NO961265L - Katalysator for anvendelse ved hydroprosessering - Google Patents

Katalysator for anvendelse ved hydroprosessering

Info

Publication number
NO961265L
NO961265L NO961265A NO961265A NO961265L NO 961265 L NO961265 L NO 961265L NO 961265 A NO961265 A NO 961265A NO 961265 A NO961265 A NO 961265A NO 961265 L NO961265 L NO 961265L
Authority
NO
Norway
Prior art keywords
catalyst
group viii
refractory oxide
viii metal
metal component
Prior art date
Application number
NO961265A
Other languages
English (en)
Other versions
NO961265D0 (no
Inventor
Pradeep S Iyer
Howard D Simpson
Suheil F Abdo
Original Assignee
Uop Inc
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 US08/130,109 external-priority patent/US5389595A/en
Application filed by Uop Inc filed Critical Uop Inc
Publication of NO961265L publication Critical patent/NO961265L/no
Publication of NO961265D0 publication Critical patent/NO961265D0/no

Links

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
    • 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
    • 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
    • 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
    • B01J23/88—Molybdenum
    • B01J23/883—Molybdenum and nickel
    • 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
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • 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
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19—Molybdenum
    • 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
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

Katalysator inneholdende et oversjikt av en katalytisk aktivator på en porøs ild- fast bærer som inneholder et undersjikt med en bestanddel av metall fra gruppe VIII. Katalysatoren fremstilles ved trinnvis innlemmelse av metallet fra gruppe VIII, fulgt av en ytterligere katalytisk aktivatorbestanddel, vanlig- vis et metall fra gruppe VIB, på den porøse ildfaste oksidbærer. Nikkel- bestanddeler i undersjiktet på kata- lysatoren kjennetegnes ved et Raman- spektrum som viser Raman-bånd i områdene 240-250 cm'1 og 595-605 cm'1. Katalysa- toren har et vektforhold Mo03/NiO på mindre enn 6:1 og inneholder mer enn 4 vekt% NiO. Katalysatoren tilberedes ved først å fremstille et kalsinert partik- kelformet stoff som inneholder en metallbestanddel fra gruppe VIII og et ildfast oksid, og deretter tilsette en aktivator, så som en metallbestanddel fra gruppe VIB, og deretter rekalsinere slik at det oppnås et partikkelformet stoff. Foretrukne aktivatorer er molybden- og fosforforbindelser. Den foretrukne sammensetning er Ni-P-Mo-oksider på alumina. Katalysatoren er anvendelig ved samtidig hydrodenitrogenering og hydro- desulfurering av gassolje, særlig når den ildfaste oksid-bærer har porer med smal størrelsesfordeling.
NO961265A 1993-09-30 1996-03-28 Katalysator for anvendelse ved hydroprosessering NO961265D0 (no)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US08/130,109 US5389595A (en) 1993-09-30 1993-09-30 Hydroprocessing catalyst, its use, and method of preparation
US08/313,723 US5686375A (en) 1993-09-30 1994-09-27 Hydroprocessing catalyst and its use
PCT/US1994/011095 WO1995009049A2 (en) 1993-09-30 1994-09-29 Hydroprocessing catalyst and its use

Publications (2)

Publication Number Publication Date
NO961265L true NO961265L (no) 1996-03-28
NO961265D0 NO961265D0 (no) 1996-03-28

Family

ID=26828181

Family Applications (1)

Application Number Title Priority Date Filing Date
NO961265A NO961265D0 (no) 1993-09-30 1996-03-28 Katalysator for anvendelse ved hydroprosessering

Country Status (6)

Country Link
US (1) US5906731A (no)
JP (1) JP3821483B2 (no)
CN (1) CN1074687C (no)
CA (1) CA2170625A1 (no)
NO (1) NO961265D0 (no)
WO (1) WO1995009049A2 (no)

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US7569136B2 (en) 1997-06-24 2009-08-04 Ackerson Michael D Control system method and apparatus for two phase hydroprocessing
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DE60020292T2 (de) * 1999-04-08 2006-05-04 Albemarle Netherlands B.V. Verfahren zur Sulfidierung eines organischen Stickstoff und Carbonyl enthaltenden Hydrobehandlungskatalysators
US6841512B1 (en) * 1999-04-12 2005-01-11 Ovonic Battery Company, Inc. Finely divided metal catalyst and method for making same
CN1093434C (zh) * 1999-09-17 2002-10-30 厦门大学 细菌还原法制备负载型金催化剂
JP4638610B2 (ja) * 2001-01-05 2011-02-23 日本ケッチェン株式会社 水素化処理用触媒並びに水素化処理方法
US6759364B2 (en) * 2001-12-17 2004-07-06 Shell Oil Company Arsenic removal catalyst and method for making same
US7427578B2 (en) 2002-08-30 2008-09-23 Japan Energy Corporation Method for producing hydrorefining catalyst
AR044779A1 (es) 2003-06-16 2005-10-05 Shell Int Research Un proceso y un catalizador para la hidrogenacion selectiva de las diolefinas de una corriente de olefinas y para la remocion de arsenico de la misma y un metodo de elaboracion de dicho catalizador
US20070000808A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method and catalyst for producing a crude product having selected properties
US8241489B2 (en) 2003-12-19 2012-08-14 Shell Oil Company Systems, methods, and catalysts for producing a crude product
US7745369B2 (en) * 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
JP2006035052A (ja) * 2004-07-23 2006-02-09 Nippon Oil Corp 石油系炭化水素の水素化脱硫触媒および水素化脱硫方法
JP4249632B2 (ja) * 2004-01-09 2009-04-02 新日本石油株式会社 石油系炭化水素の水素化脱硫触媒および水素化脱硫方法
EP1702682A4 (en) * 2004-01-09 2009-06-10 Nippon Oil Corp HYDROGENATION AND DESULFURIZATION CATALYST FOR PETROLEUM HYDROCARBON AND HYDROGENATION AND DESULFURATION METHOD USING THE CATALYST
WO2006116208A1 (en) * 2005-04-26 2006-11-02 Shell Internationale Research Maatschappij B.V. A method for the selective hydrodesulfurization of an olefin containing hydrocarbon feedstock
MXPA05012893A (es) * 2005-11-29 2007-11-23 Mexicano Inst Petrol Catalizador para la hidrodesulfuracion de residuos y crudos pesados.
GB201000045D0 (en) * 2010-01-04 2010-02-17 Johnson Matthey Plc Catalyst and method of catalyst manufacture
EP2567219B1 (en) * 2010-05-07 2019-09-18 MannKind Corporation Method and apparatus for determining weight percent of microparticles of diketopiperazine in suspension using raman spectroscopy
US9096804B2 (en) 2011-01-19 2015-08-04 P.D. Technology Development, Llc Process for hydroprocessing of non-petroleum feedstocks
US20130105357A1 (en) * 2011-10-27 2013-05-02 Shell Oil Company Self-activating hydroprocessing catalyst and process for treating heavy hydrocarbon feedstocks
KR102421498B1 (ko) * 2014-07-11 2022-07-14 쉘 인터내셔날 리써취 마트샤피지 비.브이. 비소 농도를 갖는 탄화수소 공급물을 처리하기 위한 수소화가공 촉매 및 이러한 촉매의 제조 및 사용 방법
CN107921413B (zh) * 2015-05-29 2021-07-20 先进炼制技术有限公司 高加氢脱氮选择性的加氢处理催化剂
CN105772004A (zh) * 2016-03-24 2016-07-20 山东成泰化工有限公司 一种苯加氢催化剂及其制备方法
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Also Published As

Publication number Publication date
WO1995009049A3 (en) 1995-06-08
JP3821483B2 (ja) 2006-09-13
US5906731A (en) 1999-05-25
CN1132482A (zh) 1996-10-02
NO961265D0 (no) 1996-03-28
JP2002504009A (ja) 2002-02-05
WO1995009049A2 (en) 1995-04-06
CA2170625A1 (en) 1995-04-06
CN1074687C (zh) 2001-11-14

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