JPS4880473A - - Google Patents

Info

Publication number
JPS4880473A
JPS4880473A JP48005611A JP561173A JPS4880473A JP S4880473 A JPS4880473 A JP S4880473A JP 48005611 A JP48005611 A JP 48005611A JP 561173 A JP561173 A JP 561173A JP S4880473 A JPS4880473 A JP S4880473A
Authority
JP
Japan
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.)
Granted
Application number
JP48005611A
Other languages
Japanese (ja)
Other versions
JPS5215272B2 (en
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 filed Critical
Publication of JPS4880473A publication Critical patent/JPS4880473A/ja
Publication of JPS5215272B2 publication Critical patent/JPS5215272B2/ja
Expired legal-status Critical Current

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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
    • F28F27/02—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus for controlling the distribution of heat-exchange media between different 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
    • 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
    • B01J2208/00106—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
    • B01J2208/00106—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
    • B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from 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
    • 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
    • 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
    • F28F2009/222—Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
    • F28F2009/226—Transversal partitions
JP48005611A 1972-01-13 1973-01-11 Expired JPS5215272B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2201528A DE2201528C2 (en) 1972-01-13 1972-01-13 Reaction apparatus for carrying out exothermic and endothermic catalytic processes with radial flow of the heat exchange medium

Publications (2)

Publication Number Publication Date
JPS4880473A true JPS4880473A (en) 1973-10-27
JPS5215272B2 JPS5215272B2 (en) 1977-04-27

Family

ID=5832921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP48005611A Expired JPS5215272B2 (en) 1972-01-13 1973-01-11

Country Status (8)

Country Link
US (1) US3871445A (en)
JP (1) JPS5215272B2 (en)
BE (1) BE793928A (en)
DE (1) DE2201528C2 (en)
FR (1) FR2168092B1 (en)
GB (1) GB1415791A (en)
IT (1) IT972669B (en)
NL (1) NL173885C (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4918768A (en) * 1972-03-07 1974-02-19
JP2002522214A (en) * 1998-08-13 2002-07-23 ビーエーエスエフ アクチェンゲゼルシャフト Reactor with contact tube nest
JP2004501759A (en) * 2000-06-29 2004-01-22 エイチ２ジーイーエヌ・イノベーションズ・インコーポレイテッド System for improved hydrogen generation by steam reforming of hydrocarbons and integrated chemical reactor for producing hydrogen from hydrocarbons
JP2010158676A (en) * 2010-02-09 2010-07-22 Mitsubishi Chemicals Corp Catalytic reactor

Families Citing this family (85)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2343788C3 (en) * 1973-08-30 1980-07-10 Wacker-Chemie Gmbh, 8000 Muenchen Device for the continuous implementation of chemical reactions, in particular polymerizations and processes for the continuous suspension polymerization of vinyl chloride
US4203906A (en) * 1977-07-13 1980-05-20 Nippon Shokubai Kagaku Kogyo Co., Ltd. Process for catalytic vapor phase oxidation
DE2903582B1 (en) * 1979-01-31 1980-11-20 Basf Ag, 6700 Ludwigshafen Tube bundle reactor for carrying out catalytic reactions in the gas phase
DE3034208A1 (en) * 1980-09-11 1982-04-22 GHT Gesellschaft für Hochtemperaturreaktor-Technik mbH, 5060 Bergisch Gladbach CANOPY WITH CATALYST MOLDED BODIES
US4635707A (en) * 1982-07-06 1987-01-13 Phillips Petroleum Company Method for varying shell fluid flow in shell and tube heat exchanger
DE3409159A1 (en) * 1984-03-13 1985-09-26 Deggendorfer Werft Und Eisenbau Gmbh, 8360 Deggendorf TUBE BUNCH REACTION APPARATUS
JPH03502422A (en) * 1988-12-13 1991-06-06 デークゲンドルファー・ヴェルフト・ウント・アイゼンバウ・ゲゼルシャフト・ミット・ベシュレンクター・ハフツング bundle tubular reactor
FR2655876B1 (en) * 1989-12-19 1994-03-11 Pecquet Tesson Ste Indle REACTOR FOR CATALYST CHEMICAL REACTIONS.
DE4013051A1 (en) * 1990-04-24 1991-11-07 Basf Ag METHOD FOR PRODUCING PHTHALIC ACID ANHYDRIDE FROM O-XYLOL
US5248483A (en) * 1991-03-28 1993-09-28 Phillips Petroleum Company Apparatus and methods for producing ceramic products
DE4123243A1 (en) * 1991-07-13 1993-01-14 Degussa TEMPERATURE VARIABLE TUBE BUNDLE HEAT EXCHANGER FOR CONSTANT QUANTITY RATIO OF EXCHANGE GAS AND HEAT EXCHANGE PROCESS
US5203405A (en) * 1992-02-03 1993-04-20 Phillips Petroleum Company Two pass shell and tube heat exchanger with return annular distributor
US5425415A (en) * 1993-06-15 1995-06-20 Abb Lummus Crest Inc. Vertical heat exchanger
DE4428018A1 (en) * 1994-08-08 1996-02-15 Bayer Ag Process for the preparation of aromatic amines
DE4428017A1 (en) * 1994-08-08 1996-02-15 Bayer Ag Process for the preparation of aromatic amines
US5544700A (en) * 1994-08-22 1996-08-13 General Electric Company Method and apparatus for preferential cooling
DE4431957A1 (en) * 1994-09-08 1995-03-16 Basf Ag Process for the catalytic gas-phase oxidation of propene to acrolein
DE4431949A1 (en) * 1994-09-08 1995-03-16 Basf Ag Process for the catalytic gas-phase oxidation of acrolein to acrylic acid
DE19542755A1 (en) 1995-11-16 1997-05-22 Basf Ag Multimetal oxides
GB9600350D0 (en) * 1996-01-09 1996-03-13 Ici Plc Heat exchange catalytic reactor
US5651386A (en) * 1996-03-14 1997-07-29 Nir; Ari Device for storing and discharging viscous liquid
DE19707943C2 (en) 1997-02-27 1999-07-08 Basf Ag Process for the preparation of phthalic anhydride and catalyst therefor
US6384274B1 (en) 1998-09-27 2002-05-07 Rohm And Haas Company Single reactor process for preparing acrylic acid from propylene having improved capacity
DE19851786A1 (en) 1998-11-10 2000-05-11 Basf Ag Multimetal oxide containing silver and vanadium oxide and its use
DE60035746T2 (en) * 1999-08-31 2008-04-30 Nippon Shokubai Co., Ltd. Reactor for catalytic gas phase oxidation
ZA200004211B (en) * 1999-08-31 2001-02-14 Nippon Catalytic Chem Ind Method for catalytic gas phase oxidation.
DE10011309A1 (en) * 2000-03-10 2001-09-13 Basf Ag Production of maleic anhydride comprises gas-phase oxidation of hydrocarbons in a reactor comprising at least two sequential cooled reaction zones at different temperatures
DE10024342A1 (en) * 2000-05-17 2001-11-22 Basf Ag Reactor having a contact tube bundle, useful for oxidation reactions, has a heat exchange agent recycle loop fed through the chamber and rotating disks that rotate in the reactor center and edge.
DE10127365A1 (en) * 2001-06-06 2002-12-12 Basf Ag Pump, used for conveying heat transfer medium, comprises housing containing guide pipe and having opening in its lower part, via which heat transfer medium removed from lower region of reactor flows into housing
JP4017928B2 (en) * 2001-07-20 2007-12-05 ビーエーエスエフ アクチェンゲゼルシャフト Reactor, pump for use in the reactor, and method for performing oxidation reaction
US7316804B2 (en) * 2001-08-02 2008-01-08 Ineos Usa Llc Flow reactors for chemical conversions with heterogeneous catalysts
DE10144857A1 (en) * 2001-09-12 2003-03-27 Deggendorfer Werft Eisenbau Reactor arrangement used for the production of phthalic acid anhydride from o-xylol and/or naphthalene has a cooling stage and a secondary reactor located in the same housing as the main reactor
WO2003076373A1 (en) * 2002-03-11 2003-09-18 Mitsubishi Chemical Corporation Process for catalytic vapor phase oxidation
US7663004B2 (en) * 2002-04-22 2010-02-16 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
US8252961B2 (en) * 2002-04-22 2012-08-28 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
US8017816B2 (en) * 2002-04-22 2011-09-13 The Curators Of The University Of Missouri Method of producing lower alcohols from glycerol
KR100450234B1 (en) * 2002-07-10 2004-09-24 주식회사 엘지화학 Catalytic oxidation reactor with enhanced heat exchanging system
EP1569745B1 (en) * 2002-12-12 2019-03-20 MAN Energy Solutions SE Shell-and-tube type reactor for catalytic gas phase reactions
DE10258180A1 (en) * 2002-12-12 2004-06-24 Basf Ag Preparation of chlorine involves oxidation of hydrogen chloride and gas stream comprising molecular oxygen in presence of fixed-bed catalyst is carried out in reactor having annular and disk-shaped deflection plates between catalyst tubes
DE10258153A1 (en) * 2002-12-12 2004-06-24 Basf Ag Preparation of chlorine by gas-phase oxidation of hydrogen chloride by a gas stream having molecular oxygen in presence of a fixed-bed catalyst is carried out in reactor having bundle of parallel catalyst tubes and deflector plate
DE10312788A1 (en) * 2003-03-21 2004-09-30 Behr Gmbh & Co. Kg Exhaust gas heat exchanger and sealing device for exhaust gas heat exchanger
DE10334132A1 (en) 2003-07-25 2005-04-07 Basf Ag Silver, vanadium and a promoter metal-containing multimetal and its use
EP1656335A1 (en) * 2003-08-14 2006-05-17 Basf Aktiengesellschaft Method for the production of (meth)acrolein and/or (meth)acrylic acid
TWI302147B (en) * 2003-09-01 2008-10-21 Lg Chemical Ltd Method of producing unsaturated aldehyde and unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
TWI288127B (en) * 2003-12-24 2007-10-11 Lg Chemical Ltd Method of producing unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system
BRPI0509632B1 (en) 2004-05-07 2015-09-08 Basf Ag process for loading contact tubes from a contact tube bundle in a structured manner
US8596858B2 (en) * 2004-09-15 2013-12-03 Kureha Corporation Apparatus for solid-liquid contact
JP4205035B2 (en) * 2004-09-27 2009-01-07 住友化学株式会社 Multi-tube reactor for catalytic gas phase reaction
KR100677051B1 (en) * 2005-03-18 2007-02-01 주식회사 엘지화학 Method of producing unsaturated acid from olefin
KR100838970B1 (en) * 2005-04-29 2008-06-16 주식회사 엘지화학 Annular-type distributor with improved flow uniformity
US20070135301A1 (en) * 2005-12-08 2007-06-14 Sud-Chemie Inc. Catalyst for the production of polyols by hydrogenolysis of carbohydrates
KR100886083B1 (en) * 2006-01-31 2009-02-26 주식회사 엘지화학 Reactor with improved heat transfer performance, and method for producing oxide by using the reactor
EP1734030A1 (en) 2006-01-18 2006-12-20 BASF Aktiengesellschaft Method for long term operation of a heterogeneously catalysed gas phase partial oxidation of an organic educt
KR100898692B1 (en) * 2006-01-18 2009-05-22 주식회사 엘지화학 Reactor with improved heat transfer performance, method for producing oxide by using the reactor, and method for increasing parallel flow of heat transfer rate
WO2007083927A1 (en) * 2006-01-18 2007-07-26 Lg Chem, Ltd. Reactor with improved heat transfer performance
KR100847199B1 (en) * 2006-01-31 2008-07-17 주식회사 엘지화학 Reactor with improved heat transfer performance, method for producing oxide by using the reactor, and method for increasing
DE102006007619A1 (en) * 2006-02-18 2007-08-23 Bayer Materialscience Ag Preparing aniline, useful to prepare e.g. di- and polyamine, comprises hydrogenating nitrobenzene to obtain raw aniline, extracting raw aniline with aqueous alkali metal hydroxide solution and separating aqueous- and organic phase
DE102006007620A1 (en) * 2006-02-18 2007-08-23 Bayer Materialscience Ag Production of crude aniline for use in producing di- and polyamines, involves purifying crude aniline by adding aqueous alkali metal hydroxide solution to crude aniline prior to and/or during distillation
TWI322882B (en) * 2006-02-24 2010-04-01 Lg Chemical Ltd Annular distributor having guide vane to improve flow rate distribution, reactor/heat exchanger including the annular distributor and method of producing unsaturated aldehyde or unsaturated acid from olefin by catalytic gas phase oxidation in the reactor
DE102006035203A1 (en) * 2006-07-29 2008-01-31 Bayer Materialscience Ag Process for the preparation of aromatic amines
DE102006052989A1 (en) * 2006-11-10 2008-05-15 Bayer Materialscience Ag Process for the removal of compounds with phenolic hydroxy groups from aromatic amines
DE102007010422A1 (en) 2007-03-01 2008-09-04 Basf Se Preparation of a catalyst, useful in the heterogeneously catalyzed partial gas phase oxidation of acrolein to acrylic acid, comprises attaching one of the active mass to the surface of the carrier body with the help of a binding agent
DE102007017080A1 (en) 2007-04-10 2008-10-16 Basf Se Method for feeding a longitudinal section of a contact tube
DE102007028332A1 (en) 2007-06-15 2008-12-18 Basf Se A method for feeding a reactor with a fixed catalyst bed comprising at least annular shaped catalyst bodies K.
DE102007039091A1 (en) 2007-08-18 2009-02-19 Bayer Materialscience Ag Process for the purification of aromatic amines
DE102007045125A1 (en) 2007-09-20 2009-04-02 Bayer Technology Services Gmbh Process for the preparation of aromatic amines
DE102007048441A1 (en) * 2007-10-10 2009-04-16 Bomat Heiztechnik Gmbh heat exchangers
DE102007061477A1 (en) 2007-12-20 2009-07-02 Man Dwe Gmbh Tube reactor
DE102009019436A1 (en) 2009-04-29 2010-11-04 Bayer Materialscience Ag Process for the preparation of aromatic amines
DE102009025374A1 (en) 2009-06-18 2010-12-23 Bayer Materialscience Ag Process for the preparation of aromatic amines
DE102009047291A1 (en) 2009-11-30 2010-09-23 Basf Se Producing (meth)acrolein, by heterogeneous catalyzed gas phase-partial oxidation, comprises guiding reaction gas mixture through a fresh fixed catalyst bed present in a reactor at increased temperature
US20130204043A1 (en) 2010-07-30 2013-08-08 Bayer Intellectual Property GmbH Creative Campus Monheim Method for continuously producing nitrobenzene
DE102010048405A1 (en) 2010-10-15 2011-05-19 Basf Se Long term operation of heterogeneously catalyzed partial gas phase oxidation of propene to acrolein, comprises conducting reaction gas input mixture containing propene, molecular oxygen and inert gas, through solid catalyst bed
KR20140043059A (en) 2011-01-11 2014-04-08 바이엘 인텔렉쳐 프로퍼티 게엠베하 Process for preparing aromatic amines
DE102011076931A1 (en) 2011-06-03 2012-12-06 Basf Se Aqueous solution containing acrylic acid and its conjugate base
DE102011084476A1 (en) * 2011-10-13 2013-04-18 Man Diesel & Turbo Se Tube reactor
EP2653462A1 (en) 2012-04-16 2013-10-23 Bayer MaterialScience AG Method for improved starting the reaction when producing aromatic amines from nitroaromatics
EP2653461A1 (en) 2012-04-16 2013-10-23 Bayer MaterialScience AG Method for improved stopping of the reaction when producing aromatic amines from nitroaromatics
DE102012207811A1 (en) 2012-05-10 2012-07-12 Basf Se Heterogeneously catalyzed gas phase partial oxidation of (meth)acrolein to (meth)acrylic acid using a catalytically active multimetal oxide mass
DE102013218628A1 (en) 2013-09-17 2014-03-06 Basf Se Catalyst useful for producing alpha, beta-unsaturated carboxylic acid by gas phase oxidation of alpha, beta-unsaturated aldehyde, comprises support molded body with active material applied on support molded body
DE102014203725A1 (en) 2014-02-28 2015-09-03 Basf Se Oxidation catalyst with saddle-shaped carrier shaped body
DE102016002679A1 (en) 2016-03-04 2017-09-21 Hans-Jürgen Eberle Apparatus and method for carrying out heterogeneously catalyzed exothermic gas phase reactions
CN105890402B (en) * 2016-06-07 2018-01-30 纳盛洁净技术（苏州）有限公司 A kind of muitishell shell-and-tube heat exchanger
EP3360611B1 (en) * 2017-02-10 2021-04-28 Technobell D.O.O. Koper Improved double zone tubular reactor and method for carrying out maleic anhydride production by n-butane oxidation
EP3643699B1 (en) 2018-10-17 2021-09-22 Covestro Intellectual Property GmbH & Co. KG Method for the purification of aniline

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US3490521A (en) * 1968-03-12 1970-01-20 Westinghouse Electric Corp Tube and shell heat exchanger
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4918768A (en) * 1972-03-07 1974-02-19
JP2002522214A (en) * 1998-08-13 2002-07-23 ビーエーエスエフ アクチェンゲゼルシャフト Reactor with contact tube nest
JP2004501759A (en) * 2000-06-29 2004-01-22 エイチ２ジーイーエヌ・イノベーションズ・インコーポレイテッド System for improved hydrogen generation by steam reforming of hydrocarbons and integrated chemical reactor for producing hydrogen from hydrocarbons
JP2010158676A (en) * 2010-02-09 2010-07-22 Mitsubishi Chemicals Corp Catalytic reactor

Also Published As

Publication number Publication date
DE2201528C2 (en) 1974-12-12
NL7300127A (en) 1973-07-17
JPS5215272B2 (en) 1977-04-27
BE793928A (en) 1973-05-02
US3871445A (en) 1975-03-18
NL173885C (en) 1984-03-16
DE2201528B1 (en) 1972-11-02
IT972669B (en) 1974-05-31
FR2168092A1 (en) 1973-08-24
GB1415791A (en) 1975-11-26
FR2168092B1 (en) 1977-07-29

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