WO2003059857A1 - Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor - Google Patents
Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor Download PDFInfo
- Publication number
- WO2003059857A1 WO2003059857A1 PCT/JP2003/000160 JP0300160W WO03059857A1 WO 2003059857 A1 WO2003059857 A1 WO 2003059857A1 JP 0300160 W JP0300160 W JP 0300160W WO 03059857 A1 WO03059857 A1 WO 03059857A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- reaction
- pipes
- reactor
- multipipe
- catalyst
- Prior art date
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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/887—Molybdenum containing in addition other metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/8876—Arsenic, antimony or bismuth
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/55—Cylinders or rings
-
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling the reactor
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
- C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
- C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
- C07C45/34—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
- C07C45/35—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds in propene or isobutene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/215—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of saturated hydrocarbyl groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
-
- 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
- B01J2208/00212—Plates; Jackets; Cylinders
- B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
-
- 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
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- 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
- B01J2208/00716—Means for reactor start-up
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0022—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for chemical reactors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/1607—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with particular pattern of flow of the heat exchange media, e.g. change of flow direction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
- F28F2265/10—Safety or protection arrangements; Arrangements for preventing malfunction for preventing overheating, e.g. heat shields
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/028—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits by using inserts for modifying the pattern of flow inside the header box, e.g. by using flow restrictors or permeable bodies or blocks with channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0306797A BRPI0306797B1 (pt) | 2002-01-11 | 2003-01-10 | reator multitubular, e, métodos de oxidação catalítica em fase vapor e para iniciar um reator tipo casco-tubo |
ES03700524T ES2719089T3 (es) | 2002-01-11 | 2003-01-10 | Uso de un reactor multitubular para la producción de (met)acroleína y/o ácido (met)acrílico |
EP03700524.6A EP1471046B1 (en) | 2002-01-11 | 2003-01-10 | Use of a multitube reactor for production of (meth)acrolein and/or (meth)acrylic acid |
AU2003201861A AU2003201861A1 (en) | 2002-01-11 | 2003-01-10 | Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor |
US10/887,868 US7144557B2 (en) | 2002-01-11 | 2004-07-12 | Multitube reactor, vapor phase catalytic oxidation method using the multitube reactor, and start up method applied to the multitube reactor |
US11/049,106 US7297814B2 (en) | 2002-01-11 | 2005-02-03 | Multitube reactor, vapor phase catalytic oxidation method using the multitube reactor, and start up method applied to the multitube reactor |
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002-4636 | 2002-01-11 | ||
JP2002004636 | 2002-01-11 | ||
JP2002-36460 | 2002-02-14 | ||
JP2002036460 | 2002-02-14 | ||
JP2002-69820 | 2002-03-14 | ||
JP2002069820A JP4103416B2 (ja) | 2002-03-14 | 2002-03-14 | 反応器のスタートアップ方法 |
JP2002-105924 | 2002-04-09 | ||
JP2002105924 | 2002-04-09 |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/887,868 Continuation US7144557B2 (en) | 2002-01-11 | 2004-07-12 | Multitube reactor, vapor phase catalytic oxidation method using the multitube reactor, and start up method applied to the multitube reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2003059857A1 true WO2003059857A1 (en) | 2003-07-24 |
Family
ID=27482765
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2003/000160 WO2003059857A1 (en) | 2002-01-11 | 2003-01-10 | Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor |
Country Status (7)
Country | Link |
---|---|
US (2) | US7144557B2 (ja) |
EP (2) | EP2361899B1 (ja) |
CN (3) | CN1277790C (ja) |
AU (1) | AU2003201861A1 (ja) |
BR (1) | BRPI0306797B1 (ja) |
ES (2) | ES2547074T3 (ja) |
WO (1) | WO2003059857A1 (ja) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102007025869A1 (de) | 2007-06-01 | 2008-07-03 | Basf Se | Verfahren der Wiederbeschickung der Reaktionsrohre eines Rohrbündelreaktors mit einem neuen Katalysatorfestbett |
CN100415356C (zh) * | 2004-06-24 | 2008-09-03 | 华东理工大学 | 一种适用于高热敏性物质的气固相反应装置 |
WO2008120956A1 (en) * | 2007-04-03 | 2008-10-09 | Lg Chem, Ltd. | Method for preparing unsaturated aldehyde and/or unsaturated fatty acid using fixed-bed catalytic partial oxidation reactor |
DE102007017080A1 (de) | 2007-04-10 | 2008-10-16 | Basf Se | Verfahren zur Beschickung eines Längsabschnitts eines Kontaktrohres |
DE102007028333A1 (de) | 2007-06-15 | 2008-12-18 | Basf Se | Verfahren zum Einbringen einer wenigstens einer Produktionscharge von ringförmigen Schalenkatalysatoren K entnommenen Teilmenge in ein Reaktionsrohr eines Rohrbündelreaktors |
DE102007028332A1 (de) | 2007-06-15 | 2008-12-18 | Basf Se | Verfahren zum Beschicken eines Reaktors mit einem Katalysatorfestbett, das wenigstens ringförmige Katalysatorformkörper K umfasst |
US7731916B2 (en) | 2004-05-07 | 2010-06-08 | Basf Aktiengesellschaft | Method of charging catalyst tubes of a bundle of catalyst tubes in a structured fashion |
US8076510B2 (en) | 2007-04-24 | 2011-12-13 | Basf Se | Process for starting-up a heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acid or of methacrolein to methacrylic acid |
CN109701454A (zh) * | 2019-01-28 | 2019-05-03 | 安庆市泰发能源科技有限公司 | 丁烷脱氢开工循环升温装置 |
CN115999320A (zh) * | 2021-10-22 | 2023-04-25 | 中国石油化工股份有限公司 | 一种利用熔盐溶剂回收环氧丙烷尾气方法 |
Families Citing this family (55)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BRPI0306797B1 (pt) * | 2002-01-11 | 2016-07-12 | Mitsubishi Chem Corp | reator multitubular, e, métodos de oxidação catalítica em fase vapor e para iniciar um reator tipo casco-tubo |
JP4145607B2 (ja) * | 2002-08-23 | 2008-09-03 | 三菱化学株式会社 | 多管式反応器を用いた気相接触酸化方法 |
US7731917B2 (en) * | 2004-05-28 | 2010-06-08 | Sumitomo Chemical Company, Limited | Heat exchange reactor |
US7371361B2 (en) * | 2004-11-03 | 2008-05-13 | Kellogg Brown & Root Llc | Maximum reaction rate converter system for exothermic reactions |
TWI349001B (en) * | 2005-03-18 | 2011-09-21 | Lg Chemical Ltd | Method of producing unsaturated acid from olefin |
WO2007075476A2 (en) | 2005-12-21 | 2007-07-05 | Virent Energy Systems Inc. | Catalysts and methods for reforming oxygenated compounds |
WO2007083927A1 (en) * | 2006-01-18 | 2007-07-26 | Lg Chem, Ltd. | Reactor with improved heat transfer performance |
MX2009006509A (es) | 2006-12-20 | 2009-10-28 | Virent Energy Systems Inc | Sistema reactor para la produccion de productos gaseosos. |
RU2472840C2 (ru) | 2007-03-08 | 2013-01-20 | Вайрент, Инк. | Синтез жидкого топлива и химических реактивов из кислородсодержащих углеводородов |
EP2196521A4 (en) * | 2007-10-03 | 2014-08-20 | Mitsui Shipbuilding Eng | DEVICE FOR PRODUCING GAS HYDRATES |
US9873305B2 (en) | 2008-02-22 | 2018-01-23 | Dow Global Technologies Inc. | Heater module including thermal energy storage material |
JP2011524966A (ja) | 2008-02-22 | 2011-09-08 | ダウ グローバル テクノロジーズ エルエルシー | 熱エネルギー貯蔵材料 |
US9038709B2 (en) | 2008-02-22 | 2015-05-26 | Dow Global Technologies Llc | Thermal energy storage materials |
JP2011527740A (ja) * | 2008-02-22 | 2011-11-04 | ダウ グローバル テクノロジーズ エルエルシー | 熱貯蔵デバイス |
CA2736800A1 (en) | 2008-08-27 | 2010-03-04 | Randy D. Cortright | Synthesis of liquid fuels from biomass |
EP2485832B1 (en) * | 2009-10-09 | 2016-11-23 | Blue Cube IP LLC | Process for producing a chlorinated and/or fluorinated propene in an isothermal multitube reactors and |
CN102574755B (zh) * | 2009-10-09 | 2015-11-25 | 陶氏环球技术有限责任公司 | 用于生产氯化和/或氟化丙烯的方法 |
JP5767231B2 (ja) | 2009-10-09 | 2015-08-19 | ダウ グローバル テクノロジーズ エルエルシー | 塩素化及び/又はフッ素化されたプロペン及びより高級なアルケンを製造するプロセス |
WO2011044522A2 (en) * | 2009-10-09 | 2011-04-14 | Dow Global Technologies, Inc | Adiabatic plug flow reactors and processes incorporating the same |
US9222733B2 (en) | 2011-02-03 | 2015-12-29 | Memc Electronic Materials S.P.A. | Reactor apparatus and methods for reacting compounds |
WO2012166393A1 (en) | 2011-05-31 | 2012-12-06 | Dow Global Technologies, Llc | Process for the production of chlorinated propenes |
EP2714631B1 (en) | 2011-05-31 | 2020-05-13 | Blue Cube IP LLC | Process for the production of chlorinated propenes |
EP2718249B1 (en) | 2011-06-08 | 2019-02-27 | Dow AgroSciences LLC | Process for the production of chlorinated and/or fluorinated propenes |
US9233896B2 (en) | 2011-08-07 | 2016-01-12 | Blue Cube Ip Llc | Process for the production of chlorinated propenes |
EP2739596B1 (en) | 2011-08-07 | 2019-05-01 | Blue Cube IP LLC | Process for the production of chlorinated propenes |
WO2013078035A1 (en) | 2011-11-21 | 2013-05-30 | Dow Global Technologies, Llc | Process for the production of chlorinated alkanes |
US9284239B2 (en) | 2011-12-02 | 2016-03-15 | Blue Cube Ip Llc | Process for the production of chlorinated alkanes |
CN104024186B (zh) | 2011-12-02 | 2016-10-12 | 蓝立方知识产权有限责任公司 | 生产氯化烷烃的方法 |
JP6170068B2 (ja) | 2011-12-13 | 2017-07-26 | ブルー キューブ アイピー エルエルシー | 塩素化プロパン及びプロペンの製造方法 |
WO2013096311A1 (en) | 2011-12-22 | 2013-06-27 | Dow Global Technologies, Llc | Process for the production of tetrachloromethane |
BR112014015123A2 (pt) | 2011-12-23 | 2017-06-13 | Dow Global Technologies Llc | processo para a produção de um ou mais alcenos ou compostos aromáticos |
KR101422630B1 (ko) * | 2011-12-30 | 2014-07-23 | 두산중공업 주식회사 | 열교환형 선개질기 |
JP6156860B2 (ja) | 2012-04-04 | 2017-07-05 | 住友化学株式会社 | 多管式反応器および多管式反応器の設計方法 |
JP2015529247A (ja) | 2012-09-20 | 2015-10-05 | ダウ グローバル テクノロジーズ エルエルシー | 塩素化プロペンの生成のためのプロセス |
EP2897930A1 (en) | 2012-09-20 | 2015-07-29 | Dow Global Technologies LLC | Process for the production of chlorinated propenes |
WO2014052945A2 (en) | 2012-09-30 | 2014-04-03 | Dow Global Technologies, Llc | Weir quench and processes incorporating the same |
WO2014066083A1 (en) | 2012-10-26 | 2014-05-01 | Dow Global Technologies, Llc | Mixer and reactor and process incorporating the same |
US9512053B2 (en) | 2012-12-18 | 2016-12-06 | Blue Cube Ip Llc | Process for the production of chlorinated propenes |
EP2935166A1 (en) | 2012-12-19 | 2015-10-28 | Blue Cube IP LLC | Process for the production of chlorinated propenes |
CA2901450A1 (en) | 2013-02-27 | 2014-09-04 | Blue Cube Ip Llc | Process for the production of chlorinated propenes |
JP6449791B2 (ja) | 2013-03-09 | 2019-01-09 | ブルー キューブ アイピー エルエルシー | クロロアルカンの製造方法 |
RU2017120503A (ru) * | 2014-11-14 | 2018-12-14 | САБИК Глобал Текнолоджиз Б.В., | Реактор с неподвижным слоем и связанные с ним способы |
US9115067B1 (en) | 2014-12-22 | 2015-08-25 | Novus International, Inc. | Process for the manufacture of acrolein |
CN109312997A (zh) * | 2016-01-21 | 2019-02-05 | 杭州富尔顿热能设备有限公司 | 用于热交换器的挡板组合件、包括所述挡板组合件的热交换器、包括所述热交换器的流体加热系统及其制造方法 |
RS62934B1 (sr) * | 2016-07-19 | 2022-03-31 | Lummus Technology Inc | Razmenјivač toplote na dopremani fluid/efluent |
WO2018236489A1 (en) * | 2017-06-21 | 2018-12-27 | Westinghouse Electric Company Llc | ENERGY STORAGE DEVICE |
CN109593151B (zh) * | 2017-09-30 | 2022-04-08 | 中国石油化工股份有限公司 | 制备聚α-烯烃的方法和系统、聚α-烯烃及连续反应器 |
US11207649B2 (en) * | 2018-03-14 | 2021-12-28 | West Biofuels, Llc | Synthesis gas reactor tubes and reactors and related systems and processes |
CN108644795B (zh) * | 2018-05-31 | 2020-11-24 | 安徽中疆环境科技有限公司 | 一种环境工程用废气处理设备 |
CN108543500B (zh) * | 2018-06-28 | 2024-02-13 | 钦州学院 | 液相用的管道催化反应装置 |
CN109482128A (zh) * | 2019-01-18 | 2019-03-19 | 山东诺为制药流体系统有限公司 | 一种多线反应器 |
CN111889036B (zh) * | 2019-05-05 | 2023-01-10 | 中国石油集团工程股份有限公司 | 环戊二烯固定床催化加氢反应装置、系统及方法 |
CN112023835A (zh) * | 2020-09-28 | 2020-12-04 | 江苏永大化工机械有限公司 | 多程径向反应器 |
CN114409686B (zh) * | 2022-01-27 | 2023-11-07 | 上海化工研究院有限公司 | 一种用于制备三氟化硼络合物的系统及方法 |
CN115106035B (zh) * | 2022-07-04 | 2023-12-05 | 福州大学 | 一种用于氨分解的微通道反应器 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5149884A (en) * | 1986-04-11 | 1992-09-22 | Basf Aktiengesellschaft | Tube bundle reactor, use thereof in exothermic organic reactions, and preparation of ketones and aldehydes using same |
US5677261A (en) * | 1994-11-29 | 1997-10-14 | Basf Aktiengesellschaft | Preparation of a catalyst consisting of a carrier and a catalytically active oxide material applied to the surface of the carrier |
Family Cites Families (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1088009A (en) * | 1964-11-03 | 1967-10-18 | Halcon International Inc | Process and apparatus for the vapour phase oxidation of organic compounds |
DE2140125A1 (en) * | 1970-08-10 | 1972-02-17 | Topsoee, Haldor Frederik Axel, Vedbaek (Danemark) | Bi-metallic catalytic reaction tubes - with corrosion-resistant outer and pressure-resistant inner layers for reforming and cracking |
AU529228B2 (en) * | 1977-07-13 | 1983-06-02 | Nippon Shokubai Kagaku Kogyo Co. Ltd. | Catalytic vapour phase oxidation |
YU41495B (en) | 1979-01-23 | 1987-08-31 | Nippon Kayaku Kk | Process for obtaining methacrolein and methacrylic acid |
DE3020845A1 (de) | 1980-06-02 | 1981-12-17 | Basf Ag, 6700 Ludwigshafen | Verfahren und anordnung zum beschicken von rohrreaktoren mit koernigen feststoffen |
US5006131A (en) * | 1985-06-27 | 1991-04-09 | Stone & Webster Engineering Corporation | Apparatus for production of synthesis gas using convective reforming |
JPH0638918B2 (ja) | 1986-02-27 | 1994-05-25 | 三菱油化株式会社 | 複合酸化物触媒の製造法 |
JPH0613096B2 (ja) | 1986-08-23 | 1994-02-23 | 三菱油化株式会社 | 複合酸化物触媒の製造法 |
JPH0613096A (ja) | 1992-06-25 | 1994-01-21 | Ishikawajima Harima Heavy Ind Co Ltd | 燃料電池発電装置における改質方法及び装置 |
JP3180168B2 (ja) | 1992-07-21 | 2001-06-25 | 克彦 小澤 | 靴乾燥機 |
DE4431957A1 (de) | 1994-09-08 | 1995-03-16 | Basf Ag | Verfahren zur katalytischen Gasphasenoxidation von Propen zu Acrolein |
DE4431949A1 (de) | 1994-09-08 | 1995-03-16 | Basf Ag | Verfahren zur katalytischen Gasphasenoxidation von Acrolein zu Acrylsäure |
DE19520351A1 (de) * | 1995-06-07 | 1996-12-12 | Norddeutsche Seekabelwerke Ag | Füllkörperblock und Verfahren zur Herstellung desselben |
MXPA98008036A (es) * | 1996-04-01 | 2004-10-14 | Union Carbide Chem Plastic | Proceso para la fabricacion de metil mercaptopropanal. |
JP2863509B2 (ja) | 1997-04-16 | 1999-03-03 | 株式会社日本触媒 | メタクロレインおよびメタクリル酸の製造方法 |
JP3948798B2 (ja) | 1997-10-27 | 2007-07-25 | 株式会社日本触媒 | アクリル酸の製造方法 |
EP0963785B1 (en) | 1998-05-12 | 2003-04-02 | Cat Tech Inc. | Reactor tube loading device |
JP3559456B2 (ja) * | 1998-09-18 | 2004-09-02 | 株式会社日本触媒 | 接触気相酸化方法及び多管式反応器 |
JP3943284B2 (ja) | 1999-05-27 | 2007-07-11 | 株式会社日本触媒 | アクリル酸の製造方法 |
DE60035746T2 (de) | 1999-08-31 | 2008-04-30 | Nippon Shokubai Co., Ltd. | Reaktor zur katalytischen Gasphasenoxidation |
ZA200004211B (en) | 1999-08-31 | 2001-02-14 | Nippon Catalytic Chem Ind | Method for catalytic gas phase oxidation. |
JP3646027B2 (ja) * | 1999-11-05 | 2005-05-11 | 株式会社日本触媒 | 接触気相酸化用反応器およびそれを使用した(メタ)アクリル酸の製造方法 |
DE10011309A1 (de) * | 2000-03-10 | 2001-09-13 | Basf Ag | Verfahren zur Herstellung von Maleinsäreanhydrid |
JP4648515B2 (ja) | 2000-05-02 | 2011-03-09 | 株式会社日本触媒 | 反応器のスタートアップ方法 |
BRPI0306797B1 (pt) * | 2002-01-11 | 2016-07-12 | Mitsubishi Chem Corp | reator multitubular, e, métodos de oxidação catalítica em fase vapor e para iniciar um reator tipo casco-tubo |
-
2003
- 2003-01-10 BR BRPI0306797A patent/BRPI0306797B1/pt active IP Right Grant
- 2003-01-10 EP EP11160182.9A patent/EP2361899B1/en not_active Expired - Lifetime
- 2003-01-10 WO PCT/JP2003/000160 patent/WO2003059857A1/ja active Application Filing
- 2003-01-10 EP EP03700524.6A patent/EP1471046B1/en not_active Expired - Lifetime
- 2003-01-10 AU AU2003201861A patent/AU2003201861A1/en not_active Abandoned
- 2003-01-10 CN CNB038021722A patent/CN1277790C/zh not_active Expired - Lifetime
- 2003-01-10 CN CNA2004100749312A patent/CN1597080A/zh active Pending
- 2003-01-10 ES ES11160182.9T patent/ES2547074T3/es not_active Expired - Lifetime
- 2003-01-10 CN CNA2004100749331A patent/CN1597081A/zh active Pending
- 2003-01-10 ES ES03700524T patent/ES2719089T3/es not_active Expired - Lifetime
-
2004
- 2004-07-12 US US10/887,868 patent/US7144557B2/en not_active Expired - Lifetime
-
2005
- 2005-02-03 US US11/049,106 patent/US7297814B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5149884A (en) * | 1986-04-11 | 1992-09-22 | Basf Aktiengesellschaft | Tube bundle reactor, use thereof in exothermic organic reactions, and preparation of ketones and aldehydes using same |
US5677261A (en) * | 1994-11-29 | 1997-10-14 | Basf Aktiengesellschaft | Preparation of a catalyst consisting of a carrier and a catalytically active oxide material applied to the surface of the carrier |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7731916B2 (en) | 2004-05-07 | 2010-06-08 | Basf Aktiengesellschaft | Method of charging catalyst tubes of a bundle of catalyst tubes in a structured fashion |
CN100415356C (zh) * | 2004-06-24 | 2008-09-03 | 华东理工大学 | 一种适用于高热敏性物质的气固相反应装置 |
WO2008120956A1 (en) * | 2007-04-03 | 2008-10-09 | Lg Chem, Ltd. | Method for preparing unsaturated aldehyde and/or unsaturated fatty acid using fixed-bed catalytic partial oxidation reactor |
US8013185B2 (en) | 2007-04-03 | 2011-09-06 | Lg Chem, Ltd. | Method for preparing unsaturated aldehyde and/or unsaturated fatty acid using fixed-bed catalytic partial oxidation reactor |
DE102007017080A1 (de) | 2007-04-10 | 2008-10-16 | Basf Se | Verfahren zur Beschickung eines Längsabschnitts eines Kontaktrohres |
US9216395B2 (en) | 2007-04-10 | 2015-12-22 | Basf Se | Process for charging a longitudinal section of a catalyst tube |
US8598065B2 (en) | 2007-04-10 | 2013-12-03 | Basf Se | Process for charging a longitudinal section of a catalyst tube |
US8076510B2 (en) | 2007-04-24 | 2011-12-13 | Basf Se | Process for starting-up a heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acid or of methacrolein to methacrylic acid |
US9422218B2 (en) | 2007-06-01 | 2016-08-23 | Basf Se | Process for recharging the reaction tubes of a tube bundle reactor with a new fixed catalyst bed |
US9126171B2 (en) | 2007-06-01 | 2015-09-08 | Basf Se | Process for recharging the reaction tubes of a tube bundle reactor with a new fixed catalyst bed |
DE102007025869A1 (de) | 2007-06-01 | 2008-07-03 | Basf Se | Verfahren der Wiederbeschickung der Reaktionsrohre eines Rohrbündelreaktors mit einem neuen Katalysatorfestbett |
DE102007028332A1 (de) | 2007-06-15 | 2008-12-18 | Basf Se | Verfahren zum Beschicken eines Reaktors mit einem Katalysatorfestbett, das wenigstens ringförmige Katalysatorformkörper K umfasst |
DE102007028333A1 (de) | 2007-06-15 | 2008-12-18 | Basf Se | Verfahren zum Einbringen einer wenigstens einer Produktionscharge von ringförmigen Schalenkatalysatoren K entnommenen Teilmenge in ein Reaktionsrohr eines Rohrbündelreaktors |
CN109701454A (zh) * | 2019-01-28 | 2019-05-03 | 安庆市泰发能源科技有限公司 | 丁烷脱氢开工循环升温装置 |
CN109701454B (zh) * | 2019-01-28 | 2024-02-13 | 安庆市泰发能源科技有限公司 | 丁烷脱氢开工循环升温装置 |
CN115999320A (zh) * | 2021-10-22 | 2023-04-25 | 中国石油化工股份有限公司 | 一种利用熔盐溶剂回收环氧丙烷尾气方法 |
Also Published As
Publication number | Publication date |
---|---|
CN1615289A (zh) | 2005-05-11 |
BRPI0306797B1 (pt) | 2016-07-12 |
CN1597081A (zh) | 2005-03-23 |
US20050131254A1 (en) | 2005-06-16 |
EP1471046B1 (en) | 2019-03-06 |
US7144557B2 (en) | 2006-12-05 |
EP2361899A3 (en) | 2012-03-28 |
EP1471046A1 (en) | 2004-10-27 |
CN1597080A (zh) | 2005-03-23 |
ES2547074T3 (es) | 2015-10-01 |
EP2361899A2 (en) | 2011-08-31 |
US20040249203A1 (en) | 2004-12-09 |
EP2361899B1 (en) | 2015-07-22 |
BR0306797A (pt) | 2004-12-07 |
EP1471046A4 (en) | 2006-08-16 |
US7297814B2 (en) | 2007-11-20 |
CN1277790C (zh) | 2006-10-04 |
AU2003201861A1 (en) | 2003-07-30 |
ES2719089T3 (es) | 2019-07-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2003059857A1 (en) | Multipipe reactor, vapor phase catalytic oxidation method using multipipe reactor, and start-up method applied to multipipe reactor | |
RU2218301C2 (ru) | Способ и устройство для получения синтез-газа | |
US5846494A (en) | Reactor for catalytically processing gaseous fluids | |
AU2681600A (en) | Heat exchanger | |
EP1113238A3 (en) | Shell and tube type heat exchanger | |
WO2007008581A2 (en) | Thermally coupled monolith reactor | |
EP1767266A4 (en) | HEAT EXCHANGE REACTOR | |
JP2009034682A (ja) | 熱交換器の管束を内蔵した触媒燃焼反応器及び触媒構造体 | |
EP0777098A2 (en) | Improved heat exchanger for use in high temperature applications | |
CN105782962A (zh) | 一种催化燃烧节能供热系统 | |
CN1181023C (zh) | 甲醇合成工艺和设备 | |
RU2552623C2 (ru) | Теплообменник для охлаждения горячих газов и теплообменная система | |
EP2237871B1 (en) | Method of converting a raw material stream into a product stream using a fluidized bed and apparatus for use in said method | |
CN201842639U (zh) | 一种利用催化燃烧反应作为热源的管壳式反应器 | |
WO2001012310A1 (en) | Catalyst tubes for endothermic reaction especially for the production of hydrogen and syngas | |
CA2480346C (en) | Reaction apparatus and reaction method | |
CN101936535A (zh) | 远红外电热管加热及低温催化焚烧废气的涂漆钢带烘烤方法及其催化焚烧炉 | |
CN100351009C (zh) | 用于在伪等温条件下执行化学反应的方法 | |
WO2006036824A3 (en) | Apparatus and method for preferential oxidation of carbon monoxide | |
DK1393798T3 (da) | Fremgangsmåde til udførelse af kemiske reaktioner under pseudo-isoterme betingelser | |
CA2309047A1 (en) | Catalytic combustion heater | |
CN204730734U (zh) | 温度可控的分段式换热器 | |
JP2817236B2 (ja) | メタノール改質反応装置 | |
CN101077855B (zh) | 利用脱氢反应余热连续脱氢生产草酸钠的工艺及设备 | |
RU2417834C1 (ru) | Конвектор для осуществления газофазных каталитических процессов |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SC SD SE SG SK SL TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 10887868 Country of ref document: US Ref document number: 20038021722 Country of ref document: CN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003201861 Country of ref document: AU |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003700524 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1761/CHENP/2004 Country of ref document: IN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2004124371 Country of ref document: RU |
|
WWP | Wipo information: published in national office |
Ref document number: 2003700524 Country of ref document: EP |