KR880012733A - Hydrogen Cracking Catalyst to Produce Medium Oil - Google Patents

Hydrogen Cracking Catalyst to Produce Medium Oil Download PDF

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Publication number
KR880012733A
KR880012733A KR870004047A KR870004047A KR880012733A KR 880012733 A KR880012733 A KR 880012733A KR 870004047 A KR870004047 A KR 870004047A KR 870004047 A KR870004047 A KR 870004047A KR 880012733 A KR880012733 A KR 880012733A
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KR
South Korea
Prior art keywords
modified
zeolite
catalyst
unit cell
cell size
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Application number
KR870004047A
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Korean (ko)
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KR900004505B1 (en
Inventor
제트.스타이글레더 카알
Original Assignee
원본미기재
유오피 인코오포레이티드
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Priority to KR1019870004047A priority Critical patent/KR900004505B1/en
Publication of KR880012733A publication Critical patent/KR880012733A/en
Application granted granted Critical
Publication of KR900004505B1 publication Critical patent/KR900004505B1/en

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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
    • C10G45/44—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
    • 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

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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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

내용 없음No content

Description

중간 유분을 생성하는 수소화 크래킹 촉매Hydrogen Cracking Catalyst to Produce Medium Oil

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

Claims (6)

제1변형 Y 제올라이트 성분을 함유한 지지체를 지닌 촉매 유효양의 수소화 성분을 내화 무기 산화물 매트릭스와 혼합하는 것으로 구성되며, 상기 변형된 Y 제올라이트 성분은 24.20 내지 24.35Å의 단위 셀 크기를 갖는 수소와 크래킹 촉매에 있어서, 내화 무기 산화물 매트릭스와 함께 제2변형 Y 제올라이트 성분을 사용하며, 상기 제2변형 Y 제올라이트 성분은 24.20 내지 24.35Å의 단위 셀 크기를 지니며, 상기 제1 및 제2변형 Y-제올라이트 성분의 단위 셀 크기는 적어도 0.1Å만큼 차이나는 것을 특징으로 하는 수소화 크래킹 촉매.Consisting of mixing a catalytically effective amount of a hydrogenation component having a support containing a first modified Y zeolite component with a refractory inorganic oxide matrix, wherein the modified Y zeolite component is cracked with hydrogen having a unit cell size of 24.20 to 24.35 mm 3 In the catalyst, a second modified Y zeolite component is used together with a refractory inorganic oxide matrix, the second modified Y zeolite component having a unit cell size of 24.20 to 24.35 mm 3, and wherein the first and second modified Y-zeolites Hydrogen cracking catalyst, characterized in that the unit cell size of the components differ by at least 0.1 kPa. 제 1항에 있어서, 제1변형 Y 제올라이트 대 제2변형 제올라이트이 중량비는 0.1:1 내지 10:1인 것을 특징으로 하는 촉매.The catalyst of claim 1 wherein the first modified Y zeolite to second modified zeolite have a weight ratio of 0.1: 1 to 10: 1. 제 1항에 있어서, 제1변형 Y 제올라이트는 약 24.25Å의 평균 단위 셀 크기를 가지며, 제 2변형 Y제올라이트는 24.35Å의 평균 단위 셀 크기를 갖는 것을 특징으로 하는 촉매.The catalyst of claim 1 wherein the first modified Y zeolite has an average unit cell size of about 24.25 mm 3 and the second modified Y zeolite has an average unit cell size of 24.35 mm 3. 제 1항에 있어서, 상기 제 1변형 Y 제올라이트는 1.0 내지 20.0중량%의 함량으로 존재하며, 제 2변형 Y 제올라이트는 약 1.0 내지 20.0중량%의 함량으로 존재하는 것을 특징으로 하는 촉매.The catalyst of claim 1, wherein the first modified Y zeolite is present in an amount of 1.0 to 20.0 wt%, and the second modified Y zeolite is present in an amount of about 1.0 to 20.0 wt%. 149 내지 371℃의 비점을 지닌 중간 유분 생성물을 선택적으로 산출하도록 조절된 수소화 크래킹 조건하에서 제1항 내지 제4항중 어느 한항에 따른 촉매를 고비점의 탄화수소 원료와 접촉시키는 것으로 구성되는 수소화 크래킹 방법.A process for hydrocracking consisting of contacting a catalyst according to any one of claims 1 to 4 with a high boiling point hydrocarbon feed under a hydrogenated cracking condition adapted to selectively yield an intermediate fraction product having a boiling point of 149 to 371 ° C. 제5항에 있어서, 상기 수소화 크래킹 조건은 93 내지 815℃의 온도, 대기압 내지 약 20685kPagage의 압력 및 0.1 내지 15hr-1의 시간당 액체 공간속도(LHSV)인 것을 특징으로 하는 수소화 크래킹 방법.6. The method of claim 5, wherein said hydrogenation cracking conditions are temperatures of 93 to 815 [deg.] C., atmospheric pressure to pressure of about 20685 kPagage, and liquid hourly space velocity (LHSV) of 0.1 to 15hr -1 . ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019870004047A 1987-04-27 1987-04-27 Middle distillate producing hydrocracking catalyst KR900004505B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019870004047A KR900004505B1 (en) 1987-04-27 1987-04-27 Middle distillate producing hydrocracking catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019870004047A KR900004505B1 (en) 1987-04-27 1987-04-27 Middle distillate producing hydrocracking catalyst

Publications (2)

Publication Number Publication Date
KR880012733A true KR880012733A (en) 1988-11-28
KR900004505B1 KR900004505B1 (en) 1990-06-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019870004047A KR900004505B1 (en) 1987-04-27 1987-04-27 Middle distillate producing hydrocracking catalyst

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100504448B1 (en) * 1996-10-22 2005-10-31 앵스띠뛰 프랑세 뒤 뻬뜨롤 Dehydrogenated Distillation of Petroleum Oil Using a Catalyst Containing Dealuminated Two or More Y Zeolites

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AR052122A1 (en) * 2004-11-05 2007-03-07 Grace W R & Co CATALYZERS FOR LIGHT OLEFINS AND LPG GAS LICUATED PETROLEUM IN FLUIDIZED CATALITICAL CRACHING UNITS
JP5940935B2 (en) * 2012-08-17 2016-06-29 日揮触媒化成株式会社 Hydrocarbon catalytic cracking catalyst

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100504448B1 (en) * 1996-10-22 2005-10-31 앵스띠뛰 프랑세 뒤 뻬뜨롤 Dehydrogenated Distillation of Petroleum Oil Using a Catalyst Containing Dealuminated Two or More Y Zeolites

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Publication number Publication date
KR900004505B1 (en) 1990-06-28

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