DE69918451D1 - Verfahren zur herstellung von olefinen unter verwendung eines pentasil-zeolith enthaltenden katalysators - Google Patents

Verfahren zur herstellung von olefinen unter verwendung eines pentasil-zeolith enthaltenden katalysators

Info

Publication number
DE69918451D1
DE69918451D1 DE69918451T DE69918451T DE69918451D1 DE 69918451 D1 DE69918451 D1 DE 69918451D1 DE 69918451 T DE69918451 T DE 69918451T DE 69918451 T DE69918451 T DE 69918451T DE 69918451 D1 DE69918451 D1 DE 69918451D1
Authority
DE
Germany
Prior art keywords
hydrocarbon
passed
catalyst
naphtha
pentasil zeolite
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.)
Expired - Fee Related
Application number
DE69918451T
Other languages
English (en)
Other versions
DE69918451T2 (de
Inventor
Fernand Froment
Jozef Dehertog
P Kaminsky
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.)
BP Corp North America Inc
Original Assignee
BP Corp North America Inc
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 BP Corp North America Inc filed Critical BP Corp North America Inc
Application granted granted Critical
Publication of DE69918451D1 publication Critical patent/DE69918451D1/de
Publication of DE69918451T2 publication Critical patent/DE69918451T2/de
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06—Catalytic processes
    • 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
    • B01J29/061—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing metallic elements added to the zeolite
    • 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
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B01J29/405—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
    • 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
    • B01J29/82—Phosphates
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/40—Ethylene production

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
DE69918451T 1998-09-28 1999-09-28 Verfahren zur herstellung von olefinen unter verwendung eines pentasil-zeolith enthaltenden katalysators Expired - Fee Related DE69918451T2 (de)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US16184598A 1998-09-28 1998-09-28
US161845 1998-09-28
US40558299A 1999-09-27 1999-09-27
US405582 1999-09-27
PCT/US1999/022460 WO2000018853A1 (en) 1998-09-28 1999-09-28 Process for manufacturing olefins using a pentasil zeolite based catalyst

Publications (2)

Publication Number Publication Date
DE69918451D1 true DE69918451D1 (de) 2004-08-05
DE69918451T2 DE69918451T2 (de) 2005-07-28

Family

ID=26858166

Family Applications (1)

Application Number Title Priority Date Filing Date
DE69918451T Expired - Fee Related DE69918451T2 (de) 1998-09-28 1999-09-28 Verfahren zur herstellung von olefinen unter verwendung eines pentasil-zeolith enthaltenden katalysators

Country Status (12)

Country Link
US (1) US6548725B2 (de)
EP (1) EP1117750B1 (de)
JP (1) JP2002525380A (de)
CN (1) CN1195714C (de)
AT (1) ATE270318T1 (de)
AU (1) AU6271299A (de)
CA (1) CA2345308A1 (de)
DE (1) DE69918451T2 (de)
ES (1) ES2224702T3 (de)
ID (1) ID29487A (de)
NO (1) NO20011561L (de)
WO (1) WO2000018853A1 (de)

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US7285511B2 (en) 2004-04-23 2007-10-23 Saudi Basic Industries Corporation Method of modifying zeolite catalyst
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CN100351344C (zh) * 2004-07-14 2007-11-28 中国石油化工股份有限公司 一种选择性制取小分子烯烃的催化转化方法
WO2006098712A1 (en) * 2005-03-11 2006-09-21 Uop Llc Catalytic naphtha cracking catalyst and process
US7304194B2 (en) * 2005-05-05 2007-12-04 Saudi Basic Industries Corporation Hydrothermal treatment of phosphorus-modified zeolite catalysts
KR100598988B1 (ko) * 2005-05-18 2006-07-12 주식회사 하이닉스반도체 오버레이 버니어 및 이를 이용한 반도체소자의 제조방법
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KR100651418B1 (ko) * 2006-03-17 2006-11-30 에스케이 주식회사 고속유동층을 이용하여 탄화수소 원료로부터 경질 올레핀을제조하는 접촉분해 공정
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US7498473B2 (en) * 2006-07-27 2009-03-03 Uop Llc Process for dehydrocyclodimerization
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CN101279881B (zh) * 2007-04-04 2010-08-18 中国石油化工股份有限公司 催化裂解石脑油生产乙烯和丙烯的方法
BRPI0815417A8 (pt) * 2007-08-13 2018-10-30 Agency Science Tech & Res composição de catalisador modificada para conversão de álcool em alceno
US8846559B2 (en) * 2008-11-03 2014-09-30 Saudi Basic Industries Corporation Stable shape-selective catalyst for aromatic alkylation and methods of using and preparing
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US8062987B2 (en) * 2009-10-05 2011-11-22 Saudi Basic Industries Corporation Phosphorus-containing zeolite catalysts and their method of preparation
US20110230333A1 (en) * 2010-03-16 2011-09-22 Uop Llc Olefin Cracking Catalyst and Manufacturing Process
WO2011121613A2 (en) 2010-03-31 2011-10-06 Indian Oil Corporation Ltd A process for simultaneous cracking of lighter and heavier hydrocarbon feed and system for the same
JP2012139640A (ja) 2010-12-28 2012-07-26 Jx Nippon Oil & Energy Corp 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法
JP5587761B2 (ja) 2010-12-28 2014-09-10 Ｊｘ日鉱日石エネルギー株式会社 単環芳香族炭化水素の製造方法
JP2012139641A (ja) * 2010-12-28 2012-07-26 Jx Nippon Oil & Energy Corp 単環芳香族炭化水素製造用触媒および単環芳香族炭化水素の製造方法
BR112014002420B1 (pt) * 2011-08-03 2024-01-09 IFP Energies Nouvelles Método de conversão de um álcool em olefinas leves
US8772192B2 (en) 2012-06-29 2014-07-08 Saudi Basic Industries Corporation Germanium silicalite catalyst and method of preparation and use
US9278342B2 (en) 2012-07-02 2016-03-08 Saudi Basic Industries Corporation Method of modifying a phosphorus-containing zeolite catalyst
CN112264086A (zh) 2013-04-29 2021-01-26 沙特基础工业公司 石脑油转化成烯烃的催化方法
KR101600430B1 (ko) 2015-01-08 2016-03-07 한국화학연구원 이산화탄소가 풍부한 합성가스로부터 단환 방향족 화합물 및 장쇄올레핀 화합물의 직접 합성방법
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FR3049954A1 (fr) 2016-04-08 2017-10-13 Ifp Energies Now Utilisation de zeolithe nu-86 pour le procede de craquage catalytique de naphtha
US9981888B2 (en) 2016-06-23 2018-05-29 Saudi Arabian Oil Company Processes for high severity fluid catalytic cracking systems
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EP3622039A1 (de) * 2017-05-10 2020-03-18 SABIC Global Technologies B.V. Verfahren zum katalytischen cracken von naphtha unter verwendung eines radialen fliessbett-reaktorsystems
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CN112654690A (zh) 2018-09-06 2021-04-13 沙特基础全球技术有限公司 使用多级径向流移动床反应器系统催化裂化石脑油的方法
JP7467475B2 (ja) * 2018-12-26 2024-04-15 ピーティーティー グローバル ケミカル パブリック カンパニー リミテッド Ｃ４－ｃ７炭化水素から軽質オレフィンを製造するための触媒
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KR102653716B1 (ko) 2020-03-03 2024-04-03 한국화학연구원 이산화탄소가 포함된 합성가스로부터 선형 알파 올레핀을 제조하기 위한 촉매 및 이를 이용한 선형 알파 올레핀의 제조방법
US11242493B1 (en) 2020-09-01 2022-02-08 Saudi Arabian Oil Company Methods for processing crude oils to form light olefins
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Also Published As

Publication number Publication date
US6548725B2 (en) 2003-04-15
NO20011561D0 (no) 2001-03-27
EP1117750B1 (de) 2004-06-30
CN1195714C (zh) 2005-04-06
DE69918451T2 (de) 2005-07-28
CN1320148A (zh) 2001-10-31
CA2345308A1 (en) 2000-04-06
ES2224702T3 (es) 2005-03-01
EP1117750A1 (de) 2001-07-25
NO20011561L (no) 2001-03-27
JP2002525380A (ja) 2002-08-13
ID29487A (id) 2001-08-30
WO2000018853A1 (en) 2000-04-06
AU6271299A (en) 2000-04-17
US20010056217A1 (en) 2001-12-27
ATE270318T1 (de) 2004-07-15

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