KR930003960A - Y-형의 변형된 제올라이트 및 결합제로 구성되는 촉매 조성물 및 y-형 변형된 제올라이트를 제조하는 방법 - Google Patents

Y-형의 변형된 제올라이트 및 결합제로 구성되는 촉매 조성물 및 y-형 변형된 제올라이트를 제조하는 방법 Download PDF

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KR930003960A
KR930003960A KR1019920014587A KR920014587A KR930003960A KR 930003960 A KR930003960 A KR 930003960A KR 1019920014587 A KR1019920014587 A KR 1019920014587A KR 920014587 A KR920014587 A KR 920014587A KR 930003960 A KR930003960 A KR 930003960A
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zeolite
catalyst composition
alkaline compound
type
solution
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KR1019920014587A
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KR100218227B1 (ko
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헨드 리크 클라진가 아안
마리어 반 베크헬 잉그리드
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알베르투스 빌헬무스 요아네스 쩨스트 라텐
셀 인터나쵸 나아레 레사아치 마아츠샤피 비이부이
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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
    • B01J29/08—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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • 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
    • B01J37/08—Heat treatment
    • 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
    • C10G45/54—Hydrogenation of the aromatic hydrocarbons 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
    • 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

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

내용 없음.

Description

Y-형의 변형된 제올라이트 및 결합제로 구성되는 촉매 조성물 및 Y-형 변형된 제올라이트를 제조하는 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음

Claims (17)

  1. 변형된 제올라이트가 Y-형인 제올라이트를 pH8-13인 알칼리성 화합물의 용액으로 처리함으로써 제조되는, Y-형의 변형된 제올라이트 및 결합제로 구성되는 촉매 조성물.
  2. 제1항에 있어서, Y-형의 변형된 제올라이트가 Y-형의 제올라이트를 pH9-12인 알칼리성 화합물 용액으로 처리함으로써 제조되는 촉매 조성물.
  3. 제1 또는 2항에 있어서, 알칼리성 화합물이 금속 수산화물, 질소-함유 알칼리성 화합물 또는 유기 알칼리성 화합물을 포함하는 촉매 조성물.
  4. 제1-3항중 어느 하나에 있어서, 알칼리성 화합물의 용액으로의 처리가 20-120℃의 온도에서 수행되는 촉매 조성물.
  5. 제1-4항중 어느 하나에 있어서, Y-형의 제올라이트가 15분-4시간의 시간동안 알칼리성 화합물의 용액과 접촉되는 촉매 조성물.
  6. 제1-5항중 어느 하나에 있어서, Y-형의 제올라이트가 초-안정 제올라이트 Y 또는 극초-안정 제올라이트 Y로 구성되는 촉매 조성물.
  7. 제1-6항중 어느 하나에 있어서, 결합제가 무기 산화물 또는 무기 산화물의 혼합물로 구성되는 촉매 조성물.
  8. 제1-7항중 어느 하나에 있어서, Y-형의 변형된 제올라이트가 2.435nm 이하의 단위 셀 사이즈를 가지는 촉매 조성물.
  9. 제1-8항중 어느 하나에 있어서, Y-형의 변형된 제올라이트가 4-25의 Si02/A1203몰비를 가지는 촉매 조성물.
  10. 제1-9항중 어느 하나에 있어서, 6족 금속의 적어도 하나의 수소화 성분 및/또는 8족 금속의 적어도 하나의 수소화 성분을 부가로 포함하는 촉매 조성물.
  11. 제1-10항중 어느 하나에 따른 촉매 조성물이 사용되는 수소 첨가전환 방법.
  12. Y-형의 제올라이트를 pH8-13인 알칼리성 화합물의 용액으로 처리하는 것으로 구성되는 Y-형의 변형된 제올라이트의 제조 방법.
  13. 제12항에 있어서, 용액이 pH9-12를 가지는 방법.
  14. 제12 또는 13항에 있어서, 알칼리성 화합물이 금속 수산화물, 질소-함유 알칼리성 화합물 또는 유기 알칼리성 화합물인 방법.
  15. 제12-14항중 어느 하나에 있어서, 알칼리성 화합물의 용액으로의 처리가 20-120℃의 온도에서 수행되는 방법.
  16. 제12-15항중 어느 하나에 있어서, Y-형의 제올라이트가 15분-4시간의 시간동안 알칼리성 화합물의 용액과 접촉되는 방법.
  17. 제12-16항에 있어서, Y-형의 제올라이트가 초-안정 제올라이트 Y 또는 극초-안정 제올라이트 Y로 구성되는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개되는 것임.
KR1019920014587A 1991-08-16 1992-08-13 Y-형의 변형된 제올라이트 및 결합제로 구성되는 촉매조성물 및 y-형 변형된 제올라이트를 제조하는 방법 KR100218227B1 (ko)

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EP91202105 1991-08-16
EP91202105.2 1991-08-16

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KR100218227B1 KR100218227B1 (ko) 1999-09-01

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EP (1) EP0528494B1 (ko)
JP (1) JPH05192581A (ko)
KR (1) KR100218227B1 (ko)
CN (1) CN1082832C (ko)
AT (1) ATE122929T1 (ko)
AU (1) AU653421B2 (ko)
CA (1) CA2076187A1 (ko)
DE (1) DE69202649T2 (ko)
DK (1) DK0528494T3 (ko)
ES (1) ES2072696T3 (ko)
TW (1) TW223029B (ko)
ZA (1) ZA926128B (ko)

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US7585405B2 (en) 2005-11-04 2009-09-08 Uop Llc Hydrocracking catalyst containing beta and Y zeolites, and process for its use to make jet fuel or distillate
US7510645B2 (en) 2005-11-04 2009-03-31 Uop Llc Hydrocracking catalyst containing beta and Y zeolites, and process for its use to produce naphtha
CN101722022B (zh) * 2008-10-10 2012-01-25 中国石油天然气集团公司 Y型分子筛的碱处理改性方法
FR2952379B1 (fr) * 2009-11-10 2012-05-11 Inst Francais Du Petrole Procede d'hydrocraquage mettant en oeuvre une zeolithe modifiee par un traitement basique
FR2969510B1 (fr) 2010-12-23 2014-06-13 Total Raffinage Marketing Procede de preparation d'un catalyseur industriel d'hydroconversion, catalyseur ainsi obtenu et son utilisation dans un procede d'hydroconversion
KR101996329B1 (ko) 2011-10-24 2019-07-04 토탈 라피나쥬 프랑스 수소첨가전환 촉매의 제조방법, 이에 따라 제조된 촉매 및 수소첨가전환 공정에서의 이의 용도
CN103930206A (zh) 2011-10-24 2014-07-16 道达尔炼油法国 用于制备包含介孔的催化剂的方法、由此获得的催化剂及其在加氢转化方法中的用途
CN103889572B (zh) 2011-10-24 2017-02-15 道达尔炼油法国 用于制备介孔化催化剂的方法、由此获得的催化剂及其在催化工艺中的用途
KR101384479B1 (ko) 2012-08-24 2014-04-10 한국화학연구원 중형 세공을 갖는 제올라이트의 제조방법
CN106669812B (zh) * 2015-11-09 2019-08-06 中国石油化工股份有限公司 生产低凝点尾油的加氢裂化催化剂及其制备方法
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CN106669808B (zh) * 2015-11-09 2020-02-14 中国石油化工股份有限公司 一种生产低凝点加氢裂化尾油的催化剂制备方法
CN107344103B (zh) * 2016-05-05 2020-07-07 中国石油化工股份有限公司 一种最大量生产优质乙烯原料的加氢裂化催化剂及其制备方法和应用
CN107344115B (zh) * 2016-05-05 2020-01-10 中国石油化工股份有限公司 一种改性Y-Beta复合分子筛及其制备方法和应用
CN107344112B (zh) * 2016-05-05 2020-02-14 中国石油化工股份有限公司 一种生产优质催化重整原料的加氢裂化催化剂及其制备方法和应用
CN107344111B (zh) * 2016-05-05 2020-04-14 中国石油化工股份有限公司 最大量生产低凝柴油的加氢裂化催化剂及其制备方法和应用
CN107344113B (zh) * 2016-05-05 2020-01-10 中国石油化工股份有限公司 一种生产高芳潜石脑油的加氢裂化催化剂及其制备方法和应用
CN107344110B (zh) * 2016-05-05 2020-04-10 中国石油化工股份有限公司 用于生产低直链烷烃含量加氢裂化尾油的催化剂及其制备方法和应用
CN107344104B (zh) * 2016-05-05 2020-01-10 中国石油化工股份有限公司 一种生产优质乙烯原料的加氢裂化催化剂及其制备方法和应用
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EP0528494A1 (en) 1993-02-24
EP0528494B1 (en) 1995-05-24
CN1082832C (zh) 2002-04-17
ES2072696T3 (es) 1995-07-16
CN1069427A (zh) 1993-03-03
KR100218227B1 (ko) 1999-09-01
DK0528494T3 (da) 1995-07-17
TW223029B (ko) 1994-05-01
DE69202649D1 (de) 1995-06-29
ZA926128B (en) 1993-04-28
ATE122929T1 (de) 1995-06-15
AU653421B2 (en) 1994-09-29
CA2076187A1 (en) 1993-02-17
DE69202649T2 (de) 1995-10-26
AU2104992A (en) 1993-02-18
JPH05192581A (ja) 1993-08-03

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