KR920700767A - 탄화수소를 수소화 처리하기 위한 촉매계 및 방법 - Google Patents

탄화수소를 수소화 처리하기 위한 촉매계 및 방법

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Publication number
KR920700767A
KR920700767A KR1019910701567A KR910701567A KR920700767A KR 920700767 A KR920700767 A KR 920700767A KR 1019910701567 A KR1019910701567 A KR 1019910701567A KR 910701567 A KR910701567 A KR 910701567A KR 920700767 A KR920700767 A KR 920700767A
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catalyst
layer
pore size
alumina
average pore
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KR1019910701567A
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KR0149505B1 (ko
Inventor
엘. 윈슬로우 필립
에프. 설리반 리차드
Original Assignee
윌리암 제랄드 덕
셰브런 리써취 앤드 테크놀로지 캄파니
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Application filed by 윌리암 제랄드 덕, 셰브런 리써취 앤드 테크놀로지 캄파니 filed Critical 윌리암 제랄드 덕
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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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining 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
    • 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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/076—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/20—Sulfiding

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

Abstract

내용 없음

Description

탄화수소를 수소화 처리하기 위한 촉매계 및 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (25)

  1. 몰리브덴 함량이 제1층 촉매의 약 14%이상이고, 평균 세공크기가 약 60Å이상인 니켈-몰리브덴-인/알루미나 촉매 또는 코발트-몰리브덴-인/알루미나 촉매를 함유하는 제1층의 촉매, 및 지올라이트 성분이 제2층 촉매의 약 2중량% 이상을 구성하는 니켈-텅스텐-/실리카-알루미나-지올라이트 또는 니켈-몰리브덴/실리카-알루미나-지올라이트 촉매를 함유하는 제2층의 촉매로 이루어진 탄화수소의 수소화 처리용 층상 촉매계.
  2. 제1항에 있어서, 제1층 촉매가 니켈-몰리브덴-인/알루미나 촉매를 함유하는 촉매계.
  3. 제1항에 있어서, 제1층 촉매가 티타늄 산화물을 추가로 함유하는 촉매계.
  4. 제3항에 있어서, 제1층 촉매가 약70Å이상의 평균 세공크기를 지니는 감마 알루미나를 함유하는 촉매계.
  5. 제3항에 있어서, 제2층 촉매 지올라이트 성분이 약 3내지 약 20중량%의 제2층 촉매를 함유하는 촉매계.
  6. 제4항에 있어서, 제2층 촉매 지올라이트 성분이 약3내지 약 20중량%의 제2층 촉매를 함유하는 촉매계.
  7. 제1항에 있어서, 제1층 촉매가 약 75 내지 약 120Å의 평균 세공크기를 지니는 촉매계.
  8. 제2항에 있어서, 제1층 촉매가 약 75 내지 약 120Å의 평균 세공크기를 지니는 촉매계.
  9. 제3항에 있어서, 제1층 촉매가 약 75 내지 약 120Å의 평균 세공크기를 지니는 촉매계.
  10. 제6항에 있어서, 제1층 촉매가 약 75 내지 약 120Å의 평균 세공크기를 지니는 촉매계.
  11. 제1항에 있어서, 촉매가 예비 황화된 촉매계.
  12. 탄화수소를, 몰리브덴 함량이 제1층 촉매의 약14%이상이고 평균 세공크기가 약 60Å이상인 니켈-몰리브덴-인/알루미나 촉매 또는 코발트-몰리브덴-인/알루미나 촉매를 함유하는 제1층의 촉매, 및 지올라이트 성분이 약 2중량% 이상의 촉매를 구성하는 니켈-텅스텐/실리카-알루미나-지올라이트 또는 니켈-몰리브덴/실리카-알루미나-지올라이트 촉매를 함유하는 제2층의 촉매로 이루어진 층상 촉매의 존재하에서, 수소와 접촉시킴을 특징으로 하여 탄화수소를 탈질화 시키는 방법.
  13. 제12항에 있어서, 제1층 촉매가 니켈-몰리브덴-인/알루미나 촉매로 이루어진 방법.
  14. 제12항에 있어서, 제2층 촉매가 티타늄 산화물을 추가로 함유하는 방법.
  15. 제14항에 있어서, 제1층 촉매가 약 70Å 이상의 평균 세공 크기를 지니는 감마 알루미나를 함유하는 방법.
  16. 제14항에 있어서, 제2층 촉매 지올라이트 성분이 약 3내지 약 20중량%의 제2층 촉매를 구성하는 방법.
  17. 제15항에 있어서, 제2층 촉매 지올라이트 성분이 약 3내지 약20중량%의 제2층 촉매를 구성하는 방법.
  18. 제12항에 있어서, 제1층 촉매의 평균 세공 크기가 약 75 내지 약 120Å인 방법.
  19. 제13항에 있어서, 제1층 촉매의 평균 세공 크기가 약 75 내지 약 120Å인 방법.
  20. 제14항에 있어서, 제1층 촉매의 평균 세공 크기가 약 75 내지 약 120Å인 방법.
  21. 제17항에 있어서, 제1층 촉매의 평균 세공 크기가 약 75 내지 약 120Å인 방법.
  22. 제12항에 있어서, 층상 촉매가 예비 황화되는 방법.
  23. 제12항에 있어서, 탄화수소가 진공가스오일인 방법.
  24. 제14항에 있어서, 탄화수소가 진공가스오일인 방법.
  25. 제22항에 있어서, 탄화수소가 진공가스오일인 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019910701567A 1989-05-10 1990-05-09 탄화수소를 수소화처리하기 위한 촉매시스템 및 방법 Expired - Fee Related KR0149505B1 (ko)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US349,848 1989-05-10
US07/349,848 US4990243A (en) 1989-05-10 1989-05-10 Process for hydrodenitrogenating hydrocarbon oils
PCT/US1990/002581 WO1990013363A1 (en) 1989-05-10 1990-05-09 Catalyst system and process for hydrotreating hydrocarbons
US349848 1994-12-06

Publications (2)

Publication Number Publication Date
KR920700767A true KR920700767A (ko) 1992-08-10
KR0149505B1 KR0149505B1 (ko) 1998-10-15

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Country Status (11)

Country Link
US (1) US4990243A (ko)
EP (1) EP0482008B1 (ko)
JP (1) JP2529778B2 (ko)
KR (1) KR0149505B1 (ko)
AT (1) ATE108198T1 (ko)
AU (1) AU5726190A (ko)
DE (1) DE69010498T2 (ko)
ES (1) ES2056466T3 (ko)
RU (1) RU2093263C1 (ko)
UA (1) UA26317A (ko)
WO (1) WO1990013363A1 (ko)

Families Citing this family (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5116484A (en) * 1990-10-31 1992-05-26 Shell Oil Company Hydrodenitrification process
US5336654A (en) * 1990-12-24 1994-08-09 Exxon Research And Engineering Company Method for the preparation of supported hydrogenation and hydrotreating catalysts
US5338717A (en) * 1990-12-24 1994-08-16 Exxon Research And Engineering Company Method for the preparation of supported hydrogenation and hydrotreating catalysts
US5198100A (en) * 1990-12-24 1993-03-30 Exxon Research And Engineering Company Hydrotreating using novel hydrotreating catalyst
US5403806A (en) * 1993-10-22 1995-04-04 Union Oil Company Of California Phosphorous-containing hydroprocessing catalyst and method of preparation
US5925235A (en) * 1997-12-22 1999-07-20 Chevron U.S.A. Inc. Middle distillate selective hydrocracking process
EP0985448A1 (en) * 1998-08-28 2000-03-15 Engelhard Corporation Nickel catalyst
US5945570A (en) * 1998-10-29 1999-08-31 Arhancet; Juan Pedro Catalyst and process for preparing 1,3-propanediol
US6554994B1 (en) * 1999-04-13 2003-04-29 Chevron U.S.A. Inc. Upflow reactor system with layered catalyst bed for hydrotreating heavy feedstocks
CN100381543C (zh) * 2004-10-29 2008-04-16 中国石油化工股份有限公司 一种复合催化剂床层的加氢裂化方法
CN100364668C (zh) * 2004-10-29 2008-01-30 中国石油化工股份有限公司 一种ⅱb族金属氧化物表面改性加氢催化剂的制备方法
US7276152B2 (en) * 2004-11-23 2007-10-02 Cpc Corporation, Taiwan Oxidative desulfurization and denitrogenation of petroleum oils
WO2008154745A1 (en) * 2007-06-19 2008-12-24 Josephine Hill Catalyst compositions with permselective coatings, methods of making same, and uses thereof
US8980080B2 (en) * 2010-03-16 2015-03-17 Saudi Arabian Oil Company System and process for integrated oxidative desulfurization, desalting and deasphalting of hydrocarbon feedstocks
US8790508B2 (en) 2010-09-29 2014-07-29 Saudi Arabian Oil Company Integrated deasphalting and oxidative removal of heteroatom hydrocarbon compounds from liquid hydrocarbon feedstocks
KR101955702B1 (ko) 2011-07-31 2019-03-07 사우디 아라비안 오일 컴퍼니 아스팔트 및 탈황 오일을 제조하는 통합 공정
US8404912B1 (en) 2012-05-09 2013-03-26 Chevron U.S.A. Inc. Process for making high VI lubricating oils
US20140034549A1 (en) 2012-08-03 2014-02-06 Lummus Technology Inc. Residue hydrocracking
US9162938B2 (en) 2012-12-11 2015-10-20 Chevron Lummus Global, Llc Conversion of triacylglycerides-containing oils to hydrocarbons
US9024096B2 (en) 2012-12-11 2015-05-05 Lummus Technology Inc. Conversion of triacylglycerides-containing oils
KR102267501B1 (ko) * 2013-01-08 2021-06-21 사우디 아라비안 오일 컴퍼니 수소화분해 공정을 위한 촉매 로딩을 최적화하는 방법
US9080113B2 (en) 2013-02-01 2015-07-14 Lummus Technology Inc. Upgrading raw shale-derived crude oils to hydrocarbon distillate fuels
US20140221709A1 (en) 2013-02-04 2014-08-07 Lummus Technology Inc. Integration of residue hydrocracking and solvent deasphalting
US20140221713A1 (en) 2013-02-04 2014-08-07 Lummus Technology Inc. Residue hydrocracking processing
US9650312B2 (en) 2013-03-14 2017-05-16 Lummus Technology Inc. Integration of residue hydrocracking and hydrotreating
US9452955B2 (en) 2013-03-14 2016-09-27 Lummus Technology Inc. Process for producing distillate fuels and anode grade coke from vacuum resid
US20150152336A1 (en) 2013-12-04 2015-06-04 Lummus Technology Inc. Co-current adiabatic reaction system for conversion of triacylglycerides rich feedstocks
KR20170034908A (ko) 2014-07-25 2017-03-29 사우디 아라비안 오일 컴퍼니 아스팔트, 석유 그린 코크스, 및 액체 및 기체 코킹 유닛 생성물을 제조하기 위한 통합된 공정
US9695369B2 (en) 2014-11-21 2017-07-04 Lummus Technology Inc. Process to upgrade partially converted vacuum residua
CN109477008A (zh) * 2016-06-29 2019-03-15 埃克森美孚研究工程公司 重质烃进料的加工
CN110249033A (zh) * 2016-12-21 2019-09-17 沙特阿拉伯石油公司 用于优化加氢裂化工艺的催化剂负载的方法
WO2020117119A1 (en) * 2018-12-05 2020-06-11 Biofuel-Solution I Malmö Ab A process for converting glycerol to propane
EP4144437A4 (en) 2020-04-28 2024-07-03 China Petroleum & Chemical Corporation HYDROGENATION CATALYST AND PREPARATION METHOD AND USE THEREOF

Family Cites Families (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL123195C (ko) * 1960-03-02
US3184403A (en) * 1960-09-12 1965-05-18 Phillips Petroleum Co Two-section catalyst bed
US3189540A (en) * 1962-01-02 1965-06-15 California Research Corp Production of lubricating oils by catalytic hydrogenation
US3238123A (en) * 1962-05-11 1966-03-01 Exxon Research Engineering Co Catalytic hydrofining process
US3228993A (en) * 1962-08-23 1966-01-11 Chevron Res Catalytic hydrogenation process employing a reduced nickel- molybdenum-alumina catalyst
NL7202241A (ko) * 1971-02-06 1973-08-23
US3923638A (en) * 1971-12-10 1975-12-02 Standard Oil Co Two-catalyst hydrocracking process
US3897365A (en) * 1973-09-20 1975-07-29 American Cyanamid Co Hydrotreating catalyst and process therefor
US3897367A (en) * 1973-10-10 1975-07-29 Du Pont Metal oxide catalytic compositions
US4022682A (en) * 1975-12-22 1977-05-10 Gulf Research & Development Company Hydrodenitrogenation of shale oil using two catalysts in series reactors
US4210521A (en) * 1977-05-04 1980-07-01 Mobil Oil Corporation Catalytic upgrading of refractory hydrocarbon stocks
JPS6038179B2 (ja) * 1977-08-26 1985-08-30 松下電器産業株式会社 排ガス浄化用触媒体
US4221677A (en) * 1979-03-19 1980-09-09 Standard Oil Company (Indiana) Catalytic cracking with reduced emission of noxious gases
US4255282A (en) * 1979-05-11 1981-03-10 Union Oil Company Of California Hydrotreating catalyst and process for its preparation
CA1182769A (en) * 1980-04-10 1985-02-19 Ronald S. Tolberg Two-bed catalytic hydroprocessing for heavy hydrocarbon feedstocks
FR2482126A1 (fr) * 1980-05-08 1981-11-13 Elf France Amelioration de la stabilite des catalyseurs d'hydrotraitement catalytique des coupes petrolieres
US4325808A (en) * 1980-07-21 1982-04-20 Standard Oil Company (Indiana) Hydrocarbon conversion catalyst system and method
JPS5829141A (ja) * 1981-08-15 1983-02-21 Hitachi Maxell Ltd 磁気記録媒体
US4406779A (en) * 1981-11-13 1983-09-27 Standard Oil Company (Indiana) Multiple catalyst system for hydrodenitrogenation of high nitrogen feeds
US4534853A (en) * 1983-10-19 1985-08-13 Union Carbide Corporation Method for cracking residual oils
US4761220A (en) * 1984-10-31 1988-08-02 Chevron Research Company Hydroprocessing catalyst fines as a first-stage catalyst in a two-stage, close-coupled thermal catalytic hydroconversion process
JPS61126198A (ja) * 1984-11-22 1986-06-13 Electric Power Dev Co Ltd 脱灰高濃度スラリ−の製造プロセス
JPH0631333B2 (ja) * 1984-11-22 1994-04-27 重質油対策技術研究組合 炭化水素類の水素化分解方法
US4534852A (en) * 1984-11-30 1985-08-13 Shell Oil Company Single-stage hydrotreating process for converting pitch to conversion process feedstock
US4680280A (en) * 1985-03-15 1987-07-14 Chevron Research Company Sulfur tolerance of zeolitic reforming catalysts
US4657663A (en) * 1985-04-24 1987-04-14 Phillips Petroleum Company Hydrotreating process employing a three-stage catalyst system wherein a titanium compound is employed in the second stage
US4797196A (en) * 1988-02-26 1989-01-10 Amoco Corporation Hydrocracking process using special juxtaposition of catalyst zones
US4797195A (en) * 1988-02-26 1989-01-10 Amoco Corporation Three zone hydrocracking process

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DE69010498D1 (de) 1994-08-11
RU2093263C1 (ru) 1997-10-20
KR0149505B1 (ko) 1998-10-15
WO1990013363A1 (en) 1990-11-15
AU5726190A (en) 1990-11-29
UA26317A (uk) 1999-08-30
EP0482008A4 (en) 1992-07-15
JPH04505278A (ja) 1992-09-17
JP2529778B2 (ja) 1996-09-04
EP0482008B1 (en) 1994-07-06
US4990243A (en) 1991-02-05
ES2056466T3 (es) 1994-10-01
EP0482008A1 (en) 1992-04-29
ATE108198T1 (de) 1994-07-15
DE69010498T2 (de) 1995-03-02

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