JP2013518103A - 側方取り出し式の第2の反応器を備える酸化システム - Google Patents

側方取り出し式の第2の反応器を備える酸化システム Download PDF

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JP2013518103A
JP2013518103A JP2012551151A JP2012551151A JP2013518103A JP 2013518103 A JP2013518103 A JP 2013518103A JP 2012551151 A JP2012551151 A JP 2012551151A JP 2012551151 A JP2012551151 A JP 2012551151A JP 2013518103 A JP2013518103 A JP 2013518103A
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reaction zone
oxidant
slurry
range
inlet
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Japanese (ja)
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JP2013518103A5 (cg-RX-API-DMAC7.html
Inventor
シャイク アシュファク
ジョージ ワンダーズ アラン
ランジ デイビッド
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グルーポ ペトロテメックス,ソシエダ アノニマ デ カピタル バリアブレ
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Publication of JP2013518103A publication Critical patent/JP2013518103A/ja
Publication of JP2013518103A5 publication Critical patent/JP2013518103A5/ja
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    • 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
    • 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
    • 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
    • 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

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  • 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)
JP2012551151A 2010-01-29 2010-12-09 側方取り出し式の第2の反応器を備える酸化システム Pending JP2013518103A (ja)

Applications Claiming Priority (9)

Application Number Priority Date Filing Date Title
US29945010P 2010-01-29 2010-01-29
US29945310P 2010-01-29 2010-01-29
US29945510P 2010-01-29 2010-01-29
US61/299,453 2010-01-29
US61/299,455 2010-01-29
US61/299,450 2010-01-29
US12/957,730 US8936767B2 (en) 2010-01-29 2010-12-01 Oxidation system with sidedraw secondary reactor
US12/957,730 2010-12-01
PCT/US2010/059626 WO2011093948A1 (en) 2010-01-29 2010-12-09 Oxidation system with sidedraw secondary reactor

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2015223180A Division JP6538528B2 (ja) 2010-01-29 2015-11-13 側方取り出し式の第2の反応器を備える酸化システム

Publications (2)

Publication Number Publication Date
JP2013518103A true JP2013518103A (ja) 2013-05-20
JP2013518103A5 JP2013518103A5 (cg-RX-API-DMAC7.html) 2014-01-23

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JP2012551151A Pending JP2013518103A (ja) 2010-01-29 2010-12-09 側方取り出し式の第2の反応器を備える酸化システム
JP2015223180A Active JP6538528B2 (ja) 2010-01-29 2015-11-13 側方取り出し式の第2の反応器を備える酸化システム
JP2017147142A Active JP6542849B2 (ja) 2010-01-29 2017-07-28 側方取り出し式の第2の反応器を備える酸化システム

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JP2015223180A Active JP6538528B2 (ja) 2010-01-29 2015-11-13 側方取り出し式の第2の反応器を備える酸化システム
JP2017147142A Active JP6542849B2 (ja) 2010-01-29 2017-07-28 側方取り出し式の第2の反応器を備える酸化システム

Country Status (16)

Country Link
US (1) US8936767B2 (cg-RX-API-DMAC7.html)
EP (1) EP2528886B1 (cg-RX-API-DMAC7.html)
JP (3) JP2013518103A (cg-RX-API-DMAC7.html)
KR (2) KR102115688B1 (cg-RX-API-DMAC7.html)
CN (1) CN102811993B (cg-RX-API-DMAC7.html)
BR (1) BR112012018893B1 (cg-RX-API-DMAC7.html)
CA (1) CA2787930C (cg-RX-API-DMAC7.html)
ES (1) ES2640483T3 (cg-RX-API-DMAC7.html)
IN (1) IN2012DN06566A (cg-RX-API-DMAC7.html)
LT (1) LT2528886T (cg-RX-API-DMAC7.html)
MX (1) MX338623B (cg-RX-API-DMAC7.html)
MY (1) MY157558A (cg-RX-API-DMAC7.html)
PL (1) PL2528886T3 (cg-RX-API-DMAC7.html)
PT (1) PT2528886T (cg-RX-API-DMAC7.html)
RU (1) RU2579452C2 (cg-RX-API-DMAC7.html)
WO (1) WO2011093948A1 (cg-RX-API-DMAC7.html)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013518104A (ja) * 2010-01-29 2013-05-20 グルーポ ペトロテメックス,ソシエダ アノニマ デ カピタル バリアブレ 側流抜き出し二次反応器を有する酸化システム
US8968686B2 (en) 2010-01-29 2015-03-03 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
ES2399881T3 (es) 2000-12-07 2013-04-04 Grupo Petrotemex, S.A. De C.V. Procedimiento para la producción de poliésteres a bajo coste usando un reactor tubular
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
JP2008511645A (ja) * 2004-09-02 2008-04-17 イーストマン ケミカル カンパニー 最適化液相酸化
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

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013518104A (ja) * 2010-01-29 2013-05-20 グルーポ ペトロテメックス,ソシエダ アノニマ デ カピタル バリアブレ 側流抜き出し二次反応器を有する酸化システム
US8968686B2 (en) 2010-01-29 2015-03-03 Grupo Petrotemex, S.A. De C.V. Oxidation system with sidedraw secondary reactor
JP2016040312A (ja) * 2010-01-29 2016-03-24 グルーポ ペトロテメックス,ソシエダ アノニマ デ カピタル バリアブレ 側方取り出し式の第2の反応器を備える酸化システム

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Publication number Publication date
CN102811993B (zh) 2015-12-16
PL2528886T3 (pl) 2017-11-30
BR112012018893B1 (pt) 2018-09-25
JP2016026232A (ja) 2016-02-12
RU2012136135A (ru) 2014-02-27
RU2579452C2 (ru) 2016-04-10
MX338623B (es) 2016-04-25
US20110190536A1 (en) 2011-08-04
KR20130023196A (ko) 2013-03-07
LT2528886T (lt) 2017-09-25
MX2012008826A (es) 2012-09-07
JP6542849B2 (ja) 2019-07-10
KR102115688B1 (ko) 2020-05-26
BR112012018893A2 (pt) 2016-04-12
CA2787930A1 (en) 2011-08-04
MY157558A (en) 2016-06-30
JP2017190350A (ja) 2017-10-19
PT2528886T (pt) 2017-09-19
CN102811993A (zh) 2012-12-05
IN2012DN06566A (cg-RX-API-DMAC7.html) 2015-10-23
CA2787930C (en) 2017-10-17
EP2528886A1 (en) 2012-12-05
EP2528886B1 (en) 2017-09-06
WO2011093948A1 (en) 2011-08-04
US8936767B2 (en) 2015-01-20
KR20180067732A (ko) 2018-06-20
JP6538528B2 (ja) 2019-07-03
ES2640483T3 (es) 2017-11-03

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