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KR910015689A - How to convert hydrocarbonaceous feedstock - Google Patents

How to convert hydrocarbonaceous feedstock Download PDF

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Publication number
KR910015689A
KR910015689A KR1019900002434A KR900002434A KR910015689A KR 910015689 A KR910015689 A KR 910015689A KR 1019900002434 A KR1019900002434 A KR 1019900002434A KR 900002434 A KR900002434 A KR 900002434A KR 910015689 A KR910015689 A KR 910015689A
Authority
KR
South Korea
Prior art keywords
feedstock
zeolite
catalyst
seconds
pore diameter
Prior art date
Application number
KR1019900002434A
Other languages
Korean (ko)
Inventor
비스와스 제이디프
어니스트 맥스웰 이언
Original Assignee
오노 알버어스
셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
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Application filed by 오노 알버어스, 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 filed Critical 오노 알버어스
Publication of KR910015689A publication Critical patent/KR910015689A/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/16Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "moving bed" method
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G35/00Reforming naphtha
    • C10G35/04Catalytic reforming
    • C10G35/10Catalytic reforming with moving catalysts

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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)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

내용 없음No content

Description

탄화수소성 공급원료의 전환 방법How to convert hydrocarbonaceous feedstock

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

Claims (10)

10초 이하동안 480℃ 이상의 온도에서 0.3-0.7nm의 기공 직경을 가지는 제올라이트로 구성되는 제올라이트 촉매의 이동베드와 공급원료를 접촉시킴으로 구성되는, 공급원료의 양이 최소한 330℃의 온도에서 끓는 그러한 비점 범위를 가지는 탄화수소 함유 직류(直留) 탄화수소성 공급원료의 전환 방법.Such a boiling point at which the amount of feedstock boils at a temperature of at least 330 ° C., consisting of contacting the feedstock with a moving bed of a zeolite catalyst consisting of a zeolite having a pore diameter of 0.3-0.7 nm at temperatures above 480 ° C. for less than 10 seconds. A process for converting a hydrocarbon-containing direct current hydrocarbonaceous feedstock having a range. 제1항에 있어서, 공급원료가 0.2-6초 동안 제올라이트 촉매와 접촉되는 방법.The process of claim 1 wherein the feedstock is contacted with the zeolite catalyst for 0.2-6 seconds. 제1항 또는 제2항에 있어서, 온도가 550-850℃인 방법.The method according to claim 1 or 2, wherein the temperature is 550-850 ° C. 제1항 내지 제3항 중 어느 한 항에 있어서, 제올라이트가 0.5-0.7nm의 기공직경을 가지는 방법.The method of claim 1, wherein the zeolite has a pore diameter of 0.5-0.7 nm. 제1항 내지 제4항중 어느 한 항에 있어서, 제올라이트가 ZSM-5 구조를 가지는 결정성 금속 실리케이트, 페리에라이트, 에리오나이트 및 그들의 혼합물중에서 선택되는 방법.The method according to any one of claims 1 to 4, wherein the zeolite is selected from crystalline metal silicates having a ZSM-5 structure, ferrierite, erionite and mixtures thereof. 제1항 내지 제5항중 어느 한 항에 있어서, 제올라이트가 본질적으로 그의 수소형인 방법.The process according to claim 1, wherein the zeolite is essentially hydrogen type thereof. 제1항 내지 제6항중 어느 한 항에 있어서, 압력이 1-10바아인 방법.The process of claim 1, wherein the pressure is 1-10 bar. 제1항 내지 제7항중 어느 한 항에 있어서, 촉매/공급원료 중량비가 20-100 : 1인 방법.The process according to claim 1, wherein the catalyst / feedstock weight ratio is 20-100: 1. 제1항 내지 제8항중 어느 한 항에 있어서, 공급원료가 가스오일인 방법.The method of claim 1, wherein the feedstock is a gas oil. 제1항 내지 제9항중 어느 한항의 방법에 의해 얻어지는, 탄화수소성 생성물 또는 그들의 분별물.A hydrocarbonaceous product or fractions thereof obtained by the method of any one of claims 1 to 9. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019900002434A 1989-02-27 1990-02-26 How to convert hydrocarbonaceous feedstock KR910015689A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB898904408A GB8904408D0 (en) 1989-02-27 1989-02-27 Process for the conversion of a hydrocarbonaceous feedstock
GB8904408.5 1989-02-27

Publications (1)

Publication Number Publication Date
KR910015689A true KR910015689A (en) 1991-09-30

Family

ID=10652368

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019900002434A KR910015689A (en) 1989-02-27 1990-02-26 How to convert hydrocarbonaceous feedstock

Country Status (11)

Country Link
EP (1) EP0385538B1 (en)
JP (1) JPH02276888A (en)
KR (1) KR910015689A (en)
CN (1) CN1019981C (en)
AU (1) AU628929B2 (en)
BR (1) BR9000880A (en)
CA (1) CA2009986A1 (en)
DE (1) DE69009234T2 (en)
ES (1) ES2056362T3 (en)
GB (1) GB8904408D0 (en)
RU (1) RU2017791C1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9026775D0 (en) * 1990-12-10 1991-01-30 Shell Int Research Process for the preparation of an olefins-containing mixture of hydrocarbons
GB9114390D0 (en) * 1991-07-03 1991-08-21 Shell Int Research Hydrocarbon conversion process and catalyst composition
US6835863B2 (en) 1999-07-12 2004-12-28 Exxonmobil Oil Corporation Catalytic production of light olefins from naphtha feed
US6222087B1 (en) 1999-07-12 2001-04-24 Mobil Oil Corporation Catalytic production of light olefins rich in propylene
EP1195424A1 (en) * 2000-10-05 2002-04-10 ATOFINA Research A process for cracking an olefin-rich hydrocarbon feedstock
DE102012006992A1 (en) * 2012-04-05 2013-10-10 Linde Aktiengesellschaft Process for the separation of olefins with mild cleavage
US10689586B2 (en) 2015-12-21 2020-06-23 Sabic Global Technologies B.V. Methods and systems for producing olefins and aromatics from coker naphtha

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3856659A (en) * 1972-12-19 1974-12-24 Mobil Oil Corp Multiple reactor fcc system relying upon a dual cracking catalyst composition
US4514285A (en) * 1983-03-23 1985-04-30 Texaco Inc. Catalytic cracking system
US4985136A (en) * 1987-11-05 1991-01-15 Bartholic David B Ultra-short contact time fluidized catalytic cracking process
GB8814292D0 (en) * 1988-06-16 1988-07-20 Shell Int Research Process for conversion of hydrocarbonaceous feedstock
EP0347003B1 (en) * 1988-06-16 1996-05-08 Shell Internationale Researchmaatschappij B.V. Process for the conversion of a hydrocarbonaceous feedstock
NL8801653A (en) * 1988-06-29 1990-01-16 Stork Kwant Bv OPERATING SYSTEM.
GB8828206D0 (en) * 1988-12-02 1989-01-05 Shell Int Research Process for conversion of hydrocarbonaceous feedstock

Also Published As

Publication number Publication date
CN1045120A (en) 1990-09-05
EP0385538A1 (en) 1990-09-05
BR9000880A (en) 1991-02-13
CN1019981C (en) 1993-03-03
RU2017791C1 (en) 1994-08-15
AU628929B2 (en) 1992-09-24
AU5014990A (en) 1990-08-30
EP0385538B1 (en) 1994-06-01
GB8904408D0 (en) 1989-04-12
JPH02276888A (en) 1990-11-13
DE69009234T2 (en) 1994-11-24
ES2056362T3 (en) 1994-10-01
CA2009986A1 (en) 1990-08-27
DE69009234D1 (en) 1994-07-07

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