SG102053A1 - Reactor filled with solid particle and gas-phase catalytic oxidation with the reactor - Google Patents

Reactor filled with solid particle and gas-phase catalytic oxidation with the reactor

Info

Publication number
SG102053A1
SG102053A1 SG200203373A SG200203373A SG102053A1 SG 102053 A1 SG102053 A1 SG 102053A1 SG 200203373 A SG200203373 A SG 200203373A SG 200203373 A SG200203373 A SG 200203373A SG 102053 A1 SG102053 A1 SG 102053A1
Authority
SG
Singapore
Prior art keywords
reactor
gas
solid particle
catalytic oxidation
phase catalytic
Prior art date
Application number
SG200203373A
Other languages
English (en)
Inventor
Matsumoto Yukihiro
Nishimura Takeshi
Nakahara Sei
Kasaya Naoto
Original Assignee
Nippon Catalytic Chem Ind
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 Nippon Catalytic Chem Ind filed Critical Nippon Catalytic Chem Ind
Publication of SG102053A1 publication Critical patent/SG102053A1/en

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
    • B01J8/067—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
    • B01J8/02—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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/001—Controlling 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • 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
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • B01J2208/00061—Temperature measurement of the reactants
    • 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
    • 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
    • B01J2208/00513—Controlling the temperature using inert heat absorbing solids in the bed
    • 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
    • B01J2208/00539—Pressure
    • 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
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/021—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles comprising a plurality of beds with flow of reactants in parallel
    • 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
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023—Details
    • B01J2208/024—Particulate material
    • B01J2208/025—Two or more types of catalyst
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00761—Details of the reactor
    • B01J2219/00763—Baffles
    • B01J2219/00765—Baffles attached to the reactor wall
    • B01J2219/00777—Baffles attached to the reactor wall horizontal

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
SG200203373A 2001-06-26 2002-06-07 Reactor filled with solid particle and gas-phase catalytic oxidation with the reactor SG102053A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001193137A JP4092090B2 (ja) 2001-06-26 2001-06-26 固体粒子充填反応器およびその反応器を用いた接触気相酸化方法

Publications (1)

Publication Number Publication Date
SG102053A1 true SG102053A1 (en) 2004-02-27

Family

ID=19031477

Family Applications (1)

Application Number Title Priority Date Filing Date
SG200203373A SG102053A1 (en) 2001-06-26 2002-06-07 Reactor filled with solid particle and gas-phase catalytic oxidation with the reactor

Country Status (11)

Country Link
US (2) US20030006026A1 (de)
EP (1) EP1270065B1 (de)
JP (1) JP4092090B2 (de)
KR (1) KR100623638B1 (de)
CN (2) CN1853767A (de)
BR (1) BR0202414B1 (de)
DE (1) DE60235939D1 (de)
IN (1) IN206405B (de)
MY (1) MY151079A (de)
SG (1) SG102053A1 (de)
ZA (1) ZA200204622B (de)

Families Citing this family (73)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1607032A (zh) 2001-12-28 2005-04-20 三菱化学株式会社 装填催化剂的方法
JP4424991B2 (ja) * 2002-02-27 2010-03-03 ビーエーエスエフ ソシエタス・ヨーロピア ホスゲンを製造するための反応器およびホスゲンの製造方法
AU2003211899B2 (en) * 2002-03-11 2008-09-25 Mitsubishi Chemical Corporation Process for catalytic vapor phase oxidation
US7285251B2 (en) * 2003-03-28 2007-10-23 Tubemaster Inc. Tool for loading reactor tubes
JP4838585B2 (ja) * 2003-07-14 2011-12-14 三菱レイヨン株式会社 固定床多管式反応器
JP2007522104A (ja) * 2003-12-23 2007-08-09 ビーエーエスエフ　アクチェンゲゼルシャフト Ｃ３および／またはｃ４−前駆化合物の不均一系触媒部分酸化による（メタ）アクロレインおよび／または（メタ）アクリル酸の製造法
DE10361456A1 (de) * 2003-12-23 2005-07-28 Basf Ag Verfahren zur Herstellung von (Meth)acrolein und/oder (Meth)acrylsäure durch heterogen katalysierte Partialoxidation von C3 und/oder C4-Vorläuferverbindungen
KR101237662B1 (ko) 2004-05-07 2013-02-26 바스프 에스이 촉매 튜브 다발의 촉매 튜브를 구조화된 방식으로 충진하는방법
DE102004023249A1 (de) * 2004-05-07 2005-03-10 Basf Ag Verfahren zur strukturierten Befüllung von Kontaktrohren eines Kontaktrohrbündels
JP2005325044A (ja) * 2004-05-13 2005-11-24 Mitsubishi Chemicals Corp 多管式反応器のパイロットテスト方法
DE102004025872A1 (de) * 2004-05-27 2005-12-22 Degussa Ag Verfahren zur Messung der gleichmäßigen Befüllung von Reaktoren mit Festkörpern
WO2005115608A1 (ja) * 2004-05-28 2005-12-08 Sumitomo Chemical Company, Limited 熱交換型反応器
DE102004040472A1 (de) * 2004-08-20 2006-03-02 Man Dwe Gmbh Verfahren und Rohrbündelreaktor zur Durchführung endothermer oder exothermer Gasphasenreaktionen
US7371361B2 (en) * 2004-11-03 2008-05-13 Kellogg Brown & Root Llc Maximum reaction rate converter system for exothermic reactions
KR100868454B1 (ko) * 2005-07-08 2008-11-11 주식회사 엘지화학 고정층 촉매 부분산화 반응기에서 고효율의 불포화산의제조방법
KR100833057B1 (ko) * 2005-11-23 2008-05-27 주식회사 엘지화학 관형 고정층 촉매 반응기에서 온도를 측정하는 도구 및방법
JP2006142299A (ja) * 2005-12-16 2006-06-08 Sumitomo Chemical Co Ltd 固定床多管式反応器
JP4549290B2 (ja) * 2005-12-16 2010-09-22 住友化学株式会社 多管式反応装置
JP4582039B2 (ja) * 2006-03-30 2010-11-17 住友化学株式会社 温度測定装置又はその保護管の設置方法
US7884235B2 (en) * 2006-07-20 2011-02-08 Nippon Shokubai Co., Ltd. Method for gas-phase catalytic oxidation using a fixed bed reactor
JP5311751B2 (ja) * 2007-03-09 2013-10-09 株式会社日本触媒 固定床反応装置およびその使用方法
JP2008024644A (ja) * 2006-07-20 2008-02-07 Nippon Shokubai Co Ltd 固定床反応装置およびその使用方法
DE102007017080A1 (de) * 2007-04-10 2008-10-16 Basf Se Verfahren zur Beschickung eines Längsabschnitts eines Kontaktrohres
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
DE102007031028A1 (de) * 2007-07-04 2009-01-08 Hte Ag The High Throughput Experimentation Company Steckverbindungsvorrichtung mit Temperaturmesskern
WO2009017074A1 (ja) * 2007-07-27 2009-02-05 Nippon Shokubai Co., Ltd. 二段接触気相酸化によるアクリル酸の製造方法
JP2009082865A (ja) * 2007-10-02 2009-04-23 Sumitomo Chemical Co Ltd 不飽和アルデヒド製造用触媒又は不飽和カルボン酸製造用触媒の充填方法
DE102007061477A1 (de) 2007-12-20 2009-07-02 Man Dwe Gmbh Rohrbündelreaktor
CN101977677B (zh) * 2008-01-25 2015-02-18 巴斯夫欧洲公司 进行高压反应的反应器,启动的方法和进行反应的方法
JP5563744B2 (ja) * 2008-03-31 2014-07-30 三菱化学株式会社 プレート式反応器に温度測定装置を設置する方法、及びプレート式反応器
US7951341B2 (en) 2008-06-25 2011-05-31 Uop Llc Reactor design for smaller batch transfers of catalyst
JPWO2010001732A1 (ja) * 2008-06-30 2011-12-15 株式会社日本触媒 固定床多管式反応器への固体粒状物の充填方法
ES2735985T3 (es) * 2008-09-26 2019-12-23 Univ Ohio State Conversión de combustibles carbonosos en portadores de energía libre de carbono
EP3431175B1 (de) * 2008-11-25 2022-11-30 Mitsubishi Chemical Corporation Verfahren zum packen eines bepackungsmaterials in einen reaktor vom platten-typ
AU2010292310B2 (en) 2009-09-08 2017-01-12 The Ohio State University Research Foundation Synthetic fuels and chemicals production with in-situ CO2 capture
DE102009047291A1 (de) 2009-11-30 2010-09-23 Basf Se Verfahren zur Herstellung von (Meth)acrolein durch heterogen katalysierte Gasphasen-Partialoxidation
DE102010006723A1 (de) * 2010-02-03 2011-08-04 Süd-Chemie AG, 80333 Reaktorvorrichtung und Verfahren zur Optimierung der Messung des Temperaturverlaufs in Reaktorrohren
JP5780069B2 (ja) * 2010-09-07 2015-09-16 三菱化学株式会社 共役ジエンの製造方法
DE102010048405A1 (de) 2010-10-15 2011-05-19 Basf Se Verfahren zum Langzeitbetrieb einer heterogen katalysierten partiellen Gasphasenoxidation von Proben zu Acrolein
CN103354763B (zh) 2010-11-08 2016-01-13 俄亥俄州立大学 具有反应器之间的气体密封和移动床下导管的循环流化床
JP5618800B2 (ja) * 2010-12-09 2014-11-05 株式会社日本触媒 固定床多管式反応器および該固定床多管式反応器を用いた不飽和アルデヒドおよび／または不飽和カルボン酸の製造方法
CN103635449B (zh) 2011-05-11 2016-09-07 俄亥俄州国家创新基金会 用来转化燃料的系统
AU2012253332B2 (en) 2011-05-11 2017-05-11 Ohio State Innovation Foundation Oxygen carrying materials
EP2814910A4 (de) * 2012-02-17 2015-11-11 Ceramatec Inc Erweitertes fischer-tropsch-system
WO2013126341A1 (en) 2012-02-21 2013-08-29 Ceramatec, Inc. Compact fischer tropsch system with integrated primary and secondary bed temperature control
US9162935B2 (en) 2012-02-21 2015-10-20 Ceramatec, Inc. Compact FT combined with micro-fibrous supported nano-catalyst
US9174910B2 (en) 2012-03-29 2015-11-03 Nippon Shokubai Co., Ltd. Method for producing acrylic acid with a fixed-bed multitubular reactor
CN104203883B (zh) 2012-03-30 2015-11-25 株式会社日本触媒 使用固定床多管式反应器的丙烯醛和丙烯酸的制备方法
CN103055767B (zh) * 2012-12-10 2015-04-29 中国石油集团东北炼化工程有限公司吉林设计院 丙烯酸生产中反应器上安装热电偶用装置
CN109536210B (zh) 2013-02-05 2020-12-18 俄亥俄州国家创新基金会 用于碳质燃料转化的方法
JP2016539936A (ja) 2013-11-11 2016-12-22 ビーエーエスエフ ソシエタス・ヨーロピアＢａｓｆ Ｓｅ 不飽和アルデヒド及び／又は不飽和カルボン酸の製造法
MY173267A (en) 2013-11-11 2020-01-09 Basf Se Mechanically stable hollow-cylindrical moulded catalyst body for the gas phase oxidation of an alkene in order to obtain an unsaturated aldehyde and/or an unsaturated carboxylic acid
US20150238915A1 (en) 2014-02-27 2015-08-27 Ohio State Innovation Foundation Systems and methods for partial or complete oxidation of fuels
JP6422764B2 (ja) * 2014-12-19 2018-11-14 住友化学株式会社 触媒の充填方法
DE102014018825A1 (de) 2014-12-19 2016-06-23 Man Diesel & Turbo Se Faseroptische Temperaturmessung
CA2904477A1 (en) * 2015-09-14 2017-03-14 Nova Chemicals Corporation Heat dissipating diluent in fixed bed reactors
LU93012B1 (en) * 2016-04-04 2017-11-08 Cppe Carbon Process & Plant Eng S A En Abrege Cppe S A Sulfur dioxide removal from waste gas
CA3020406A1 (en) 2016-04-12 2017-10-19 Ohio State Innovation Foundation Chemical looping syngas production from carbonaceous fuels
EP3445738B1 (de) * 2016-04-21 2022-02-16 Rohm and Haas Company Verfahren zur verwendung makroporöser inerter materialien bei der monomerproduktion
CN106475020B (zh) * 2016-10-20 2019-01-29 中国石油化工股份有限公司 一种用于异丙苯催化氧化制过氧化氢异丙苯的振荡流反应器及方法
US11090624B2 (en) 2017-07-31 2021-08-17 Ohio State Innovation Foundation Reactor system with unequal reactor assembly operating pressures
CN108314611B (zh) * 2017-12-27 2021-04-27 福建南平青松化工有限公司 异龙脑连续气相脱氢制樟脑的设备及生产工艺
US10549236B2 (en) 2018-01-29 2020-02-04 Ohio State Innovation Foundation Systems, methods and materials for NOx decomposition with metal oxide materials
JP6907981B2 (ja) * 2018-03-23 2021-07-21 三菱ケミカル株式会社 縦型多管式反応器
CN108654523B (zh) * 2018-06-15 2023-10-13 中国五环工程有限公司 列管式反应器催化剂的装填结构
WO2020033500A1 (en) 2018-08-09 2020-02-13 Ohio State Innovation Foundation Systems, methods and materials for hydrogen sulfide conversion
CN109304133B (zh) * 2018-11-21 2024-03-05 爱润森德（天津）能源科技有限公司 一种用于加氢反应的加氢反应器装置
CA3129146A1 (en) 2019-04-09 2020-10-15 Liang-Shih Fan Alkene generation using metal sulfide particles
WO2021124696A1 (ja) * 2019-12-16 2021-06-24 昭和電工株式会社 酢酸アルケニル製造用固定床多管式反応器
JP7287312B2 (ja) * 2020-02-26 2023-06-06 三菱ケミカル株式会社 多管式反応器への粒状物の充填方法
CN116457083A (zh) * 2020-11-27 2023-07-18 株式会社力森诺科 乙酸烯基酯制造用固定床多管式反应器
CN113041968B (zh) * 2021-03-12 2022-07-01 烟台大学 一种微反应器系统内基于Pickering乳液固体输送的方法

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3656914A (en) * 1969-03-15 1972-04-18 Basf Ag Filled reaction tube provided with temperature sensors
US4929798A (en) * 1984-03-05 1990-05-29 Canadian Patents And Development Limited Pseudoadiabatic reactor for exothermal catalytic conversions
WO2000017946A2 (en) * 1998-09-22 2000-03-30 Celanese International Corporation Method of evaluating a reaction for thermal runaway within a shell and tube reactor

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US492798A (en) * 1893-03-07 Sole-inking machine
US2148706A (en) * 1937-10-09 1939-02-28 Harry C Morrow Protective temperature measuring device for pickling tanks
NL6918448A (de) * 1968-12-16 1970-06-18
US3955419A (en) * 1974-06-20 1976-05-11 Westinghouse Electric Corporation Multiple sensor temperature measuring device
US4224187A (en) * 1978-11-13 1980-09-23 Celanese Corporation Olefin oxidation catalyst and process for its preparation
DE4431949A1 (de) * 1994-09-08 1995-03-16 Basf Ag Verfahren zur katalytischen Gasphasenoxidation von Acrolein zu Acrylsäure
JPH10152509A (ja) * 1996-05-14 1998-06-09 Mitsui Chem Inc 気相重合方法及びそのための気相重合装置ならびにブロワー
DE19717165A1 (de) * 1997-04-23 1998-10-29 Basf Ag Vorrichtung und Verfahren zur Temperaturmessung in Rohrreaktoren
JP3732080B2 (ja) 1999-08-31 2006-01-05 株式会社日本触媒 接触気相酸化反応器
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.

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3656914A (en) * 1969-03-15 1972-04-18 Basf Ag Filled reaction tube provided with temperature sensors
US4929798A (en) * 1984-03-05 1990-05-29 Canadian Patents And Development Limited Pseudoadiabatic reactor for exothermal catalytic conversions
WO2000017946A2 (en) * 1998-09-22 2000-03-30 Celanese International Corporation Method of evaluating a reaction for thermal runaway within a shell and tube reactor

Also Published As

Publication number Publication date
EP1270065B1 (de) 2010-04-14
IN206405B (de) 2006-04-07
ZA200204622B (en) 2003-02-13
JP4092090B2 (ja) 2008-05-28
US20070003460A1 (en) 2007-01-04
KR20030004074A (ko) 2003-01-14
CN1394671A (zh) 2003-02-05
KR100623638B1 (ko) 2006-09-18
MY151079A (en) 2014-04-15
EP1270065A1 (de) 2003-01-02
BR0202414B1 (pt) 2013-01-22
CN1289178C (zh) 2006-12-13
US20030006026A1 (en) 2003-01-09
US7534339B2 (en) 2009-05-19
JP2003001094A (ja) 2003-01-07
DE60235939D1 (de) 2010-05-27
CN1853767A (zh) 2006-11-01
BR0202414A (pt) 2003-04-29

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