AU2003227673A1 - Device for producing propylene from methanol - Google Patents
Device for producing propylene from methanolInfo
- 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
Links
Classifications
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical 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
- B01J8/04—Chemical 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
- B01J8/0496—Heating or cooling the reactor
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/0085—Details 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
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical 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
- B01J8/04—Chemical 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
- B01J8/0446—Chemical 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
- B01J8/0449—Chemical 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
- B01J8/0453—Chemical 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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements 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)
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) |
Families Citing this family (40)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
-
2002
- 2002-07-25 DE DE10233975A patent/DE10233975A1/en not_active Ceased
-
2003
- 2003-04-25 AU AU2003227673A patent/AU2003227673A1/en not_active Abandoned
- 2003-04-25 WO PCT/EP2003/004290 patent/WO2004018089A1/en not_active Application Discontinuation
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 |