KR850003428A - 탄화수소 유분을 수소화 분해하고 수소화 탈납하는 촉매 및 방법 - Google Patents

탄화수소 유분을 수소화 분해하고 수소화 탈납하는 촉매 및 방법 Download PDF

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Publication number
KR850003428A
KR850003428A KR1019840006352A KR840006352A KR850003428A KR 850003428 A KR850003428 A KR 850003428A KR 1019840006352 A KR1019840006352 A KR 1019840006352A KR 840006352 A KR840006352 A KR 840006352A KR 850003428 A KR850003428 A KR 850003428A
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South Korea
Prior art keywords
catalyst
zeolite
component
catalyst according
hydrocarbon fraction
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KR1019840006352A
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English (en)
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KR910008565B1 (ko
Inventor
미챌 올렉크 스테펜 (외 1)
Original Assignee
에드워드 에취. 발란스
모빌 오일 코오포레이숀
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Priority claimed from US06/541,763 external-priority patent/US4486296A/en
Application filed by 에드워드 에취. 발란스, 모빌 오일 코오포레이숀 filed Critical 에드워드 에취. 발란스
Publication of KR850003428A publication Critical patent/KR850003428A/ko
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    • 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
    • B01J29/80—Mixtures of different zeolites
    • 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
    • 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
    • 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
    • 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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • 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
    • B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
    • B01J29/7007—Zeolite Beta

Abstract

내용 없음

Description

탄화수소 유분을 수소화 분해하고 수소화 탈납하는 촉매 및 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 촉매 A와 B에 대한 165-340℃의 유분수율을 비교한 그래프. 제2도는 3개의 촉매 A, B 및 C의 활성을 비교한 그래프.

Claims (13)

  1. 제올라이트 X, 제올라이트 Y, 산성 제올라이트 Y 및 천연이나 기타 합성 피서사이트로부터 선택한 1 이상의 제올라이트 (ㄱ); 제올라이트 베타, (ㄴ); 수소화금속 (ㄷ)의 혼합물로 구성됨을 특징으로 하는 탄화수소 유분을 수소화 분해하고 수소화 탈납하는 촉매.
  2. 제1항에 있어서, (ㄱ), (ㄴ) 및 (ㄷ)의 총 중량을 (ㄱ)의 5-20%를 함유함을 특징으로 하는 촉매.
  3. 제1항 또는 제2항에 있어서, (ㄱ), (ㄴ) 및 (ㄷ)의 총 중량을 기준으로 한 (ㄴ)의 20-60%를 함유함을 특징으로 하는 촉매.
  4. 제1항 내지 제3항중 어느 한 항에 있어서, (ㄱ), (ㄴ) 및 (ㄷ)의 총 중량을 기준으로한 (ㄷ)의 0.1-30%를 함유함을 특징으로 하는 촉매.
  5. 제1항 내지 제4항중 어느 한 항에 있어서, 성분 (ㄱ)이 제올라이트 Y임을 특징으로 하는 촉매.
  6. 제5항에 있어서, 성분 (ㄱ)이 극도로 안정한 제올라이트 Y임을 특징으로 하는 촉매.
  7. 제5항 또는 제6항에 있어서, 성분 (ㄱ)이 희토류로 교환한 제올라이트 Y임을 특징으로 하는 촉매.
  8. 제1항 내지 제7항중 어느 한 항에 있어서, 성분 (ㄴ)은 실리카 : 알루미나의 몰비가 10-500인 제올라이트 베타임을 특징으로 하는 촉매.
  9. 제8항에 있어서, 제올라이트 베타의 실리카 : 알루미나의 몰비가 20-50임을 특징으로 하는 촉매.
  10. 제1항 내지 제9항중 어느 한 항에 있어서, 성분 (ㄷ)이 주기율표 6A족 및 8족의 금속 1이상임을 특징으로 하는 촉매.
  11. 제10항에 있어서, 성분 (ㄷ)이 텅스텐, 몰리브데늄, 닉켈, 니켈, 크롬 또는 이들의 산화물이나 황화물, 또는 백금, 팔라듐, 이리듐 또는 로듐, 이들중 2이상의 혼합물임을 특징으로 하는 촉매.
  12. 제1항 내지 제11항중 어느 한 항에 있어서, 다공성 매트릭스 물질로 구성됨을 특징으로 하는 방법.
  13. 230-500℃의 온도, 790-20800kPa의 압력 및 0.1-20LHSV의 공간속도에서 탄화수소유분을, 수소/탄화수소의 비율이 18-3500NIH2/ℓ인 수소와 접촉시키고 제1항 내지 제12항중 어느 한 항에 의한 촉매와 접촉시킴을 특징으로 하는 탄화수소유분을 수소화 분해하고 수소화 탈납하는 방법
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019840006352A 1983-10-13 1984-10-13 탄화수소 유분을 수소화 분해하고 수소화 탈납하는 촉매 및 방법 KR910008565B1 (ko)

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
US54176483A 1983-10-13 1983-10-13
US06/541,763 US4486296A (en) 1983-10-13 1983-10-13 Process for hydrocracking and dewaxing hydrocarbon oils
US541,763 1983-10-13
US541763 1983-10-13
US541764 1983-10-13
US541,764 1983-10-13

Publications (2)

Publication Number Publication Date
KR850003428A true KR850003428A (ko) 1985-06-17
KR910008565B1 KR910008565B1 (ko) 1991-10-19

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019840006352A KR910008565B1 (ko) 1983-10-13 1984-10-13 탄화수소 유분을 수소화 분해하고 수소화 탈납하는 촉매 및 방법

Country Status (5)

Country Link
EP (1) EP0140608B1 (ko)
KR (1) KR910008565B1 (ko)
AU (1) AU573630B2 (ko)
CA (1) CA1226268A (ko)
DE (1) DE3463002D1 (ko)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4797195A (en) * 1988-02-26 1989-01-10 Amoco Corporation Three zone hydrocracking process
US5279726A (en) * 1990-05-22 1994-01-18 Union Oil Company Of California Catalyst containing zeolite beta and processes for its use
US5350501A (en) * 1990-05-22 1994-09-27 Union Oil Company Of California Hydrocracking catalyst and process
CA2113896C (en) * 1991-07-24 2004-02-24 Minas Robert Apelian Production of hydrocracked lubricants
ZA956008B (en) * 1994-07-21 1996-02-22 Shell Int Research Catalyst use thereof and process for preparation thereof
US6133186A (en) * 1997-03-06 2000-10-17 Shell Oil Company Process for the preparation of a catalyst composition
DE19751875C2 (de) * 1997-11-22 2001-07-05 Karlsruhe Forschzent Herzkatheter mit Messung der Anpreßkraft
DK2424661T3 (da) 2009-04-29 2021-03-08 Pq Corp Zeolit y
WO2014177429A1 (en) * 2013-05-03 2014-11-06 Haldor Topsøe A/S Catalyst and process for dewaxing of hydrocarbons

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3758402A (en) * 1970-10-06 1973-09-11 Mobil Oil Corp Catalytic hydrocracking of hydrocarbons
US3764529A (en) * 1972-02-17 1973-10-09 Matsushita Electric Ind Co Ltd Method of manufacturing fine grain ceramic barium titanate
US3923641A (en) * 1974-02-20 1975-12-02 Mobil Oil Corp Hydrocracking naphthas using zeolite beta
NZ204093A (en) * 1982-05-18 1985-01-31 Mobil Oil Corp Simultaneous catalytic hydrocracking and hydrodewaxing of hydrocarbon oils using zeolite beta
DE3366278D1 (en) * 1982-08-09 1986-10-23 Mobil Oil Corp A process and catalyst composition for upgrading a hydrocarbon feedstock

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Publication number Publication date
DE3463002D1 (en) 1987-05-14
EP0140608A1 (en) 1985-05-08
KR910008565B1 (ko) 1991-10-19
AU3414084A (en) 1985-04-18
CA1226268A (en) 1987-09-01
AU573630B2 (en) 1988-06-16
EP0140608B1 (en) 1987-04-08

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