KR910001001A - 탄화수소성 공급원료의 전환 방법 - Google Patents

탄화수소성 공급원료의 전환 방법 Download PDF

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KR910001001A
KR910001001A KR1019890008210A KR890008210A KR910001001A KR 910001001 A KR910001001 A KR 910001001A KR 1019890008210 A KR1019890008210 A KR 1019890008210A KR 890008210 A KR890008210 A KR 890008210A KR 910001001 A KR910001001 A KR 910001001A
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South Korea
Prior art keywords
feedstock
zeolite
temperature
process according
catalyst
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KR1019890008210A
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KR0132055B1 (ko
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어니스트 맥스웰 이안
코르넬리스 민터하우트 요하네스
Original Assignee
오노 알버어스
셀 인터나쵸나아레 레사아치 마사츠샤피 비이부이
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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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
    • C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Superconductors And Manufacturing Methods Therefor (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Glass Compositions (AREA)
  • Treatment Of Steel In Its Molten State (AREA)
  • Discharge Heating (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Magnetic Resonance Imaging Apparatus (AREA)
  • Stereophonic System (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

내용 없음

Description

탄화수소성 공급원료의 전환 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (18)

  1. 최대한 480℃온도에서 10초 이내에 0.3-0.7nm의 기공 지름을 갖는 제올라이트를 포함하는 제올라이트 촉매를 공급원료와 접촉시키는 것을 포함하는, 그 양이 적어도 330℃의 온도에서 끓는 그런 비점 범위를 갖는 탄화수소를 함유하는 탄화수소성 공급원료의 전환방법.
  2. 제1항에 있어서, 공급원료를 0.1-10, 특히 1-6초 동안 제올라이트 촉매와 접촉시키는 방법.
  3. 제1항 또는 제2항에 있어서, 온도가 280-450℃인 방법.
  4. 제3항에 있어서, 온도가 320-420℃인 방법.
  5. 제1항 내지 제4항중 어느 한 항에 있어서, 제올라이트 촉매가 0.5-.07nm의 기공 지름을 갖는 제올라이트를 포함하는 방법.
  6. 제1항 내지 제5항중 어느 한 항에 있어서, 제올라이트 촉매가 제올라이트로서 0.3-0.7nm의 기공 지름을 갖는 제올라이트만을 포함하는 방법.
  7. 제1항 내지 제6항중 어느 한 항에 있어서, 제올라이트가 ZSM-5구조를 갖는 결정성 금속 실리케이트, 페리어라이트, 에리오나이트 및 그 혼합물로 이루어진 군으로 부터 선택되는 방법.
  8. 제1항 내지 제7항중 어느 한항에 있어서, 제올라이트가 본질적으로 그 수소 형태로 있는 방법.
  9. 제1항 내지 제8항중 어느 한항에 있어서, 첨가된 수소의 부재하에 수행되는 방법.
  10. 제1항 내지 제9항중 어느 한항에 있어서, 압력이 1-10바아인 방법.
  11. 제1항 내지 제10항중 어느 한항에 있어서, 촉매/공급원료 중량비가 1-100인 방법.
  12. 제11항에 있어서, 촉매/공급원료 중량비가 2-50인 방법.
  13. 제1항 내지 제12항중 어느 한항에 있어서, 이동베드안에서 수행되는 방법.
  14. 제1항 내지 제13항중 어느 한항에 있어서, 공급원료의 적어도 50중량%가 적어도 330℃의 온도에서 끓는 그런 비점 범위를 갖는 방법.
  15. 제14항에 있어서, 공급원료가 경유 또는 진공 경유인 방법.
  16. 제1항 내지 제15항중 어느 한항에 있어서, 공급원료가 질소로서 계산된, 적어도 25ppmw의 질소 함량을 갖는 방법.
  17. 제16항에 있어서, 공급원료가 질소로서 계산된 100-1000ppmw의 질소 함량을 갖는 방법.
  18. 제1항 내지 제17항중 어느 한항의 전환방법에 의해 얻어진 탄화수소성 생성물.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019890008210A 1988-06-16 1989-06-14 탄화수소성 공급원료의 전환 방법 KR0132055B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB888814292A GB8814292D0 (en) 1988-06-16 1988-06-16 Process for conversion of hydrocarbonaceous feedstock
GB8814292.2 1988-06-16

Publications (2)

Publication Number Publication Date
KR910001001A true KR910001001A (ko) 1991-01-30
KR0132055B1 KR0132055B1 (ko) 1998-04-13

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KR1019890008210A KR0132055B1 (ko) 1988-06-16 1989-06-14 탄화수소성 공급원료의 전환 방법

Country Status (12)

Country Link
US (1) US4886934A (ko)
EP (1) EP0349036B1 (ko)
JP (1) JP2777573B2 (ko)
KR (1) KR0132055B1 (ko)
CN (1) CN1020623C (ko)
AT (1) ATE118527T1 (ko)
AU (1) AU616017B2 (ko)
CA (1) CA1333375C (ko)
DE (1) DE68921105T2 (ko)
ES (1) ES2067527T3 (ko)
GB (1) GB8814292D0 (ko)
GR (1) GR3015596T3 (ko)

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GB8904409D0 (en) * 1989-02-27 1989-04-12 Shell Int Research Process for the conversion of a hydrocarbonaceous feedstock
JPH0245593A (ja) * 1988-06-16 1990-02-15 Shell Internatl Res Maatschappij Bv 炭化水素供給原料の変換方法
GB8904408D0 (en) * 1989-02-27 1989-04-12 Shell Int Research Process for the conversion of a hydrocarbonaceous feedstock
GB8908081D0 (en) * 1989-04-11 1989-05-24 Shell Int Research Process for the conversion of a hydrocarbonaceous feedstock
US5149421A (en) * 1989-08-31 1992-09-22 Chevron Research Company Catalytic dewaxing process for lube oils using a combination of a silicoaluminophosphate molecular sieve catalyst and an aluminosilicate zeolite catalyst
US6323384B1 (en) 1991-06-05 2001-11-27 Equistar Chemicals, Lp Process for isomerizing linear olefins to isoolefins
CN1032059C (zh) * 1991-06-05 1996-06-19 莱昂德尔石油化学公司 将直链烯烃异构成异烯烃的方法
AU2003279863A1 (en) * 2002-10-08 2004-05-04 Exxonmobil Research And Engineering Company Enhanced lube oil yield by low or no hydrogen partial pressure catalytic dewaxing of paraffin wax
CN1323135C (zh) * 2004-02-27 2007-06-27 中国石油化工股份有限公司 一种含硫烃油的裂化方法
US11066606B2 (en) * 2019-11-12 2021-07-20 Saudi Arabian Oil Company Systems and methods for catalytic upgrading of vacuum residue to distillate fractions and olefins with steam

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Also Published As

Publication number Publication date
ATE118527T1 (de) 1995-03-15
JPH0245592A (ja) 1990-02-15
CA1333375C (en) 1994-12-06
DE68921105T2 (de) 1995-06-29
AU3640189A (en) 1989-12-21
KR0132055B1 (ko) 1998-04-13
AU616017B2 (en) 1991-10-17
US4886934A (en) 1989-12-12
EP0349036B1 (en) 1995-02-15
CN1038663A (zh) 1990-01-10
JP2777573B2 (ja) 1998-07-16
CN1020623C (zh) 1993-05-12
DE68921105D1 (de) 1995-03-23
GR3015596T3 (en) 1995-06-30
EP0349036A1 (en) 1990-01-03
ES2067527T3 (es) 1995-04-01
GB8814292D0 (en) 1988-07-20

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