KR890005248A - 탄화수소성 공급원료의 전환 방법 - Google Patents

탄화수소성 공급원료의 전환 방법 Download PDF

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KR890005248A
KR890005248A KR1019880012462A KR880012462A KR890005248A KR 890005248 A KR890005248 A KR 890005248A KR 1019880012462 A KR1019880012462 A KR 1019880012462A KR 880012462 A KR880012462 A KR 880012462A KR 890005248 A KR890005248 A KR 890005248A
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catalyst
bed
hydrogen
feedstock
weight
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KR1019880012462A
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KR970001188B1 (ko
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반 디예크 니콜라스
알리 에제너 아이딘
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오노 알버어스
셀 인터나쵸 나아레 레사아치 마아츠샤피 비이부이
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Application filed by 오노 알버어스, 셀 인터나쵸 나아레 레사아치 마아츠샤피 비이부이 filed Critical 오노 알버어스
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    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals 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
    • C10G45/44—Hydrogenation of the aromatic hydrocarbons
    • C10G45/46—Hydrogenation of the aromatic hydrocarbons characterised by the catalyst used
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • 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
    • C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps

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

Abstract

내용 없음

Description

탄화수소성 공급원료의 전환 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (10)

  1. 상승된 압력 및 온도에서, 수소첨가 분해된 유출액을 생성하는 촉매 A의 베드를 통해 수소와 공급원료를 접촉시킨 후, 촉매 B의 베드를 통해 수소화 상기 수소첨가 분해딘 유출액 적어도 일부를 접촉시키는 것으로 구성되는 것으로 이때, 촉매 A는 무정형 분해 성분, 원소 주기율표의 VIB족 및/또는 Ⅷ족의 적어도 하나의 금속 및 불소를 포함하고, 촉매 B는 포우저 사이트(faujasite)-형 제올라이트 및 원소 주기율표 VIB족 및/또는 Ⅷ족의 적어도 하나의 금속을 포함하는 탄화수소성 공급원료를 보다 낮은 평균 비점을 갖는 생성물로 전환시키는 방법.
  2. 제1항에 있어서, 무정형 분해 성분이 알루미나인 방법.
  3. 제1항 또는 제2항에 있어서, 촉매 A가 몰리브덴 및/또는 텅스텐 및/또는 코발트 및/또는 니켈 및/또는 백금 및/또는 파라디움을 포함하는 방법.
  4. 제1항 내지 제3항중 어느 하나에 있어서, 촉매 A가 전체 촉매를 기준으로, 적어도 하나의 VIB족 금속 6-24중량%, 적어도 하나의 Ⅷ족 금속 1-16중량% 및 불소 0.5-1중량%를 포함하는 방법.
  5. 제1항 내지 제4항중 어느 하나에 있어서, 촉매 A의 베드 내 효력있는 반응 조건이, 280-450℃, 수소(부분)압력 0.3-5kg/1.h 및 수소/공급원료비 100-3000Nl/kg인 방법.
  6. 제1항 내지 제5항중 어느 하나에 있어서, 촉매 B에 불소가 포함된 방법.
  7. 제6항에 있어서, 촉매 B가 불소 0.5-10중량%를 포함하는 방법.
  8. 제1항 내지 제7항중 어느 하나에 있어서, 촉매 B의 포우저사이트-형 제올라이트가 제올라이트 Y인 방법.
  9. 제1항 내지 제8항중 어느 하나에 있어서, 촉매 B가 하나이상의 니켈 및/또는 코발트 화합물 및 하나이상의 텅스텐 및/또는 몰리브덴 화합물, 및/또는 하나이상의 백금 및/또는 팔라디움 화합물을 포함하는 방법.
  10. 제1항 내지 제9항중 어느 하나에 있어서, 촉매 B의 베드에서 효력있는 반응조건이 280-450℃, 수소(부분)압력 25-200바아, 공간 속도 0.3-5kg/l.h, 및 가스/공급원료 비 100-300Nl/kg인 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019880012462A 1987-09-29 1988-09-27 탄화수소성 공급원료의 전환 방법 KR970001188B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB878722840A GB8722840D0 (en) 1987-09-29 1987-09-29 Converting hydrocarbonaceous feedstock
GB8722840 1987-09-29

Publications (2)

Publication Number Publication Date
KR890005248A true KR890005248A (ko) 1989-05-13
KR970001188B1 KR970001188B1 (ko) 1997-01-29

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ID=10624514

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019880012462A KR970001188B1 (ko) 1987-09-29 1988-09-27 탄화수소성 공급원료의 전환 방법

Country Status (9)

Country Link
EP (1) EP0310164B1 (ko)
JP (1) JP2619701B2 (ko)
KR (1) KR970001188B1 (ko)
AU (1) AU601871B2 (ko)
BR (1) BR8804989A (ko)
CA (1) CA1337121C (ko)
DE (1) DE3862731D1 (ko)
GB (1) GB8722840D0 (ko)
IN (1) IN171775B (ko)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100379911B1 (ko) * 2000-07-07 2003-04-14 주식회사 우양코리아 미강 정제방법
KR20030085930A (ko) * 2002-05-02 2003-11-07 김원복 미강 정제방법

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5232578A (en) * 1991-04-09 1993-08-03 Shell Oil Company Multibed hydrocracking process utilizing beds with disparate particle sizes and hydrogenating metals contents
EP0671457A3 (en) * 1994-03-07 1996-03-13 Shell Int Research Hydrocracking process for a hydrocarbon feedstock.
US7192900B2 (en) 2002-11-27 2007-03-20 Shell Oil Company Hydrocracking catalyst
US7611689B2 (en) 2004-09-24 2009-11-03 Shell Oil Company Faujasite zeolite, its preparation and use in hydrocracking
RU2540071C2 (ru) 2009-04-29 2015-01-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Катализатор гидрокрекинга
WO2011067258A1 (en) 2009-12-03 2011-06-09 Shell Internationale Research Maatschappij B.V. Faujasite zeolite preparation process
WO2012035004A2 (en) 2010-09-17 2012-03-22 Shell Internationale Research Maatschappij B.V. Hydrocracking catalyst composition
US10226766B2 (en) 2011-12-23 2019-03-12 Shell Oil Company Process for preparing hydrocracking catalyst compositions
US10864503B2 (en) 2012-09-17 2020-12-15 Shell Oil Company Process for the preparation of a hydrocracking catalyst
US10563130B2 (en) 2014-07-17 2020-02-18 Sabic Global Technologies B.V. Upgrading hydrogen deficient streams using hydrogen donor streams in a hydropyrolysis process

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3730878A (en) * 1971-03-04 1973-05-01 Universal Oil Prod Co Hydrocarbon conversion catalyst
BE789645A (nl) * 1971-10-13 1973-04-04 Shell Int Research Werkwijze voor het regenereren van een gedesactiveerde hydrokraakkatalysator
US3853742A (en) * 1971-10-20 1974-12-10 Union Oil Co Selective midbarrel hydrocracking
BE793384A (fr) * 1971-12-27 1973-06-27 Texaco Development Corp Procede d'hydrocracking pour la conversion des hydrocarbures lourds en essence a faible teneur en soufre
US4211634A (en) * 1978-11-13 1980-07-08 Standard Oil Company (Indiana) Two-catalyst hydrocracking process
US4517073A (en) * 1982-08-09 1985-05-14 Union Oil Company Of California Hydrocracking process and catalyst therefor
US4435275A (en) * 1982-05-05 1984-03-06 Mobil Oil Corporation Hydrocracking process for aromatics production

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100379911B1 (ko) * 2000-07-07 2003-04-14 주식회사 우양코리아 미강 정제방법
KR20030085930A (ko) * 2002-05-02 2003-11-07 김원복 미강 정제방법

Also Published As

Publication number Publication date
BR8804989A (pt) 1989-05-02
IN171775B (ko) 1993-01-02
GB8722840D0 (en) 1987-11-04
JP2619701B2 (ja) 1997-06-11
EP0310164A1 (en) 1989-04-05
JPH01115994A (ja) 1989-05-09
AU2285688A (en) 1989-04-06
EP0310164B1 (en) 1991-05-08
KR970001188B1 (ko) 1997-01-29
DE3862731D1 (de) 1991-06-13
AU601871B2 (en) 1990-09-20
CA1337121C (en) 1995-09-26

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