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WO1995027019A1 - Procede et appareil permettant de produire des olefines legeres - Google Patents

Procede et appareil permettant de produire des olefines legeres Download PDF

Info

Publication number
WO1995027019A1
WO1995027019A1 PCT/FI1995/000177 FI9500177W WO9527019A1 WO 1995027019 A1 WO1995027019 A1 WO 1995027019A1 FI 9500177 W FI9500177 W FI 9500177W WO 9527019 A1 WO9527019 A1 WO 9527019A1
Authority
WO
WIPO (PCT)
Prior art keywords
catalyst
fluidized bed
regenerator
reactor
circulating fluidized
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/FI1995/000177
Other languages
English (en)
Inventor
Jyrki Hiltunen
Krister Fagerstolt
Outi Krause
Kari KÄÄRIÄINEN
Seppo Ruottu
Ari Halme
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Neste Oyj
Original Assignee
Neste Oyj
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.)
Filing date
Publication date
Application filed by Neste Oyj filed Critical Neste Oyj
Priority to KR1019960705409A priority Critical patent/KR100281750B1/ko
Priority to JP7525430A priority patent/JPH09511535A/ja
Priority to AU21396/95A priority patent/AU2139695A/en
Priority to DE69518407T priority patent/DE69518407T2/de
Priority to RU96119940A priority patent/RU2125079C1/ru
Priority to EP95914373A priority patent/EP0753037B1/fr
Priority to CA002186744A priority patent/CA2186744C/fr
Publication of WO1995027019A1 publication Critical patent/WO1995027019A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • 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
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/22—Higher olefins

Landscapes

  • 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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

L'invention concerne un procédé et un appareil permettant la conversion catalytique d'hydrocarbures en oléfines légères au moyen d'un système de réacteur à lit fluidisé circulant et à court temps de contact. Le procédé présenté comprend les étapes suivantes: introduction d'une charge d'hydrocarbures dans une zone de réaction (1) contenant un catalyseur solide; mise en contact de la charge d'hydrocarbure se trouvant dans la zone de réaction (1) avec le catalyseur, dans des conditions qui favorisent la conversion catalytique d'hydrocarbures en oléfines légères; séparation des produits de réaction obtenus dans la zone de réaction (1) après conversion catalytique; récupération du catalyseur; et régénération du catalyseur désactivé dans un régénérateur (3). Selon l'invention, la charge d'hydrocarbure est mise en contact avec le catalyseur dans un réacteur à lit fluidisé circulant (1), avec un temps de séjour compris entre 0,1 et 3 secondes. On met en oeuvre ledit procédé pour produire du propylène, des butylènes et des pentènes, ainsi qu'une fraction d'essence à indice d'octane élevé et à faible teneur en benzène, par conversion catalytique de gazole léger, de gazole lourd, de gazole sous vide ou de naphta, au moyen de catalyseurs améliorés ou classiques de craquage catalytique à lit fluidisé. On peut également faire appel à ce procédé pour obtenir des produits riches en propylène, isobutylène ou isoamylène par déshydrogénation catalytique, à partir, respectivement, de propane, d'isobutane ou de naphta, au moyen de catalyseurs classiques ou améliorés destinés à l'utilisation en lit fluidisé.
PCT/FI1995/000177 1994-03-31 1995-03-31 Procede et appareil permettant de produire des olefines legeres Ceased WO1995027019A1 (fr)

Priority Applications (7)

Application Number Priority Date Filing Date Title
KR1019960705409A KR100281750B1 (ko) 1994-03-31 1995-03-31 저분자량 올레핀을 제조하는 방법 및 장치
JP7525430A JPH09511535A (ja) 1994-03-31 1995-03-31 軽質オレフィンの製造方法および装置
AU21396/95A AU2139695A (en) 1994-03-31 1995-03-31 Process and apparatus for producing light olefins
DE69518407T DE69518407T2 (de) 1994-03-31 1995-03-31 Verfahren und vorrichtung zur herstellung von leichten olefinen
RU96119940A RU2125079C1 (ru) 1994-03-31 1995-03-31 Способ и устройство для получения легких олефинов
EP95914373A EP0753037B1 (fr) 1994-03-31 1995-03-31 Procede et appareil permettant de produire des olefines legeres
CA002186744A CA2186744C (fr) 1994-03-31 1995-03-31 Procede et appareil permettant de produire des olefines legeres

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI941528A FI98529C (fi) 1994-03-31 1994-03-31 Menetelmä ja laitteisto keveiden olefiinien valmistamiseksi
FI941528 1994-03-31

Publications (1)

Publication Number Publication Date
WO1995027019A1 true WO1995027019A1 (fr) 1995-10-12

Family

ID=8540434

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FI1995/000177 Ceased WO1995027019A1 (fr) 1994-03-31 1995-03-31 Procede et appareil permettant de produire des olefines legeres

Country Status (11)

Country Link
EP (1) EP0753037B1 (fr)
JP (1) JPH09511535A (fr)
KR (1) KR100281750B1 (fr)
CN (1) CN1124330C (fr)
AU (1) AU2139695A (fr)
CA (1) CA2186744C (fr)
DE (1) DE69518407T2 (fr)
ES (1) ES2149976T3 (fr)
FI (1) FI98529C (fr)
RU (1) RU2125079C1 (fr)
WO (1) WO1995027019A1 (fr)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6200534B1 (en) 1996-08-30 2001-03-13 Fortum Oil And Gas Oy Apparatus for chemical and physical processes
US6538169B1 (en) 2000-11-13 2003-03-25 Uop Llc FCC process with improved yield of light olefins
KR100473986B1 (ko) * 2001-11-01 2005-03-07 서곤 Ｆｃｃ 공정 폐촉매로부터 폐고분자 물질의 액상 분해용촉매의 제조방법 및 이 촉매를 이용한 폐고분자 물질의분해방법
RU2283339C2 (ru) * 2001-07-06 2006-09-10 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом сырья, полученного синтезом фишера-тропша, и установка для его осуществления
RU2283857C2 (ru) * 2001-07-06 2006-09-20 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом тяжелой фракции из продуктов, полученных способом фишера-тропша, и устройство для его осуществления
RU2283858C2 (ru) * 2001-07-06 2006-09-20 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом двух фракций продуктов, полученных синтезом фишера-тропша, и установка для его осуществления
RU2291184C2 (ru) * 2001-07-06 2007-01-10 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом в две стадии сырья, полученного синтезом фишера-тропша, и установка для его осуществления
US7935314B2 (en) 2008-09-30 2011-05-03 Uop Llc Apparatus for mixing regenerated and carbonized catalyst
US20110137101A1 (en) * 2009-12-09 2011-06-09 Uop Llc Process for the Production of Propylene
US8323477B2 (en) 2008-09-30 2012-12-04 Uop Llc Process for mixing regenerated and carbonized catalyst
WO2023098843A1 (fr) * 2021-12-03 2023-06-08 中国石油化工股份有限公司 Réacteur de craquage catalytique, système et application
US11981633B2 (en) 2018-08-03 2024-05-14 Neste Oyj Method to produce bio-renewable propylene from oils and fats

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040064007A1 (en) * 2002-09-30 2004-04-01 Beech James H. Method and system for regenerating catalyst from a plurality of hydrocarbon conversion apparatuses
US20050101814A1 (en) * 2003-11-07 2005-05-12 Foley Timothy D. Ring opening for increased olefin production
US7442739B1 (en) 2003-11-12 2008-10-28 Henkel Corporation Hot melt pressure sensitive adhesives
CA2576329A1 (fr) * 2004-08-10 2006-02-23 Shell Internationale Research Maatschappij B.V. Methode et appareillage permettant d'obtenir un distillat moyen et des olefines legeres a partir d'une charge d'hydrocarbures
US8888992B2 (en) * 2005-08-09 2014-11-18 Uop Llc Process and apparatus for improving flow properties of crude petroleum
KR100651329B1 (ko) * 2005-10-07 2006-11-30 에스케이 주식회사 탄화수소 원료로부터 경질 올레핀을 제조하는 공정
KR100651418B1 (ko) 2006-03-17 2006-11-30 에스케이 주식회사 고속유동층을 이용하여 탄화수소 원료로부터 경질 올레핀을제조하는 접촉분해 공정
DE102006035718A1 (de) * 2006-07-28 2008-01-31 Basf Ag Verfahren zum Langzeitbetrieb einer kontinuierlich betriebenen heterogen katalysierten partiellen Dehydrierung eines zu dehydrierenden Kohlenwasserstoffs
KR101489768B1 (ko) * 2006-12-28 2015-02-04 유오피 엘엘씨 알칸 스트림을 탈수소화하는 촉매 탈수소화 방법 및 장치
KR100898816B1 (ko) * 2007-02-12 2009-05-22 한국에너지기술연구원 수증기 전처리기를 포함한 ｃｏ2 분리회수장치
RU2344116C1 (ru) * 2007-03-22 2009-01-20 Некоммерческая организация Учреждение Институт химической физики Российской академии наук (статус государственного учреждения) ИПХФ РАН Способ получения пропилена термическим или окислительным дегидрированием пропана, катализатор, реактор для получения пропилена термическим дегидрированием пропана и реактор для получения пропилена окислительным дегидрированием пропана
KR100841804B1 (ko) 2007-07-13 2008-06-26 에스케이에너지 주식회사 유동층 촉매 반응 공정의 유출물로부터 나프텐계 베이스오일을 제조하는 방법
JP5124407B2 (ja) * 2008-09-26 2013-01-23 ジェイパワー・エンテック株式会社 乾式排ガス処理装置のコンベヤシステム
JP2013141659A (ja) * 2012-01-12 2013-07-22 Sumitomo Chemical Co Ltd 反応装置及びε−カプロラクタムの製造方法
CN103566838B (zh) * 2012-08-02 2018-04-13 宁波科元塑胶有限公司 丙烯腈流化反应系统及丙烯腈流化床生产方法
KR102179574B1 (ko) * 2017-06-07 2020-11-16 에스케이가스 주식회사 환원 전처리를 포함하는 올레핀 제조 방법
MY192623A (en) * 2017-07-18 2022-08-29 Lummus Technology Inc Integrated thermal and catalytic cracking for olefin production
EP4004153A1 (fr) * 2019-07-31 2022-06-01 SABIC Global Technologies, B.V. Équilibre thermique de systèmes à lit fluidisé à haute densité
KR102827512B1 (ko) * 2022-10-19 2025-07-02 한국화학연구원 포화 탄화수소의 탈수소-크래킹 반응을 통한 올레핀 제조방법
EP4594281A1 (fr) * 2022-11-29 2025-08-06 Dow Global Technologies LLC Procédés pour constituer des oléfines légères avec recyclage du catalyseur

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0236054A2 (fr) * 1986-02-24 1987-09-09 Engelhard Corporation Procédé de traitement d'hydrocarbures
WO1990012077A1 (fr) * 1989-04-10 1990-10-18 Mobil Oil Corporation Procede et appareil de craquage catalytique de petrole brut lourd
US5009769A (en) * 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
EP0512164A1 (fr) * 1989-11-21 1992-11-11 Mobil Oil Corporation Fractionnement des produits de craquage catalytique fluidisé
US5234578A (en) * 1988-08-26 1993-08-10 Uop Fluidized catalytic cracking process utilizing a high temperature reactor

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US4419221A (en) * 1981-10-27 1983-12-06 Texaco Inc. Cracking with short contact time and high temperatures
EP0311375A1 (fr) * 1987-10-08 1989-04-12 Mobil Oil Corporation Procédé pour le craquage d'une charge hydrocarbonée pour l'obtention d'essence et d'oléfines et valorisation des oléfines pour améliorer le rendement total en essence

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0236054A2 (fr) * 1986-02-24 1987-09-09 Engelhard Corporation Procédé de traitement d'hydrocarbures
US5234578A (en) * 1988-08-26 1993-08-10 Uop Fluidized catalytic cracking process utilizing a high temperature reactor
US5009769A (en) * 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
WO1990012077A1 (fr) * 1989-04-10 1990-10-18 Mobil Oil Corporation Procede et appareil de craquage catalytique de petrole brut lourd
EP0512164A1 (fr) * 1989-11-21 1992-11-11 Mobil Oil Corporation Fractionnement des produits de craquage catalytique fluidisé

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6200534B1 (en) 1996-08-30 2001-03-13 Fortum Oil And Gas Oy Apparatus for chemical and physical processes
US6538169B1 (en) 2000-11-13 2003-03-25 Uop Llc FCC process with improved yield of light olefins
US7312370B2 (en) 2000-11-13 2007-12-25 Uop Llc FCC process with improved yield of light olefins
RU2291184C2 (ru) * 2001-07-06 2007-01-10 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом в две стадии сырья, полученного синтезом фишера-тропша, и установка для его осуществления
RU2283857C2 (ru) * 2001-07-06 2006-09-20 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом тяжелой фракции из продуктов, полученных способом фишера-тропша, и устройство для его осуществления
RU2283858C2 (ru) * 2001-07-06 2006-09-20 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом двух фракций продуктов, полученных синтезом фишера-тропша, и установка для его осуществления
RU2283339C2 (ru) * 2001-07-06 2006-09-10 Энститю Франсэ Дю Петроль Способ получения средних дистиллятов гидроизомеризацией и гидрокрекингом сырья, полученного синтезом фишера-тропша, и установка для его осуществления
KR100473986B1 (ko) * 2001-11-01 2005-03-07 서곤 Ｆｃｃ 공정 폐촉매로부터 폐고분자 물질의 액상 분해용촉매의 제조방법 및 이 촉매를 이용한 폐고분자 물질의분해방법
US7935314B2 (en) 2008-09-30 2011-05-03 Uop Llc Apparatus for mixing regenerated and carbonized catalyst
US8323477B2 (en) 2008-09-30 2012-12-04 Uop Llc Process for mixing regenerated and carbonized catalyst
US20110137101A1 (en) * 2009-12-09 2011-06-09 Uop Llc Process for the Production of Propylene
US8293670B2 (en) 2009-12-09 2012-10-23 Uop Llc Process for the production of propylene
US11981633B2 (en) 2018-08-03 2024-05-14 Neste Oyj Method to produce bio-renewable propylene from oils and fats
WO2023098843A1 (fr) * 2021-12-03 2023-06-08 中国石油化工股份有限公司 Réacteur de craquage catalytique, système et application

Also Published As

Publication number Publication date
KR100281750B1 (ko) 2001-03-02
FI941528A7 (fi) 1995-10-01
CN1148865A (zh) 1997-04-30
CA2186744A1 (fr) 1995-10-12
EP0753037A1 (fr) 1997-01-15
JPH09511535A (ja) 1997-11-18
FI98529C (fi) 1997-07-10
EP0753037B1 (fr) 2000-08-16
ES2149976T3 (es) 2000-11-16
RU2125079C1 (ru) 1999-01-20
FI941528A0 (fi) 1994-03-31
AU2139695A (en) 1995-10-23
DE69518407D1 (de) 2000-09-21
CA2186744C (fr) 2003-06-24
FI98529B (fi) 1997-03-27
CN1124330C (zh) 2003-10-15
DE69518407T2 (de) 2001-03-22
KR970702349A (ko) 1997-05-13

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