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AU2003227673A1 - Device for producing propylene from methanol - Google Patents

Device for producing propylene from methanol

Info

Publication number
AU2003227673A1
AU2003227673A1 AU2003227673A AU2003227673A AU2003227673A1 AU 2003227673 A1 AU2003227673 A1 AU 2003227673A1 AU 2003227673 A AU2003227673 A AU 2003227673A AU 2003227673 A AU2003227673 A AU 2003227673A AU 2003227673 A1 AU2003227673 A1 AU 2003227673A1
Authority
AU
Australia
Prior art keywords
methanol
producing propylene
propylene
producing
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.)
Abandoned
Application number
AU2003227673A
Inventor
Hermann Bach
Lothar Brehm
Sandra Jensen
Harald Kompel
Peter Trabold
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.)
Air Liquide Global E&C Solutions Germany GmbH
Original Assignee
Lurgi GmbH
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 Lurgi GmbH filed Critical Lurgi GmbH
Publication of AU2003227673A1 publication Critical patent/AU2003227673A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496Heating or cooling the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • B01J8/0085Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction promoting uninterrupted fluid flow, e.g. by filtering out particles in front of the catalyst layer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
AU2003227673A 2002-07-25 2003-04-25 Device for producing propylene from methanol Abandoned AU2003227673A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10233975A DE10233975A1 (en) 2002-07-25 2002-07-25 Device for the production of propylene from methanol comprises preferably two or three vertically arranged reaction stages having a form-selective pentasil-type zeolite catalyst with heat exchangers arranged between the stages
DE10233975.9 2002-07-25
PCT/EP2003/004290 WO2004018089A1 (en) 2002-07-25 2003-04-25 Device for producing propylene from methanol

Publications (1)

Publication Number Publication Date
AU2003227673A1 true AU2003227673A1 (en) 2004-03-11

Family

ID=30128410

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2003227673A Abandoned AU2003227673A1 (en) 2002-07-25 2003-04-25 Device for producing propylene from methanol

Country Status (3)

Country Link
AU (1) AU2003227673A1 (en)
DE (1) DE10233975A1 (en)
WO (1) WO2004018089A1 (en)

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US7205376B2 (en) 2004-05-04 2007-04-17 General Electric Company Processes for the production of cumene, polyetherimides, and polycarbonates
US7465845B2 (en) 2004-12-22 2008-12-16 Exxonmobil Chemical Patents Inc. Increasing ethylene and/or propylene production in an oxygenate to olefins reaction systems
US7678953B2 (en) 2005-01-31 2010-03-16 Exxonmobil Chemical Patents Inc. Olefin oligomerization
WO2006084286A2 (en) 2005-01-31 2006-08-10 Exxonmobil Chemical Patents Inc. Hydrocarbon compositions useful for producing fuels
DE102005015923B4 (en) * 2005-04-06 2014-12-04 Air Liquide Global E&C Solutions Germany Gmbh Process for the preparation of C2 to C4 olefins from an oxygenate and steam containing feed stream
DE102005048931B8 (en) * 2005-10-13 2015-06-18 Air Liquide Global E&C Solutions Germany Gmbh Process and plant for the production of C 2 -C 4 olefins from methanol and / or dimethyl ether
US7687671B2 (en) 2005-12-05 2010-03-30 Uop Llc Integrated oxygenate conversion and product cracking
US8168842B2 (en) 2006-05-19 2012-05-01 Shell Oil Company Process for the alkylation of a cycloalkene
CN101448766A (en) 2006-05-19 2009-06-03 国际壳牌研究有限公司 Process for the preparation of C5 and/or C6 olefins
DE102006026103B4 (en) * 2006-06-03 2010-05-06 Lurgi Gmbh Reactor for the production of C2- to C8-olefins from an oxygenate, water vapor and one or more hydrocarbons containing stream
US7741526B2 (en) 2006-07-19 2010-06-22 Exxonmobil Chemical Patents Inc. Feedstock preparation of olefins for oligomerization to produce fuels
CN101239872B (en) * 2007-02-07 2011-11-30 中国石油化工股份有限公司 Method for increasing selectivity of low-carbon olefins
AU2008327864B2 (en) 2007-11-19 2011-06-30 Shell Internationale Research Maatschappij B.V. Catalyst particles, process for the preparation of an olefinic product, and process for the preparation of an oxygenate conversion catalyst
US8884090B2 (en) 2007-11-19 2014-11-11 Shell Oil Company Process for the preparation of an olefin
DE102008061300A1 (en) 2008-12-11 2010-07-08 Lurgi Gmbh Method for producing a product containing C3H6 and C2H4
AU2009331847B2 (en) 2008-12-22 2012-06-07 Air Products And Chemicals, Inc. Process to prepare methanol and/or dimethylether
CN102190546B (en) * 2010-03-03 2013-09-18 中国石油化工股份有限公司 Method for preparing propylene and aromatic hydrocarbon by virtue of conversion of methanol
CN101869819B (en) * 2010-06-18 2014-12-03 王伟跃 Reactor for preparing propylene from oxygen-containing compound
DE102010042216A1 (en) 2010-10-08 2011-06-09 Basf Se Inhibiting the unwanted radical polymerization of acrylic acid present in a liquid phase, comprises adding a chemical compound of copper to the liquid phase, and the liquid phase additionally contains propionic acid and glyoxal
CN102345848B (en) * 2011-06-30 2014-01-29 神华集团有限责任公司 Method and system suitable for propylene preparation technology from coal-based methanol for improving load of process steam tower
CN103028434B (en) * 2011-09-29 2015-10-21 中国石油化工股份有限公司 The Catalysts and its preparation method of preparing propylene by methanol transformation
CN103030504B (en) * 2011-09-29 2015-12-16 中国石油化工股份有限公司 The production method of propylene
CN103962170A (en) 2013-01-31 2014-08-06 上海碧科清洁能源技术有限公司 Methanol-to-olefin catalyst with high C4 olefin selectivity and preparation method thereof
CN104109072B (en) * 2013-04-16 2017-03-15 中国石油化工股份有限公司 The reaction unit of methanol-to-olefins and its application
CN103623859B (en) * 2013-12-06 2016-04-13 陕西煤化工技术工程中心有限公司 Catalyst for producing propylene with methanol of high third second ratio and preparation method thereof is obtained under high-speed
CN105949021B (en) * 2016-05-25 2019-01-18 上海交通大学 A kind of system and method that propylene is prepared by Catalytic dehydration of methanol
CN106008128B (en) * 2016-05-25 2018-06-26 上海交通大学 The reaction-regeneration system and method for a kind of preparing propylene from methanol
CN106010626A (en) * 2016-07-08 2016-10-12 成都赛普瑞兴科技有限公司 Process of preparing stable light hydrocarbon through methanol conversion in isothermal method
US10702841B2 (en) 2016-10-19 2020-07-07 Dalian Institute Of Chemical Physics, Chinese Academy Of Sciences Fast fluidized-bed reactor, device, and method using oxygen-containing compound for manufacturing propene or C4 hydrocarbon
EP3530643B1 (en) 2016-10-19 2024-10-09 Dalian Institute Of Chemical Physics, Chinese Academy of Sciences Turbulent fluidized-bed reactor, device, and method using oxygen-containing compound for manufacturing propene and c4 hydrocarbon
EP3530642B1 (en) 2016-10-19 2024-01-24 Dalian Institute Of Chemical Physics, Chinese Academy of Sciences Method and device for manufacturing propene and c4 hydrocarbon
MY195877A (en) 2016-10-19 2023-02-27 Dalian Inst Chem & Physics Cas Method and Device for Manufacturing Propene and C4 Hydrocarbon
JP7384519B2 (en) 2018-07-26 2023-11-21 ベーアーエスエフ・エスエー Method for suppressing undesirable radical polymerization of acrylic acid present in liquid phase P
US20230132285A1 (en) 2020-03-26 2023-04-27 Basf Se Process for inhibiting the undesired free-radical polymerization of acrylic acid present in a liquid phase p
WO2023196305A1 (en) 2022-04-06 2023-10-12 ExxonMobil Technology and Engineering Company Isoparaffinic and iso-olefinic distillate compositions
WO2023196295A1 (en) 2022-04-06 2023-10-12 ExxonMobil Technology and Engineering Company Isoparaffinic kerosene compositions
US12012562B2 (en) 2022-04-06 2024-06-18 ExxonMobil Technology and Engineering Company Methods for converting C2+ olefins to higher carbon number olefins useful in producing isoparaffinic distillate compositions
CN115259982B (en) * 2022-08-01 2024-05-14 润和催化剂股份有限公司 Technological method and reaction system for preparing propylene by methanol conversion
WO2024187036A1 (en) * 2023-03-07 2024-09-12 Gevo, Inc. Multistage reactor systems and processes for conversion of oxygenates
WO2024194206A1 (en) 2023-03-17 2024-09-26 Basf Se Process for producing propylene

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DE2221288C3 (en) * 1972-04-29 1975-04-17 Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf Reaction apparatus for carrying out catalytic reactions in several stages
CA1202986A (en) * 1982-02-05 1986-04-08 Mobil Oil Corporation Process for converting methanol into olefins
US4542252A (en) * 1984-07-20 1985-09-17 Mobil Oil Corporation Multi-stage adiabatic process for methanol conversion to light olefins
DE3631642A1 (en) * 1986-09-17 1988-04-07 Linde Ag METHOD FOR CARRYING OUT CATALYTIC REACTIONS
US5840259A (en) * 1993-04-05 1998-11-24 Catalytic Distillation Technologies Boiling point reactor with heat removal
DE10027159A1 (en) * 2000-05-31 2001-12-13 Mg Technologies Ag Production of propylene from methanol via two-stage catalytic dimethyl ether conversion, introduces dimethyl ether, vapor and steam into reactors containing shape-selective catalyst

Also Published As

Publication number Publication date
DE10233975A1 (en) 2004-02-12
WO2004018089A1 (en) 2004-03-04

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Legal Events

Date Code Title Description
MK6 Application lapsed section 142(2)(f)/reg. 8.3(3) - pct applic. not entering national phase