DE69508022D1 - Hydrobehandlungskatalysator, seine Herstellung und Verwendung - Google Patents

Hydrobehandlungskatalysator, seine Herstellung und Verwendung

Info

Publication number
DE69508022D1
DE69508022D1 DE69508022T DE69508022T DE69508022D1 DE 69508022 D1 DE69508022 D1 DE 69508022D1 DE 69508022 T DE69508022 T DE 69508022T DE 69508022 T DE69508022 T DE 69508022T DE 69508022 D1 DE69508022 D1 DE 69508022D1
Authority
DE
Germany
Prior art keywords
manufacture
hydrotreatment catalyst
hydrotreatment
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 - Lifetime
Application number
DE69508022T
Other languages
German (de)
English (en)
Inventor
Katsuhisa Fujita
Tetsuro Kamo
Masafumi Shimowake
Yoshimasa Inoue
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.)
Nippon Ketjen Co Ltd
Original Assignee
Nippon Ketjen Co Ltd
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 Nippon Ketjen Co Ltd filed Critical Nippon Ketjen Co Ltd
Application granted granted Critical
Publication of DE69508022D1 publication Critical patent/DE69508022D1/de
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • 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
    • 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
    • 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
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • 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
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/63Pore volume
    • B01J35/6350.5-1.0 ml/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64Pore diameter
    • B01J35/6472-50 nm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66Pore distribution

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)
DE69508022T 1994-09-19 1995-09-12 Hydrobehandlungskatalysator, seine Herstellung und Verwendung Expired - Lifetime DE69508022D1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24828894A JP3504984B2 (ja) 1994-09-19 1994-09-19 重質炭化水素油の水素化脱硫脱金属触媒

Publications (1)

Publication Number Publication Date
DE69508022D1 true DE69508022D1 (de) 1999-04-08

Family

ID=36954225

Family Applications (1)

Application Number Title Priority Date Filing Date
DE69508022T Expired - Lifetime DE69508022D1 (de) 1994-09-19 1995-09-12 Hydrobehandlungskatalysator, seine Herstellung und Verwendung

Country Status (10)

Country Link
US (1) US5888380A (cg-RX-API-DMAC10.html)
EP (1) EP0704239B1 (cg-RX-API-DMAC10.html)
JP (1) JP3504984B2 (cg-RX-API-DMAC10.html)
KR (1) KR100356431B1 (cg-RX-API-DMAC10.html)
CA (1) CA2158594C (cg-RX-API-DMAC10.html)
DE (1) DE69508022D1 (cg-RX-API-DMAC10.html)
MY (1) MY112928A (cg-RX-API-DMAC10.html)
SG (1) SG34272A1 (cg-RX-API-DMAC10.html)
TW (1) TW364861B (cg-RX-API-DMAC10.html)
ZA (1) ZA957855B (cg-RX-API-DMAC10.html)

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11319584A (ja) * 1998-05-11 1999-11-24 Nippon Kecchen Kk 粒状触媒用担体の製造方法および該担体を用いた触媒の製造方法
JP4266406B2 (ja) 1998-05-11 2009-05-20 日本ケッチェン株式会社 粒状触媒用担体及びこの担体を用いた触媒及び該触媒による炭化水素油の水素化処理方法
RU2167715C1 (ru) * 2000-02-03 2001-05-27 ОАО "Газпром" Способ получения катализатора
RU2185240C2 (ru) * 2000-04-24 2002-07-20 Закрытое акционерное общество "Катализаторная компания" Никельалюмохромовый катализатор для гидрирования органических соединений, для метанирования co и co2 и других процессов и способ его получения
RU2186623C1 (ru) * 2001-03-11 2002-08-10 Закрытое акционерное общество "Катализаторная компания" Способ получения катализатора для гидрирования ароматических соединений, для метанирования со и со2
JP4773634B2 (ja) * 2001-06-08 2011-09-14 日本ケッチェン株式会社 重質炭化水素油の2段階水素化処理方法
JP4773633B2 (ja) * 2001-06-08 2011-09-14 日本ケッチェン株式会社 重質炭化水素油の2段階水素化処理方法
JP4612229B2 (ja) * 2001-06-08 2011-01-12 日本ケッチェン株式会社 重質炭化水素油の水素化処理用触媒並びに水素化処理方法
RU2205068C1 (ru) * 2002-02-18 2003-05-27 Меньшов Владимир Никифорович Способ получения никель-алюмо-хромового катализатора для окислительно-восстановительных процессов, в частности для метанирования оксидов углерода
FR2839902B1 (fr) * 2002-05-24 2007-06-29 Inst Francais Du Petrole Catalyseur d'hydroraffinage et/ou d'hydroconversion et son utilisation dans des procedes d'hydrotraitement de charges hydrocarbonees
US20060013972A1 (en) * 2002-11-14 2006-01-19 Katsuhiro Nishiyama Multilayer sheet and package body made from the multilayer sheet for packaging food, medicine or tool
AU2003201827A1 (en) * 2003-01-06 2004-08-10 Uop Llc Attrition resistant catalyst for hydrocarbon conversion
US20050113250A1 (en) * 2003-11-10 2005-05-26 Schleicher Gary P. Hydrotreating catalyst system suitable for use in hydrotreating hydrocarbonaceous feedstreams
US7816299B2 (en) * 2003-11-10 2010-10-19 Exxonmobil Research And Engineering Company Hydrotreating catalyst system suitable for use in hydrotreating hydrocarbonaceous feedstreams
US20050109679A1 (en) * 2003-11-10 2005-05-26 Schleicher Gary P. Process for making lube oil basestocks
US7745369B2 (en) 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
US8025794B2 (en) * 2003-12-19 2011-09-27 Shell Oil Company Systems, methods, and catalysts for producing a crude product
BRPI0405589B1 (pt) * 2003-12-19 2014-09-02 Shell Int Research Método de produzir um produto de petróleo bruto
US20100098602A1 (en) 2003-12-19 2010-04-22 Opinder Kishan Bhan Systems, methods, and catalysts for producing a crude product
US7811445B2 (en) 2003-12-19 2010-10-12 Shell Oil Company Systems and methods of producing a crude product
US20060060510A1 (en) * 2004-09-17 2006-03-23 Bhan Opinder K High activity hydrodesulfurization catalyst, a method of making a high activity hydrodesulfurization catalyst, and a process for manufacturing an ultra-low sulfur distillate product
CA2604012C (en) 2005-04-11 2013-11-19 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced mcr content
CN101166811A (zh) 2005-04-11 2008-04-23 国际壳牌研究有限公司 生产具有降低氮含量的原油产品的方法和催化剂
BRPI0608827A2 (pt) * 2005-04-21 2016-11-08 Shell Int Research processo para a hidrogenação de aldeídos, catalisador de hidrogenação, e, processo para preparar um catalisador
BRPI0709821A2 (pt) * 2006-04-13 2011-07-26 Shell Int Research processo para a hirogenaÇço de um aldeÍdo
US8110527B2 (en) 2006-08-11 2012-02-07 China Petroleum & Chemical Corporation Alumina having a complex pore structure, and catalyst and process for selective hydrogenation of cracking gasoline
US20080135449A1 (en) 2006-10-06 2008-06-12 Opinder Kishan Bhan Methods for producing a crude product
US8212062B2 (en) 2007-04-02 2012-07-03 Inventure Chemical, Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of oil-containing materials with cellulosic and peptidic content
US7943792B2 (en) * 2007-04-02 2011-05-17 Inventure Chemical Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and peptidic content
KR20110018875A (ko) * 2008-04-10 2011-02-24 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 촉매 시스템 및 이 촉매 시스템으로 미정제 공급물을 변환시키는 방법
US7777085B2 (en) * 2008-10-01 2010-08-17 Inventure Chemical, Inc. Method for conversion of oil-containing algae to 1,3-propanediol
TWI579043B (zh) 2012-02-17 2017-04-21 先進精鍊科技有限公司 球形觸媒支撐物及其製備方法
TWI611836B (zh) 2012-02-17 2018-01-21 Advanced Refining Technologies Llc. 觸媒支撐物及其製備方法
TWI632235B (zh) 2012-06-20 2018-08-11 美商先進精鍊科技有限公司 用於殘渣油徑原料之加氫脫硫反應的觸媒及其製備方法
TWI666310B (zh) * 2013-03-15 2019-07-21 Advanced Refining Technologies Llc 觸媒組成物、加氫處理重烴類部分之方法及製備沉澱氧化鋁組成物的方法
RU2605939C2 (ru) * 2015-05-22 2016-12-27 Открытое акционерное общество "Нефтяная компания "Роснефть" Носитель катализатора гидрооблагораживания вакуумного газойля и способ его приготовления (варианты)
FR3075072B1 (fr) * 2017-12-14 2021-11-26 Ifp Energies Now Catalyseur d'hydrodesulfuration selective des essences de fcc

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US3931052A (en) 1973-08-29 1976-01-06 Mobil Oil Corporation Alumina-supported catalyst for residua demetalation and desulfurization
US4271042A (en) * 1977-12-20 1981-06-02 Mobil Oil Corporation Process for demetalation and desulfurization of petroleum oils
US4588709A (en) 1983-12-19 1986-05-13 Intevep, S.A. Catalyst for removing sulfur and metal contaminants from heavy crudes and residues
US5223472A (en) * 1992-04-14 1993-06-29 Union Oil Company Of California Demetallation catalyst
US5358633A (en) * 1993-05-28 1994-10-25 Texaco Inc. Hydrodesulfurization of cracked naphtha with low levels of olefin saturation

Also Published As

Publication number Publication date
JPH0889805A (ja) 1996-04-09
CA2158594C (en) 2005-05-24
EP0704239B1 (en) 1999-03-03
US5888380A (en) 1999-03-30
TW364861B (en) 1999-07-21
ZA957855B (en) 1996-05-06
KR100356431B1 (ko) 2003-02-07
JP3504984B2 (ja) 2004-03-08
EP0704239A3 (cg-RX-API-DMAC10.html) 1996-05-01
KR960010073A (ko) 1996-04-20
EP0704239A2 (en) 1996-04-03
MY112928A (en) 2001-10-31
CA2158594A1 (en) 1996-03-20
SG34272A1 (en) 1996-12-06

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