HUP0100656A2 - Eljárás aromás karbonsavak előállítására - Google Patents

Eljárás aromás karbonsavak előállítására

Info

Publication number
HUP0100656A2
HUP0100656A2 HU0100656A HUP0100656A HUP0100656A2 HU P0100656 A2 HUP0100656 A2 HU P0100656A2 HU 0100656 A HU0100656 A HU 0100656A HU P0100656 A HUP0100656 A HU P0100656A HU P0100656 A2 HUP0100656 A2 HU P0100656A2
Authority
HU
Hungary
Prior art keywords
substituted aromatic
reactor
organic acid
diacid
stirred tank
Prior art date
Application number
HU0100656A
Other languages
English (en)
Inventor
Charles Lee Edwards
Raymond Lawrence June
Michael Wayne Potter
Edward James Simpson
Original Assignee
Shell Internationale Research Maatschappij B.V.
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 Shell Internationale Research Maatschappij B.V. filed Critical Shell Internationale Research Maatschappij B.V.
Publication of HUP0100656A2 publication Critical patent/HUP0100656A2/hu
Publication of HUP0100656A3 publication Critical patent/HUP0100656A3/hu

Links

Classifications

    • 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
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling of unreacted starting or intermediate materials

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

A találmány tárgya eljárás 97%-os tisztaságú, disav-szubsztituáltaromás előállítására, amely eljárás során: betáplálási áramotbiztosítanak, amely dialkil-szubsztituált aromást és szerves savoldószert tartalmaz; a betáplálási áramot egy gőzárammalérintkeztetik, a gőzáram legalább 50 térfogat% oxigént tartalmaz, ésaz oxigén parciális nyomása legalább 0,07 bar, 80-130 °Chőmérsékleten, egy katalizátorrendszer jelenlétében, amely cirkóniumotés kobaltot tartalmaz, ahol a kobaltnak a cirkóniumhoz viszonyítottmólaránya (5:1 ) - (15:1) és az érintkeztetést kevert üstreaktorbanvégzik; a kevert üstreaktorból egy gőzáramot távolítanak el, amelyszerves savat és vizet tartalmaz; a szerves sav és a víz legalább egyrészét kondenzáltatják a gőzáramból; a gőzáramból elválasztott szervessavból a víz legalább egy részét elválasztják; a kondenzált szervessav legalább egy részét visszavezetik a kevert üstreaktorba; a kevertüstreaktorból folyamatosan eltávolítják a reaktorterméket, amelydisav-szubsztituált aromást tartalmaz; a reaktortermékből elválasztjáka disav-szubsztituált aromás szilárd kristályait; és a disav-szubsztituált aromás szilárd kristályaiból kinyerik a legalább 97tömeg%-os tisztaságú disav-szubsztituált aromást. A nagy tisztaságútermék mellett a találmány szerinti eljárás további előnye, hogykivitelezése egyszerű rozsdamentes acél reaktorban történhet, és arefluxáltatásos hűtés következtében a reaktor eltömődése nemkövetkezik be. Ó
HU0100656A 1997-12-15 1998-12-14 Method for produce aromatic carboxylic acids HUP0100656A3 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US6944197P 1997-12-15 1997-12-15
PCT/EP1998/008134 WO1999031038A1 (en) 1997-12-15 1998-12-14 Method to produce aromatic carboxylic acids

Publications (2)

Publication Number Publication Date
HUP0100656A2 true HUP0100656A2 (hu) 2001-06-28
HUP0100656A3 HUP0100656A3 (en) 2002-03-28

Family

ID=22089001

Family Applications (1)

Application Number Title Priority Date Filing Date
HU0100656A HUP0100656A3 (en) 1997-12-15 1998-12-14 Method for produce aromatic carboxylic acids

Country Status (10)

Country Link
EP (1) EP1045824A1 (hu)
JP (1) JP2002508343A (hu)
KR (1) KR20010033086A (hu)
CN (1) CN1282314A (hu)
AU (1) AU732522B2 (hu)
BR (1) BR9813606A (hu)
CA (1) CA2315151A1 (hu)
HU (1) HUP0100656A3 (hu)
TR (1) TR200001718T2 (hu)
WO (1) WO1999031038A1 (hu)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6949673B2 (en) 2000-01-12 2005-09-27 E.I. Du Pont De Nemours And Company Process for producing carboxylic acids
US7060853B2 (en) 2000-01-12 2006-06-13 Invista North America S.A R.L. Method for increasing oxidation reactor production capacity
US7485747B2 (en) 2001-06-04 2009-02-03 Eastman Chemical Company Two stage oxidation process for the production of aromatic dicarboxylic acids
US7276625B2 (en) 2002-10-15 2007-10-02 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
US7074954B2 (en) 2002-12-09 2006-07-11 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
US7132566B2 (en) 2003-09-22 2006-11-07 Eastman Chemical Company Process for the purification of a crude carboxylic acid slurry
US7161027B2 (en) 2002-12-09 2007-01-09 Eastman Chemical Company Process for the oxidative purification of terephthalic acid
US20040215036A1 (en) 2003-04-25 2004-10-28 Robert Lin Method for heating a crude carboxylic acid slurry in a post oxidation zone by the addition of steam
CN101111312B (zh) * 2004-12-20 2012-01-18 工艺设计中心有限公司 用于制备芳族羧酸的方法
KR100744754B1 (ko) * 2005-12-13 2007-08-01 삼성석유화학(주) 방향족 카르복실산의 제조방법
US7816556B2 (en) 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US7772424B2 (en) 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7326807B2 (en) 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system with enhanced heating for oxidative digestion
US20070208194A1 (en) 2006-03-01 2007-09-06 Woodruff Thomas E Oxidation system with sidedraw secondary reactor
US7326808B2 (en) 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system
US7393973B2 (en) 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
US7420082B2 (en) 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US8455680B2 (en) 2008-01-15 2013-06-04 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
US8614350B2 (en) 2008-01-15 2013-12-24 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
RU2496764C2 (ru) * 2008-03-18 2013-10-27 ДжиТиСи ТЕКНОЛОДЖИ, ЭлПи Способ (варианты) и системы получения изофталевой и терефталевой кислот
GB0807904D0 (en) * 2008-04-30 2008-06-04 Invista Technologies Srl Oxidation reactions
US8658820B2 (en) * 2008-05-23 2014-02-25 Gtc Technology Us, Llc Catalyst systems for the production of acids
US20100113735A1 (en) * 2008-10-31 2010-05-06 Eastman Chemical Company Integrated Co-Production of Dicarboxylic Acids
CN110452392B (zh) * 2019-08-30 2021-11-02 湘潭大学 一种钴基金属有机骨架材料的制备方法及其在对二甲苯氧化反应中的应用

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3562318A (en) * 1966-11-10 1971-02-09 Petro Tex Chem Corp Catalytic oxidation process of mono-aryl compounds
GB1373230A (en) * 1971-12-23 1974-11-06 Mitsui Petrochemical Ind Process for producing terephthalic acid
GB9104776D0 (en) * 1991-03-07 1991-04-17 Ici Plc Process for the production of terephthalic acid

Also Published As

Publication number Publication date
KR20010033086A (ko) 2001-04-25
WO1999031038A1 (en) 1999-06-24
HUP0100656A3 (en) 2002-03-28
BR9813606A (pt) 2000-10-10
AU2161099A (en) 1999-07-05
JP2002508343A (ja) 2002-03-19
TR200001718T2 (tr) 2001-01-22
CN1282314A (zh) 2001-01-31
EP1045824A1 (en) 2000-10-25
CA2315151A1 (en) 1999-06-24
AU732522B2 (en) 2001-04-26

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