ES8404528A1 - Sistema de control de temperatura en un reactor de oxidacion de olefina. - Google Patents

Sistema de control de temperatura en un reactor de oxidacion de olefina.

Info

Publication number
ES8404528A1
ES8404528A1 ES522344A ES522344A ES8404528A1 ES 8404528 A1 ES8404528 A1 ES 8404528A1 ES 522344 A ES522344 A ES 522344A ES 522344 A ES522344 A ES 522344A ES 8404528 A1 ES8404528 A1 ES 8404528A1
Authority
ES
Spain
Prior art keywords
flow rate
reactor
parameters
temperature control
calculate
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
Application number
ES522344A
Other languages
English (en)
Other versions
ES522344A0 (es
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.)
Babcock and Wilcox Co
Original Assignee
Babcock and Wilcox Co
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 Babcock and Wilcox Co filed Critical Babcock and Wilcox Co
Publication of ES8404528A1 publication Critical patent/ES8404528A1/es
Publication of ES522344A0 publication Critical patent/ES522344A0/es
Granted 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
    • 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
    • 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
    • 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
    • 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
    • B01J2208/00088—Flow rate 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
    • B01J2208/00097—Mathematical modelling
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00054—Controlling or regulating the heat exchange system
    • B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2219/00058—Temperature measurement
    • B01J2219/0006—Temperature measurement 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00054—Controlling or regulating the heat exchange system
    • B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2219/00069—Flow rate 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00085—Plates; Jackets; Cylinders
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Control Of Temperature (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

SISTEMA DE CONTROL DE TEMPERATURA PARA UN REACTOR DE OXIDACION DE OLEFINA, QUE REGULA EL CAUDAL DEL FLUJO DE REFRIGERANTE PARA MANTENER LA TEMPERATURA DEL REACTOR DENTRO DE UNA GAMA DE TEMPERATURAS DESEADA DURANTE EL FUNCIONAMIENTO DEL MISMO, ASI COMO DURANTE SU PUESTA EN MARCHA, SU PARO Y SUS CONDICIONES DE FUNCIONAMIENTO TRANSITORIO.CONSTA DE UN TRANSMISOR DE FLUJO DE ALIMENTACION CONECTADO AL CONDUCTO DE ALIMENTACION; DE UN TRANSMISOR DE FLUJO DE EFLUENTE CONECTADO AL CONDUCTO DE EFLUENTE; DE UN TRANSMISOR DE TEMPERATURA DE EFLUENTE CONECTADO AL CONDUCTO DEEFLUENTE; DE UN TRANSMISOR DE TEMPERATURA DEL REACTOR; DE UN TRANSMISOR DE CONCENTRACION; DE MEDIOS PARA EL CONTROL DEL FLUJO DEL REFRIGERANTE; Y DE MEDIOS DE CIRCUITO CONECTADOS A DICHOS TRANSMISORES.
ES522344A 1982-05-07 1983-04-29 Sistema de control de temperatura en un reactor de oxidacion de olefina. Granted ES522344A0 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US06/375,795 US4491924A (en) 1982-04-22 1982-05-07 Olefin oxidation reactor temperature control

Publications (2)

Publication Number Publication Date
ES8404528A1 true ES8404528A1 (es) 1984-04-16
ES522344A0 ES522344A0 (es) 1984-04-16

Family

ID=23482380

Family Applications (1)

Application Number Title Priority Date Filing Date
ES522344A Granted ES522344A0 (es) 1982-05-07 1983-04-29 Sistema de control de temperatura en un reactor de oxidacion de olefina.

Country Status (9)

Country Link
US (1) US4491924A (es)
EP (1) EP0094208B1 (es)
JP (1) JPS6033537B2 (es)
AU (1) AU559836B2 (es)
BR (1) BR8302460A (es)
CA (1) CA1187267A (es)
DE (1) DE3374841D1 (es)
ES (1) ES522344A0 (es)
IN (1) IN160808B (es)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4668473A (en) * 1983-04-25 1987-05-26 The Babcock & Wilcox Company Control system for ethylene polymerization reactor
JPS60248702A (ja) * 1984-05-24 1985-12-09 Mitsubishi Rayon Co Ltd 重合反応制御方法および装置
US4654801A (en) * 1984-11-30 1987-03-31 Phillips Petroleum Company Control of a vinyl acetate process
US4707245A (en) * 1985-12-20 1987-11-17 Lummus Crest, Inc. Temperature control for hydrogenation reactions
US4858155A (en) * 1985-12-24 1989-08-15 Beckman Instruments, Inc. Reaction temperature control system
US4742131A (en) * 1985-12-27 1988-05-03 Mitsui Toatsu Chemicals, Incorporated Method of controlling polymerization temperature
US4881185A (en) * 1986-04-01 1989-11-14 Chugai Ro. Co., Ltd. Method of measuring temperature and apparatus for effecting the method
US5000924A (en) * 1987-06-02 1991-03-19 Elsagainternational B.V. Autoacceleration control for exothermic reactors
IN168767B (es) * 1987-06-02 1991-06-01 Int Control Automation Finance
US4888704A (en) * 1987-12-18 1989-12-19 Amoco Corporation Advanced control strategies for melt flow rate and reactor concentration in the polypropylene slurry process
US4958826A (en) * 1988-08-08 1990-09-25 Microtek Lab., Inc. Paper feed system having a pressure plate that resiliently urges a plurality of elongated bearing, spring biased idler rollers against associated drive rollers for feeding a sheet of paper therebetween
NO178790C (no) * 1993-12-13 1996-06-05 Borealis Holding As Fremgangsmåte ved fremstilling av olefinpolymerer i en autoklavrektor
US6284196B1 (en) * 1999-04-01 2001-09-04 Bp Corporation North America Inc. Apparatus for monitor and control of an ammoxidation reactor with a fourier transform infrared spectrometer
US6991763B2 (en) * 2000-04-26 2006-01-31 Rohm And Haas Company Polymer process
AU2001255551A1 (en) * 2000-04-27 2001-11-07 Bp Corporation North America Inc. Method for control of a chemical manufacturing process
GB0121071D0 (en) * 2001-08-31 2001-10-24 Ashe Morris Ltd Multi-port flow control valves
EP1447128A1 (en) * 2003-02-17 2004-08-18 Methanol Casale S.A. Method for carrying out chemical reactions in pseudo-isothermal conditions
SG138525A1 (en) * 2006-06-13 2008-01-28 Sumitomo Chemical Co Method for measuring concentration of propylene polymer slurry, and process for producing propylene polymer
EP2059334A1 (de) * 2006-11-15 2009-05-20 Basf Se Verfahren zum betreiben einer exothermen heterogen katalysierten partiellen gasphasenoxidation einer organischen ausgangsverbindung zu einer organischen zielverbindung
CN105273747B (zh) * 2015-11-18 2017-05-03 北京中科诚毅科技发展有限公司 一种浆态床加氢反应器的控温措施及其设计方法和用途
CN112973580B (zh) * 2021-02-08 2022-01-21 湖北昌发容器制造有限公司 一种耐酸耐高温的无汞触媒催化氯乙烯转化器

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3271472A (en) * 1961-09-22 1966-09-06 Phillips Petroleum Co Method of controlling a thermal conversion process
US3471582A (en) * 1967-11-16 1969-10-07 Phillips Petroleum Co Control of exothermic reactions
US3967937A (en) * 1974-05-30 1976-07-06 Phillips Petroleum Company Absorption process method and apparatus
FR2318674A1 (fr) * 1975-07-23 1977-02-18 Dart Ind Inc Perfectionnements aux dispositifs et aux procedes utilisables pour assurer la maitrise de parametres operatoires au cours d'une polymerisation
FR2356197A1 (fr) * 1976-06-25 1978-01-20 Ici Ltd Procede et systeme de commande pour reactions chimiques exothermiques et endothermiques
US4132530A (en) * 1977-10-13 1979-01-02 Uop Inc. Temperature control in exothermic/endothermic reaction systems
US4236219A (en) * 1979-05-02 1980-11-25 Phillips Petroleum Company Temperature control of exothermic reactions
US4236218A (en) * 1979-05-02 1980-11-25 Phillips Petroleum Company Control of a cracking furnace
US4249907A (en) * 1979-08-23 1981-02-10 Phillips Petroleum Company Temperature control of exothermic reactions
US4249908A (en) * 1979-09-11 1981-02-10 Phillips Petroleum Company Temperature control of exothermic reactions
US4241230A (en) * 1979-11-19 1980-12-23 Mobil Oil Corporation Control system for the selective hydrogenation of acetylene present in ethylene product streams
US4329150A (en) * 1980-12-11 1982-05-11 Mobil Oil Corporation Method and apparatus for control and optimization of pyrolysis furnace with multiple parallel passes

Also Published As

Publication number Publication date
US4491924A (en) 1985-01-01
EP0094208A3 (en) 1985-07-10
JPS5925382A (ja) 1984-02-09
EP0094208A2 (en) 1983-11-16
ES522344A0 (es) 1984-04-16
DE3374841D1 (en) 1988-01-21
AU1430583A (en) 1984-11-08
IN160808B (es) 1987-08-08
CA1187267A (en) 1985-05-21
BR8302460A (pt) 1984-01-17
AU559836B2 (en) 1987-03-19
JPS6033537B2 (ja) 1985-08-03
EP0094208B1 (en) 1987-12-09

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Legal Events

Date Code Title Description
MM4A Patent lapsed

Effective date: 19960506