CO4410352A1 - Bandejas de reactor para un reactor de policondensacion escalonado verticalmente - Google Patents

Bandejas de reactor para un reactor de policondensacion escalonado verticalmente

Info

Publication number
CO4410352A1
CO4410352A1 CO95018055A CO95018055A CO4410352A1 CO 4410352 A1 CO4410352 A1 CO 4410352A1 CO 95018055 A CO95018055 A CO 95018055A CO 95018055 A CO95018055 A CO 95018055A CO 4410352 A1 CO4410352 A1 CO 4410352A1
Authority
CO
Colombia
Prior art keywords
tray
liquid polymer
reactor
flow
trays
Prior art date
Application number
CO95018055A
Other languages
English (en)
Inventor
Thomas Lloyd Yount
James Wesley Adams
Larry Cates Windes
Original Assignee
Eastman Chem 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 Eastman Chem Co filed Critical Eastman Chem Co
Publication of CO4410352A1 publication Critical patent/CO4410352A1/es

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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/006—Baffles
    • 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
    • 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
    • B01J2219/00132—Controlling the temperature using electric heating or cooling elements
    • B01J2219/00135—Electric resistance heaters
    • 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
    • B01J2219/00164—Controlling or regulating processes controlling the flow
    • B01J2219/00166—Controlling or regulating processes controlling the flow controlling the residence time inside the reactor vessel
    • 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
    • B01J2219/00168—Controlling or regulating processes controlling the viscosity
    • 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)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Polymerisation Methods In General (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Polyoxymethylene Polymers And Polymers With Carbon-To-Carbon Bonds (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)

Abstract

ESTA INVENCION SE RELACIONA CON UN REACTOR DE PO- LIMERIZACION EN DISPOSICION VERTICAL QUE PRESENTA UNA SERIE DE CONJUNTOS DE BANDEJAS ESENCIALMENTE CIRCULARES; CADA CONJUNTO DE BANDEJA PRESENTANDO UNA CHIMENEA DE VAPOR CENTRAL ABIERTA Y UN SOLO PASAJE DE FLUJO COMPUESTO DE POR LO MENOS DOS CIRCUITOS EN LOS CUALES EL FLUJO DEL POLIMERO LI- QUIDO SE INVIERTE MEDIANTE UNA PARED DE GIRO SUS- TANCIALMENTE SEMICIRCULAR; DICHAS BANDEJAS PRESEN- TANDO UNA ENTRADA DE BANDEJA Y UNA SALIDA DE BANDEJA PARA POLIMERO LIQUIDO, PARA DIRIGIR UN FLUJO DEL POLIMERO LIQUIDO MEDIANTE UN GRADIENTE HIDRAULICO; CADA CONJUNTO DE BANDEJA ESTANDO ABIERTO EN LA PARTE SUPERIOR PARA DEJAR ESCAPAR EL VAPOR DEL FLUJO DE POLIMERO LIQUIDO A LA CHIMENEA DE VAPOR CENTRAL ABIERTA; Y DICHAS BANDEJAS ESTAN- DO ORDENADAS EN DISPOSICION VERTICAL, UNA SOBRE LA OTRA. FIGURA 1
CO95018055A 1994-05-02 1995-05-02 Bandejas de reactor para un reactor de policondensacion escalonado verticalmente CO4410352A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/238,077 US5464590A (en) 1994-05-02 1994-05-02 Reactor trays for a vertical staged polycondensation reactor

Publications (1)

Publication Number Publication Date
CO4410352A1 true CO4410352A1 (es) 1997-01-09

Family

ID=22896399

Family Applications (1)

Application Number Title Priority Date Filing Date
CO95018055A CO4410352A1 (es) 1994-05-02 1995-05-02 Bandejas de reactor para un reactor de policondensacion escalonado verticalmente

Country Status (24)

Country Link
US (1) US5464590A (es)
EP (1) EP0758265B1 (es)
JP (1) JPH09512583A (es)
CN (1) CN1146734A (es)
AT (1) ATE167640T1 (es)
AU (1) AU681030B2 (es)
BR (1) BR9507583A (es)
CA (1) CA2188792C (es)
CO (1) CO4410352A1 (es)
CZ (1) CZ319596A3 (es)
DE (1) DE69503125T2 (es)
ES (1) ES2117866T3 (es)
FI (1) FI964408A (es)
HU (1) HUT76716A (es)
IL (1) IL113554A0 (es)
MY (1) MY130511A (es)
NO (1) NO964606L (es)
NZ (1) NZ284706A (es)
PL (1) PL317104A1 (es)
RU (1) RU2140816C1 (es)
SK (1) SK133596A3 (es)
TW (1) TW327610B (es)
WO (1) WO1995029753A1 (es)
ZA (1) ZA953507B (es)

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002020474A (ja) * 2000-07-13 2002-01-23 Daicel Chem Ind Ltd ポリエステルの製造装置
EP1325323A2 (en) * 2000-10-13 2003-07-09 Avantium International B.V. Method and apparatus for screening of polycondensation catalysts
US6906164B2 (en) * 2000-12-07 2005-06-14 Eastman Chemical Company Polyester process using a pipe reactor
US6429278B1 (en) 2001-01-22 2002-08-06 Eastman Chemical Company Process for manufacture of polyesters based on 1,4-cyclohexanedimethanol and isophthalic acid
DE10246251A1 (de) * 2002-10-02 2004-04-15 Zimmer Ag Verfahren und Vorrichtung zur kontinuierlichen Herstellung von Polyestern
US6914120B2 (en) * 2002-11-13 2005-07-05 Eastman Chemical Company Method for making isosorbide containing polyesters
DE102004038466B4 (de) * 2004-08-07 2014-08-28 Lurgi Zimmer Gmbh Verfahren und Vorrichtung zur kontinuierlichen Vorpolykondensation von Ver-/Umesterungsprodukten
US20060251547A1 (en) * 2005-05-05 2006-11-09 Windes Larry C Family of stationary film generators and film support structures for vertical staged polymerization reactors
US7435393B2 (en) * 2005-05-05 2008-10-14 Eastman Chemical Company Baffle assembly module for vertical staged polymerization reactors
US7718137B2 (en) * 2005-10-28 2010-05-18 Eastman Chemical Company Reactor with optimized internal tray design
US7628927B2 (en) * 2005-12-14 2009-12-08 Vesitech, Inc. Reactor for removing chemical and biological contaminants from a contaminated fluid
EP1820814B1 (de) * 2006-01-24 2007-08-29 Lurgi Zimmer GmbH Verfahren zur Veresterung von Terephthalsäure mit Butandiol, Verfahren zur Herstellung von Polybutylenterephthalat und Vorrichtung dafür
US7649109B2 (en) 2006-12-07 2010-01-19 Eastman Chemical Company Polyester production system employing recirculation of hot alcohol to esterification zone
US7943094B2 (en) 2006-12-07 2011-05-17 Grupo Petrotemex, S.A. De C.V. Polyester production system employing horizontally elongated esterification vessel
US7863477B2 (en) 2007-03-08 2011-01-04 Eastman Chemical Company Polyester production system employing hot paste to esterification zone
US7868130B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Multi-level tubular reactor with vertically spaced segments
US7872089B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Multi-level tubular reactor with internal tray
US7872090B2 (en) 2007-07-12 2011-01-18 Eastman Chemical Company Reactor system with optimized heating and phase separation
US7858730B2 (en) 2007-07-12 2010-12-28 Eastman Chemical Company Multi-level tubular reactor with dual headers
US7829653B2 (en) * 2007-07-12 2010-11-09 Eastman Chemical Company Horizontal trayed reactor
US7842777B2 (en) 2007-07-12 2010-11-30 Eastman Chemical Company Sloped tubular reactor with divided flow
US7868129B2 (en) 2007-07-12 2011-01-11 Eastman Chemical Company Sloped tubular reactor with spaced sequential trays
US7847053B2 (en) 2007-07-12 2010-12-07 Eastman Chemical Company Multi-level tubular reactor with oppositely extending segments
WO2009012391A1 (en) * 2007-07-17 2009-01-22 Sabic Innovative Plastics Ip B.V. Aliphatic polycarbonates for use in thermosetting powder coatings
US9517584B2 (en) 2013-12-18 2016-12-13 Eastman Chemical Company Articles comprising isosorbide and processes for their manufacture
DE102017106177A1 (de) * 2017-03-22 2018-09-27 Thyssenkrupp Ag Boden für eine Stoffaustauschkolonne

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US1084554A (en) * 1906-06-14 1914-01-13 William Brayton Mann Triple valve for air-brakes.
FR990870A (fr) * 1948-10-29 1951-09-27 Nouvelle Soc Induschimie D Etu Appareil pour le traitement de fluides gazeux
US3017950A (en) * 1960-12-30 1962-01-23 Henry F Koshoot Bubble-plate structure for rectification columns
US3359074A (en) * 1963-06-11 1967-12-19 Monsanto Co Polycondensation apparatus
US3509203A (en) * 1966-12-16 1970-04-28 Engels Chemiefaserwerk Veb Transesterification of dicarboxylic alkyl esters with glycols
US3658484A (en) * 1969-10-24 1972-04-25 Arthur W Bright Countercurrent contact apparatus
DE1957458B2 (de) * 1969-11-15 1973-04-19 Chemische Werke Hüls AG, 4370 Mari Vorrichtung zur kontinuierlichen durchfuehrung chemischer umsetzungen in fluessiger phase
CH521302A (de) * 1970-03-05 1972-04-15 Inventa Ag Verfahren zum kontinuierlichen Umestern von Dicarbonsäurealkylestern mit Diolen
US3841836A (en) * 1972-08-10 1974-10-15 Eastman Kodak Co Apparatus for the production of condensation polymers
US4019866A (en) * 1973-03-05 1977-04-26 Du Pont Of Canada Limited Recirculating reaction apparatus for continuous preparation of a polyamide
SE7813257L (sv) * 1978-01-04 1979-07-05 Markfort Dieter Sett och anordning for rektifikation
US4196168A (en) * 1978-05-05 1980-04-01 Eastman Kodak Company Sloped tray arrangement for polymerization reactor
GB2053721B (en) * 1979-07-09 1983-03-09 Krasnodar Politekhn I Gas-liquid contact tray
US4615770A (en) * 1983-10-14 1986-10-07 Rakesh Govind Distillation column and process
US5013407A (en) * 1988-03-08 1991-05-07 Institut Francais Du Petrole Apparatus for reactive distillation
US5091060A (en) * 1990-09-10 1992-02-25 Phillips Petroleum Company Fractional distillation column and method for its use
US5230839A (en) * 1991-08-15 1993-07-27 Atlantic Richfield Company Fractionator feed section

Also Published As

Publication number Publication date
WO1995029753A1 (en) 1995-11-09
ATE167640T1 (de) 1998-07-15
FI964408A0 (fi) 1996-11-01
CZ319596A3 (en) 1997-09-17
DE69503125D1 (de) 1998-07-30
ES2117866T3 (es) 1998-08-16
US5464590A (en) 1995-11-07
CA2188792C (en) 2000-03-21
MX9605262A (es) 1997-10-31
CA2188792A1 (en) 1995-11-09
MY130511A (en) 2007-06-29
NO964606D0 (no) 1996-10-31
PL317104A1 (en) 1997-03-17
EP0758265B1 (en) 1998-06-24
TW327610B (en) 1998-03-01
CN1146734A (zh) 1997-04-02
AU681030B2 (en) 1997-08-14
DE69503125T2 (de) 1998-10-22
RU2140816C1 (ru) 1999-11-10
HUT76716A (en) 1997-10-28
AU2392195A (en) 1995-11-29
FI964408A (fi) 1996-11-04
NO964606L (no) 1996-10-31
SK133596A3 (en) 1997-09-10
JPH09512583A (ja) 1997-12-16
EP0758265A1 (en) 1997-02-19
BR9507583A (pt) 1997-09-09
HU9603134D0 (en) 1997-01-28
ZA953507B (en) 1996-01-15
IL113554A0 (en) 1995-08-31
NZ284706A (en) 1997-01-29

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