DE60222630D1 - Reaktor und kühlersystem für exotherme reaktionen - Google Patents

Reaktor und kühlersystem für exotherme reaktionen

Info

Publication number
DE60222630D1
DE60222630D1 DE60222630T DE60222630T DE60222630D1 DE 60222630 D1 DE60222630 D1 DE 60222630D1 DE 60222630 T DE60222630 T DE 60222630T DE 60222630 T DE60222630 T DE 60222630T DE 60222630 D1 DE60222630 D1 DE 60222630D1
Authority
DE
Germany
Prior art keywords
reactor
cooler system
exothermal reactions
heat exchanger
exothermal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
DE60222630T
Other languages
English (en)
Other versions
DE60222630T2 (de
DE60222630T3 (de
Inventor
Barry Billig
Bhupendra Ranibhai Baria
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Scientific Design Co Inc
Original Assignee
Scientific Design Co Inc
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
Priority claimed from US09/779,030 external-priority patent/US7294317B2/en
Application filed by Scientific Design Co Inc filed Critical Scientific Design Co Inc
Publication of DE60222630D1 publication Critical patent/DE60222630D1/de
Publication of DE60222630T2 publication Critical patent/DE60222630T2/de
Application granted granted Critical
Publication of DE60222630T3 publication Critical patent/DE60222630T3/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0476—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more otherwise shaped beds
    • B01J8/048—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more otherwise shaped beds the beds being superimposed one above the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—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
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D301/00—Preparation of oxiranes
    • C07D301/02—Synthesis of the oxirane ring
    • C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
    • C07D301/04—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen
    • C07D301/08—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase
    • C07D301/10—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase with catalysts containing silver or gold
    • 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
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • 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
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0083—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
    • F28D7/0091—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium the supplementary medium flowing in series through the units
    • 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
    • B01J2208/00522—Controlling the temperature using inert heat absorbing solids outside 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
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Epoxy Compounds (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Saccharide Compounds (AREA)
  • Steering Control In Accordance With Driving Conditions (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
DE60222630.9T 2001-02-08 2002-01-24 Reaktor und kühlersystem für exotherme reaktionen Expired - Lifetime DE60222630T3 (de)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US779030 2001-02-08
US09/779,030 US7294317B2 (en) 2001-02-08 2001-02-08 Exothermic reaction system
PCT/US2002/002197 WO2002063230A1 (en) 2001-02-08 2002-01-24 Exothermic reaction system
EP02707569.6A EP1358441B2 (de) 2001-02-08 2002-01-24 Reaktor und kühlersystem für exotherme reaktionen

Publications (3)

Publication Number Publication Date
DE60222630D1 true DE60222630D1 (de) 2007-11-08
DE60222630T2 DE60222630T2 (de) 2008-07-17
DE60222630T3 DE60222630T3 (de) 2015-02-19

Family

ID=34435896

Family Applications (1)

Application Number Title Priority Date Filing Date
DE60222630.9T Expired - Lifetime DE60222630T3 (de) 2001-02-08 2002-01-24 Reaktor und kühlersystem für exotherme reaktionen

Country Status (10)

Country Link
US (1) US7700791B2 (de)
AT (1) ATE374073T1 (de)
AU (1) AU2002241969B2 (de)
DE (1) DE60222630T3 (de)
DK (1) DK1358441T4 (de)
ES (1) ES2294111T5 (de)
MX (1) MX246250B (de)
PT (1) PT1358441E (de)
RU (1) RU2292946C2 (de)
SA (1) SA02220721B1 (de)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2547434B1 (de) * 2010-03-17 2020-01-08 Dow Technology Investments LLC Katalytischer festbettreaktor und verfahren zur herstellung von ethylenoxid durch teiloxidation von ethylen
SE535331C2 (sv) * 2010-06-01 2012-07-03 Skellefteaa Kraftaktiebolag Värmeväxlingssystem och metod för värmning av ett kollektormedium samt tork och bioenergikombinat innefattande värmeväxlingssystemet
CN107401674A (zh) * 2017-08-17 2017-11-28 武健 列管式汽化装置
TW202237260A (zh) * 2021-01-19 2022-10-01 美商科學設計有限公司 用於製造管間距減小的立式沸騰反應器的管與管板焊接

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB898374A (en) 1959-12-22 1962-06-06 Universal Oil Prod Co Method and apparatus for effecting reactions of flowing reactants
NL289830A (de) 1962-03-08
US3147084A (en) 1962-03-08 1964-09-01 Shell Oil Co Tubular catalytic reactor with cooler
GB1107319A (en) 1964-10-20 1968-03-27 Richard James Brooks Gas absorption process
IT986732B (it) 1973-04-30 1975-01-30 Snam Progetti Procedimento per condurre reazioni di ossidazione parzialecon ossi geno di composti organici in fase vapore ed apparecchiatura atta a realizzare detto procedimento
US4061659A (en) 1976-06-28 1977-12-06 Shell Oil Company Process for the production of ethylene oxide
US4101287A (en) 1977-01-21 1978-07-18 Exxon Research & Engineering Co. Combined heat exchanger reactor
EP0082609B1 (de) 1981-12-14 1987-01-14 Imperial Chemical Industries Plc Chemischer Reaktor und Verfahren
US5114685A (en) 1983-07-15 1992-05-19 Catalyst Technology, Inc. Catalyst recovery trough for unloading multi-tube reactors with maximum dust containment
JPH0629198B2 (ja) 1984-10-19 1994-04-20 武田薬品工業株式会社 化学的脱水反応方法
US4973777A (en) 1985-11-08 1990-11-27 Institut Francais Du Petrole Process for thermally converting methane into hydrocarbons with higher molecular weights, reactor for implementing the process and process for realizing the reactor
DE3768372D1 (de) * 1986-08-29 1991-04-11 Ici Plc Verfahren zur herstellung von aethylenoxid.
US4921681A (en) * 1987-07-17 1990-05-01 Scientific Design Company, Inc. Ethylene oxide reactor
JP2778878B2 (ja) * 1991-09-12 1998-07-23 株式会社日本触媒 エチレンオキシドの製造方法
US5525740A (en) 1993-03-01 1996-06-11 Scientific Design Company, Inc. Process for preparing silver catalyst and process of using same to produce ethylene oxide
US5504052A (en) 1994-12-02 1996-04-02 Scientific Design Company, Inc. Silver catalyst preparation
US5854167A (en) 1997-09-02 1998-12-29 Scientific Design Company, Inc. Ethylene oxide catalyst

Also Published As

Publication number Publication date
DK1358441T3 (da) 2008-02-04
AU2002241969B2 (en) 2006-06-15
SA02220721B1 (ar) 2008-05-21
ATE374073T1 (de) 2007-10-15
US7700791B2 (en) 2010-04-20
DE60222630T2 (de) 2008-07-17
RU2003124506A (ru) 2005-02-27
MXPA03007109A (es) 2003-12-04
US20080071100A1 (en) 2008-03-20
ES2294111T3 (es) 2008-04-01
DK1358441T4 (da) 2014-11-03
RU2292946C2 (ru) 2007-02-10
DE60222630T3 (de) 2015-02-19
ES2294111T5 (es) 2014-12-09
MX246250B (es) 2007-06-07
PT1358441E (pt) 2008-01-02

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Legal Events

Date Code Title Description
8363 Opposition against the patent
8328 Change in the person/name/address of the agent

Representative=s name: WESTENDORP SOMMER, 80336 MUENCHEN