MX338623B - Sistema de oxidacion con reactor secundario equipado con descarga lateral. - Google Patents

Sistema de oxidacion con reactor secundario equipado con descarga lateral.

Info

Publication number
MX338623B
MX338623B MX2012008826A MX2012008826A MX338623B MX 338623 B MX338623 B MX 338623B MX 2012008826 A MX2012008826 A MX 2012008826A MX 2012008826 A MX2012008826 A MX 2012008826A MX 338623 B MX338623 B MX 338623B
Authority
MX
Mexico
Prior art keywords
oxidation system
post
secondary reactor
oxidation reactor
sidedraw
Prior art date
Application number
MX2012008826A
Other languages
English (en)
Spanish (es)
Other versions
MX2012008826A (es
Inventor
David Lange
Alan George Wonders
Ashfaq Shaikh
Original Assignee
Grupo Petrotemex Sa De Cv
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 Grupo Petrotemex Sa De Cv filed Critical Grupo Petrotemex Sa De Cv
Publication of MX2012008826A publication Critical patent/MX2012008826A/es
Publication of MX338623B publication Critical patent/MX338623B/es

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/228Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
    • C07C51/21Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
    • C07C51/255Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
    • C07C51/265Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting having alkyl side chains which are oxidised to carboxyl groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00265Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00265Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00292Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
    • B01J2208/003Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids involving reactant slurries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
MX2012008826A 2010-01-29 2010-12-09 Sistema de oxidacion con reactor secundario equipado con descarga lateral. MX338623B (es)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US29945310P 2010-01-29 2010-01-29
US29945010P 2010-01-29 2010-01-29
US29945510P 2010-01-29 2010-01-29
US12/957,730 US8936767B2 (en) 2010-01-29 2010-12-01 Oxidation system with sidedraw secondary reactor
PCT/US2010/059626 WO2011093948A1 (en) 2010-01-29 2010-12-09 Oxidation system with sidedraw secondary reactor

Publications (2)

Publication Number Publication Date
MX2012008826A MX2012008826A (es) 2012-09-07
MX338623B true MX338623B (es) 2016-04-25

Family

ID=44319660

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2012008826A MX338623B (es) 2010-01-29 2010-12-09 Sistema de oxidacion con reactor secundario equipado con descarga lateral.

Country Status (16)

Country Link
US (1) US8936767B2 (enExample)
EP (1) EP2528886B1 (enExample)
JP (3) JP2013518103A (enExample)
KR (2) KR102115688B1 (enExample)
CN (1) CN102811993B (enExample)
BR (1) BR112012018893B1 (enExample)
CA (1) CA2787930C (enExample)
ES (1) ES2640483T3 (enExample)
IN (1) IN2012DN06566A (enExample)
LT (1) LT2528886T (enExample)
MX (1) MX338623B (enExample)
MY (1) MY157558A (enExample)
PL (1) PL2528886T3 (enExample)
PT (1) PT2528886T (enExample)
RU (1) RU2579452C2 (enExample)
WO (1) WO2011093948A1 (enExample)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8968686B2 (en) * 2010-01-29 2015-03-03 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor
US8790601B2 (en) * 2010-01-29 2014-07-29 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5278846A (en) * 1975-12-25 1977-07-02 Matsuyama Sekyu Kagaku Kk Continuous production of high purity telephthalic acid
US5356600A (en) * 1990-09-24 1994-10-18 Praxair Technology, Inc. Oxygen enrichment method and system
SI9500109A (en) * 1995-04-05 1996-10-31 Levec Janez Dipl Ing Prof Dr Apparatus and Process for Thermal Oxidative Treatment of Waste Waters
JPH09278709A (ja) * 1996-02-13 1997-10-28 Mitsubishi Chem Corp 芳香族カルボン酸の製造方法
ID19133A (id) * 1996-12-12 1998-06-18 Praxair Technology Inc Pengisian oksigen langsung kedalam reaktor-reaktor ruang gelembung
US7060853B2 (en) 2000-01-12 2006-06-13 Invista North America S.A R.L. Method for increasing oxidation reactor production capacity
EP1453883B1 (en) 2000-12-07 2012-11-21 Grupo Petrotemex, S.A. de C.V. Low cost polyester process using a pipe reactor
US7196215B2 (en) * 2001-06-04 2007-03-27 Eastman Chemical Company Process for the production of purified terephthalic acid
DE10240816A1 (de) * 2002-08-30 2004-03-11 Basf Ag Oxidationsverfahren
US7132566B2 (en) 2003-09-22 2006-11-07 Eastman Chemical Company Process for the purification of a crude carboxylic acid slurry
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
KR20070048251A (ko) * 2004-09-02 2007-05-08 이스트만 케미칼 컴파니 최적화된 액상 산화 방법
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US20070208194A1 (en) 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US8790601B2 (en) 2010-01-29 2014-07-29 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor
US8968686B2 (en) 2010-01-29 2015-03-03 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor

Also Published As

Publication number Publication date
ES2640483T3 (es) 2017-11-03
CA2787930C (en) 2017-10-17
EP2528886A1 (en) 2012-12-05
EP2528886B1 (en) 2017-09-06
JP6538528B2 (ja) 2019-07-03
BR112012018893B1 (pt) 2018-09-25
MX2012008826A (es) 2012-09-07
CN102811993A (zh) 2012-12-05
BR112012018893A2 (pt) 2016-04-12
IN2012DN06566A (enExample) 2015-10-23
PT2528886T (pt) 2017-09-19
CN102811993B (zh) 2015-12-16
PL2528886T3 (pl) 2017-11-30
WO2011093948A1 (en) 2011-08-04
JP2016026232A (ja) 2016-02-12
RU2012136135A (ru) 2014-02-27
RU2579452C2 (ru) 2016-04-10
KR102115688B1 (ko) 2020-05-26
MY157558A (en) 2016-06-30
JP6542849B2 (ja) 2019-07-10
CA2787930A1 (en) 2011-08-04
US8936767B2 (en) 2015-01-20
JP2013518103A (ja) 2013-05-20
KR20130023196A (ko) 2013-03-07
US20110190536A1 (en) 2011-08-04
LT2528886T (lt) 2017-09-25
JP2017190350A (ja) 2017-10-19
KR20180067732A (ko) 2018-06-20

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