE ALUMINA, CONTENIENDO TAMBIEN SILICE, SUSTENTE INICIALMENTE UN PRIMER TERMINO DE UN METAL SELECCIONADO DEL GRUPO CONSISTENTE EN METALES DEL GRUPO VIII DE LA TABLA PERIODICA DE LOS ELEMENETOS, ESTANDO CONTENIDO EL METAL SELECCIONADO DEL GRUPO VIII EN UNA CANTIDAD DE 0,5 A 20% EN PESO, EN TERMINOS DE UN OXIDO; B) DAR LUGAR A QUE EL SOPORTE QUE CONTIENE EL METAL DEL GRUPO VIII SUSTENTE, DESPUES DE ELLO, UN METAL SELECCIONADO DEL GRUPO CONSISTENTE EN METALES DEL GRUPO VIB DE LA TABLA PERIODICA DE LOS ELEMENTOS, ESTANDO CONTENIDO DICHO METAL SELECCIONADO DEL GRUPO VIB EN UNA CANTIDAD DE 5 A 30% EN PESO, EN TERMINOS DE UN OXIDO; Y C) RECUPERAR EL CATALIZADOR DE HIDROTRATAMIENTO.
ES542525A 1984-04-25 1985-04-24 Un procedimiento para producir un catalizador de hidrotrata-miento Expired ES8608567A1 (es)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP59081961A JPS60225645A (ja) 1984-04-25 1984-04-25 水素化処理用触媒の製造法
JP59133072A JPS6115739A (ja) 1984-04-25 1984-06-29 水素化処理用触媒
JP4166874A JPH0772273B2 (ja) 1984-04-25 1992-06-01 炭化水素油の水素化処理方法

Publications (2)

Publication Number Publication Date
ES542525A0 ES542525A0 (es) 1986-06-16
ES8608567A1 true ES8608567A1 (es) 1986-06-16

Family

ID=27303752

Family Applications (1)

Application Number Title Priority Date Filing Date
ES542525A Expired ES8608567A1 (es) 1984-04-25 1985-04-24 Un procedimiento para producir un catalizador de hidrotrata-miento

Country Status (8)

Country Link
US (1) US4837193A (es)
EP (1) EP0160475B1 (es)
JP (2) JPS6115739A (es)
AU (1) AU570794B2 (es)
CA (1) CA1249570A (es)
ES (1) ES8608567A1 (es)
FI (1) FI851626L (es)
NO (1) NO851641L (es)

Families Citing this family (79)

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CN112717949B (zh) * 2019-10-28 2022-07-12 中国石油化工股份有限公司 一种加氢精制催化剂及其制备方法和应用
CN113042021B (zh) * 2019-12-27 2023-05-26 中国石油化工股份有限公司 一种沸腾床加氢催化剂及其制备方法
CN116060032A (zh) * 2021-10-30 2023-05-05 中国石油化工股份有限公司 一种蜡油加氢处理催化剂及其制备方法与应用

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JPH0772273B2 (ja) 1995-08-02
NO851641L (no) 1985-10-28
JPH0331496B2 (es) 1991-05-07
EP0160475A3 (en) 1987-09-09
JPH05192587A (ja) 1993-08-03
JPS6115739A (ja) 1986-01-23
AU570794B2 (en) 1988-03-24
FI851626A0 (fi) 1985-04-24
FI851626L (fi) 1985-10-26
ES542525A0 (es) 1986-06-16
US4837193A (en) 1989-06-06
EP0160475B1 (en) 1991-07-03
AU4169385A (en) 1985-10-31
CA1249570A (en) 1989-01-31
EP0160475A2 (en) 1985-11-06

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