MY151079A - Reactor filled with sold particle and gas-phase catalytic oxidation with the reactor - Google Patents

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

Info

Publication number
MY151079A
MY151079A MYPI20022174A MY151079A MY 151079 A MY151079 A MY 151079A MY PI20022174 A MYPI20022174 A MY PI20022174A MY 151079 A MY151079 A MY 151079A
Authority
MY
Malaysia
Prior art keywords
reactor
gas
filled
catalytic oxidation
phase catalytic
Prior art date
Application number
Other languages
English (en)
Inventor
Yukihiro Matsumoto
Takeshi Nishimura
Sei Nakahara
Naoto Kasaya
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 MY151079A publication Critical patent/MY151079A/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)
MYPI20022174 2001-06-26 2002-06-11 Reactor filled with sold particle and gas-phase catalytic oxidation with the reactor MY151079A (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
MY151079A true MY151079A (en) 2014-04-15

Family

ID=19031477

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI20022174 MY151079A (en) 2001-06-26 2002-06-11 Reactor filled with sold particle and gas-phase catalytic oxidation with the reactor

Country Status (11)

Country Link
US (2) US20030006026A1 (OSRAM)
EP (1) EP1270065B1 (OSRAM)
JP (1) JP4092090B2 (OSRAM)
KR (1) KR100623638B1 (OSRAM)
CN (2) CN1289178C (OSRAM)
BR (1) BR0202414B1 (OSRAM)
DE (1) DE60235939D1 (OSRAM)
IN (1) IN206405B (OSRAM)
MY (1) MY151079A (OSRAM)
SG (1) SG102053A1 (OSRAM)
ZA (1) ZA200204622B (OSRAM)

Families Citing this family (77)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100349648C (zh) * 2001-12-28 2007-11-21 三菱化学株式会社 汽相催化氧化方法
WO2003072237A1 (de) * 2002-02-27 2003-09-04 Basf Aktiengesellschaft Reaktor und verfahren zur herstellung von phosgen
RU2295383C2 (ru) 2002-03-11 2007-03-20 Мицубиси Кемикал Корпорейшн Способ каталитического окисления в паровой фазе
US7285251B2 (en) * 2003-03-28 2007-10-23 Tubemaster Inc. Tool for loading reactor tubes
CN100377773C (zh) * 2003-07-14 2008-04-02 三菱丽阳株式会社 固定床多管式反应器
EP1699749B1 (de) * 2003-12-23 2015-09-09 Basf Se Verfahren zur herstellung von (meth)acrolein und/oder (meth)acrylsäure durch heterogen katalysierte partialoxidation von c3 und/oder c4-vorlä uferverbindungen
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
BRPI0509632B1 (pt) 2004-05-07 2015-09-08 Basf Ag processo para carregamento de tubos de contato de um feixe de tubos de contato de uma maneira estruturada
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
CN1988950B (zh) * 2004-05-28 2012-09-05 住友化学株式会社 热交换型反应器
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
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
US7884235B2 (en) * 2006-07-20 2011-02-08 Nippon Shokubai Co., Ltd. Method for gas-phase catalytic oxidation using a fixed bed 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
DE102007031028A1 (de) * 2007-07-04 2009-01-08 Hte Ag The High Throughput Experimentation Company Steckverbindungsvorrichtung mit Temperaturmesskern
JPWO2009017074A1 (ja) * 2007-07-27 2010-10-21 株式会社日本触媒 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
WO2009092724A1 (de) * 2008-01-25 2009-07-30 Basf Se Reaktor zur durchführung von hochdruckreaktionen, verfahren zur inbetriebnahme sowie verfahren zur durchführung einer reaktion
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
EP2295136A4 (en) * 2008-06-30 2011-12-28 Nippon Catalytic Chem Ind METHOD OF PACKAGING A SOLID PARTICLE SUBSTANCE IN A MULTI-TUBE FIXED BED REACTOR
WO2010037011A2 (en) * 2008-09-26 2010-04-01 The Ohio State University Conversion of carbonaceous fuels into carbon free energy carriers
EP2363203B1 (en) * 2008-11-25 2020-03-25 Mitsubishi Chemical Corporation Method of reaction using heat-exchange type reactor
CA3011693C (en) 2009-09-08 2021-03-09 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
WO2012064712A1 (en) 2010-11-08 2012-05-18 The Ohio State University Circulating fluidized bed with moving bed downcomers and gas sealing between reactors
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
WO2012155054A1 (en) 2011-05-11 2012-11-15 The Ohio State University Systems for converting fuel
EP3584426B1 (en) 2011-05-11 2021-04-14 Ohio State Innovation Foundation Oxygen carrying materials
EP2814910A4 (en) * 2012-02-17 2015-11-11 Ceramatec Inc EXTENDED FISCHER TROPSCH SYSTEM
WO2013126449A1 (en) 2012-02-21 2013-08-29 Ceramatec, Inc. Compact ft combined with micro-fibrous supported nano-catalyst
US9199215B2 (en) 2012-02-21 2015-12-01 Ceramatec, Inc. Compact Fischer Tropsch system with integrated primary and secondary bed temperature control
EP2832718B1 (en) 2012-03-29 2020-01-08 Nippon Shokubai Co., Ltd. Process for producing acrylic acid using fixed-bed multitubular reactor
US9073845B2 (en) 2012-03-30 2015-07-07 Nippon Shokubai Co., Ltd. Method for producing acrolein and acrylic acid with a fixed-bed multitubular reactor
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
WO2015067656A1 (de) 2013-11-11 2015-05-14 Basf Se Verfahren zur herstellung eines ungesättigten aldehyds und/oder einer ungesättigten carbonsäure
BR112016010410B1 (pt) 2013-11-11 2021-12-28 Basf Se Corpo de catalisador conformado em cilindro oco, e, processo para preparação de um aldeído a,ss-insaturado e um ácido carboxílico a,ss-insaturado ou ambos
WO2015131117A1 (en) 2014-02-27 2015-09-03 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
EP3429738B1 (en) 2016-04-12 2024-07-17 Ohio State Innovation Foundation Chemical looping syngas production from carbonaceous fuels
WO2017184496A1 (en) * 2016-04-21 2017-10-26 Rohm And Haas Company Methods for using macroporous inert materials in monomer production
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
CN111065459B (zh) 2017-07-31 2023-09-22 俄亥俄州立创新基金会 具有不相等反应器组件运行压力的反应器系统
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
CA3125491A1 (en) 2019-01-17 2020-07-23 Ohio State Innovation Foundation Systems, methods and materials for stable phase syngas generation
US11453626B2 (en) 2019-04-09 2022-09-27 Ohio State Innovation Foundation Alkene generation using metal sulfide particles
WO2021034888A1 (en) 2019-08-19 2021-02-25 Ohio State Innovation Foundation Mesoporous support-immobilized metal oxide-based nanoparticles
AU2020340961A1 (en) 2019-09-03 2022-03-24 Ohio State Innovation Foundation Redox reaction facilitated carbon dioxide capture from flue gas and conversion to carbon monoxide
JP6935039B1 (ja) * 2019-12-16 2021-09-15 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
WO2022113423A1 (ja) * 2020-11-27 2022-06-02 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
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
JP7738496B2 (ja) * 2022-02-04 2025-09-12 三菱重工業株式会社 熱交換器

Family Cites Families (14)

* 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
SE368777B (OSRAM) * 1968-12-16 1974-07-22 Montedison Spa
AT294018B (de) 1969-03-15 1971-11-10 Basf Ag Reaktionsrohr für Röhrenöfen sowie Verfahren zu seiner Herstellung
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
CA1223895A (en) * 1984-03-05 1987-07-07 Hugo I. De Lasa Pseudodiabatic reactor for exothermal catalytic conversions
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
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
ZA200004211B (en) * 1999-08-31 2001-02-14 Nippon Catalytic Chem Ind Method for catalytic gas phase oxidation.
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

Also Published As

Publication number Publication date
CN1853767A (zh) 2006-11-01
JP4092090B2 (ja) 2008-05-28
EP1270065A1 (en) 2003-01-02
DE60235939D1 (de) 2010-05-27
EP1270065B1 (en) 2010-04-14
US20030006026A1 (en) 2003-01-09
BR0202414B1 (pt) 2013-01-22
BR0202414A (pt) 2003-04-29
IN206405B (OSRAM) 2006-04-07
KR100623638B1 (ko) 2006-09-18
CN1289178C (zh) 2006-12-13
US7534339B2 (en) 2009-05-19
CN1394671A (zh) 2003-02-05
ZA200204622B (en) 2003-02-13
US20070003460A1 (en) 2007-01-04
KR20030004074A (ko) 2003-01-14
JP2003001094A (ja) 2003-01-07
SG102053A1 (en) 2004-02-27

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