WO2000031014A1 - Process of purifying and producing high purity aromatic polycarboxylic acids and derivatives thereof - Google Patents

Process of purifying and producing high purity aromatic polycarboxylic acids and derivatives thereof Download PDF

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Publication number
WO2000031014A1
WO2000031014A1 PCT/US1999/027604 US9927604W WO0031014A1 WO 2000031014 A1 WO2000031014 A1 WO 2000031014A1 US 9927604 W US9927604 W US 9927604W WO 0031014 A1 WO0031014 A1 WO 0031014A1
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WO
WIPO (PCT)
Prior art keywords
salt
acid
base compound
derivative
base
Prior art date
Application number
PCT/US1999/027604
Other languages
English (en)
French (fr)
Other versions
WO2000031014A8 (en
Inventor
T. D. Vincent Lin
Original Assignee
Lin T D Vincent
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
Priority claimed from US09/286,262 external-priority patent/US6392091B2/en
Priority claimed from US09/347,486 external-priority patent/US6291707B1/en
Application filed by Lin T D Vincent filed Critical Lin T D Vincent
Priority to JP2000583843A priority Critical patent/JP2003510247A/ja
Priority to EP99967120A priority patent/EP1131276A4/en
Priority to KR1020017006507A priority patent/KR100642625B1/ko
Publication of WO2000031014A1 publication Critical patent/WO2000031014A1/en
Publication of WO2000031014A8 publication Critical patent/WO2000031014A8/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/48Separation; Purification; Stabilisation; Use of additives

Definitions

  • the method uses base-extraction solvents to extract base compound and impurities from the salt and recovered product.
  • the residual base compound in the recovered product is removed by leaching, stripping, thermal agitating with electromagnetic waves, or evaporation with thermal decomposition.
  • the residual base compound is not an impurity but a contaminant introduced by the purification process.
  • the method allows eliminating crystallizers for crystallization and equipment for drying and pneumatically carrying to reduce costs.
  • the purification method is combined with the oxidation and solvent recovery in prior art to use only one set of process steps, instead of two, to produce aromatic polycarboxylic acids.
  • an acid-substitution solvent is added to substitute and precipitate the product acid.
  • the salt may be mixed with a base-extraction solvent. It is preferred to completely dissolve ether basic salts and common salts before adding an acid- substitution solvent, and the preferred solvent is water, methanol, ethanol, alkylene glycol, or a mixture of these. Carbonyl basic salts are insoluble in most solvents, and water is a preferred acid-substitution solvent. Water is preferably added in the presence of the base- extraction solvent, such as methanol, ethanol, acetone, tetrahydrofuran, or tetrahydropyran. Acid substitution may be conducted under electromagnetic waves. Acid substitution with a base-extraction solvent reduces the inclusion of base compound and impurities in the recovered product.
  • water or a base-extraction solvent can be an acid- substitution solvent for carbonyl basic salts.
  • An acid-substitution solvent can be a mixture of these acids in any proportion, or a mixture of these acids with a dissolving solvent or a base-extraction solvent in a proportion that the acid is greater than 1 % by weight.
  • the preferred acid-substitution solvent is aliphatic carboxylic acid, and the most preferable is acetic acid.
  • water is preferred.
  • the amount of acid-substitution solvent added is 0.5-100 mole per mole of carboxylic functional group in the aromatic polycarboxylic acid. It is usually added in an amount of slightly more than the mole parts of the carboxylic functional group.
  • the invention tries to reduce the residual base compound by removing excessive base compound from the salt and extracting the residual compound from the recovered product.
  • these efforts can reduce but cannot totally remove the residual base compound from the recovered product.
  • Some of the previous steps for removing base compound may be eliminated by having higher residual base compound in the recovered product. Since removing the residual base compound is a difficult process. Therefore, it is preferred to minimize the residual base compound in the recovered product.
  • This step produces aromatic polycarboxylic acids through the oxidation of the corresponding alkyl group with molecular oxygen.
  • the oxidation of aromatic polycarboxylic acid has been extensively studied in the last 50 years, the invention may use any previously known prior art and is not limited to any specific one.
  • a sample of 150 grams of CTA as described in Table 1 was dissolved at room temperature into a solution with composition close to flashed reactor effluent compositions.
  • the solution contained 202 grams of mo ⁇ holine, 191 grams of water, 29 grams of 48% hydrobromic acid, 0.23 grams of cobalt acetate tetrahydrate, 0.3 grams of magnesium acetic tetrahydrate, and 60 grams of acetic acid.
  • the temperature of this solution was raised to 110 C to dissolve the CTA and evaporate 79 c.c. of condensate.
  • the solution was then cooled to room temperature for precipitation, and the filter cake was subsequently washed and leached by methanol to obtain 278 grams of wet cake.

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)
PCT/US1999/027604 1998-11-24 1999-11-19 Process of purifying and producing high purity aromatic polycarboxylic acids and derivatives thereof WO2000031014A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2000583843A JP2003510247A (ja) 1998-11-24 1999-11-19 高純度芳香族ポリカルボン酸及びその誘導体の精製及び製造過程
EP99967120A EP1131276A4 (en) 1998-11-24 1999-11-19 METHOD FOR PURIFYING AND PRODUCING HIGH-PURITY AROMATIC POLYCARBOXYLIC ACIDS AND DERIVATIVES THEREOF
KR1020017006507A KR100642625B1 (ko) 1998-11-24 1999-11-19 고순도 방향족 폴리카르복실산 및 이것의 유도체를 정제및 생성하는 방법

Applications Claiming Priority (8)

Application Number Priority Date Filing Date Title
US10964898P 1998-11-24 1998-11-24
US60/109,648 1998-11-24
US26749999A 1999-03-12 1999-03-12
US09/267,499 1999-03-12
US09/286,262 US6392091B2 (en) 1998-11-24 1999-04-05 Process of purifying and producing high purity aromatic polycarboxylic acids
US09/286,262 1999-04-15
US09/347,486 1999-07-02
US09/347,486 US6291707B1 (en) 1999-03-12 1999-07-02 Process of purifying and producing high purity aromatic polycarboxylic acids and derivatives thereof

Publications (2)

Publication Number Publication Date
WO2000031014A1 true WO2000031014A1 (en) 2000-06-02
WO2000031014A8 WO2000031014A8 (en) 2000-08-17

Family

ID=27493707

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1999/027604 WO2000031014A1 (en) 1998-11-24 1999-11-19 Process of purifying and producing high purity aromatic polycarboxylic acids and derivatives thereof

Country Status (5)

Country Link
EP (1) EP1131276A4 (ja)
JP (1) JP2003510247A (ja)
KR (1) KR100642625B1 (ja)
CN (1) CN1264798C (ja)
WO (1) WO2000031014A1 (ja)

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1484305A1 (en) * 2003-06-05 2004-12-08 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
EP1484306A1 (en) * 2003-06-05 2004-12-08 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
EP1484307A1 (en) * 2003-06-05 2004-12-08 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
WO2006028815A3 (en) * 2004-09-02 2006-04-27 Eastman Chem Co Optimized liquid-phase oxidation
US7273559B2 (en) 2004-10-28 2007-09-25 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7282151B2 (en) 2003-06-05 2007-10-16 Eastman Chemical Company Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration
US7291270B2 (en) 2004-10-28 2007-11-06 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7402694B2 (en) 2005-08-11 2008-07-22 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7452522B2 (en) 2003-06-05 2008-11-18 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
US7494641B2 (en) 2003-06-05 2009-02-24 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
US7556784B2 (en) 2004-09-02 2009-07-07 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7569722B2 (en) 2005-08-11 2009-08-04 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7759516B2 (en) 2006-03-01 2010-07-20 Eastman Chemical Company Versatile oxidation byproduct purge process
US7863481B2 (en) 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
US7880032B2 (en) 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7888530B2 (en) 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7897810B2 (en) 2004-09-02 2011-03-01 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7897808B2 (en) 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
EP1784378B1 (en) * 2004-09-02 2014-09-24 Grupo Petrotemex, S.A. De C.V. PRODUCTION PROCESS OF crude terephthalic acid
WO2015186073A1 (en) * 2014-06-04 2015-12-10 Reliance Industries Limited Process for the purification of crude carboxylic acid

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101144887B1 (ko) 2009-12-16 2012-05-14 호남석유화학 주식회사 이소프탈산의 정제 방법

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5565609A (en) * 1993-02-12 1996-10-15 Mitsui Petrochemical Industries, Ltd. Method of purifying aromatic dicarboxylic acids
WO1998012157A2 (en) * 1996-09-17 1998-03-26 Tsong-Dar Vincent Lin Process for purification of aromatic polycarboxylic acids
US5840968A (en) * 1995-06-07 1998-11-24 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1011411B (de) * 1953-07-20 1957-07-04 Bataafsche Petroleum Verfahren zur Gewinnung reiner tert. Butylbenzoesaeuren
GB1003650A (en) * 1963-04-05 1965-09-08 Teijin Ltd Process for producing purified terephthalic acid

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5565609A (en) * 1993-02-12 1996-10-15 Mitsui Petrochemical Industries, Ltd. Method of purifying aromatic dicarboxylic acids
US5840968A (en) * 1995-06-07 1998-11-24 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid
WO1998012157A2 (en) * 1996-09-17 1998-03-26 Tsong-Dar Vincent Lin Process for purification of aromatic polycarboxylic acids

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1131276A4 *

Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7452522B2 (en) 2003-06-05 2008-11-18 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
EP1484306A1 (en) * 2003-06-05 2004-12-08 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
EP1484307A1 (en) * 2003-06-05 2004-12-08 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
EP2292581A1 (en) * 2003-06-05 2011-03-09 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
EP1484305A1 (en) * 2003-06-05 2004-12-08 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
US7282151B2 (en) 2003-06-05 2007-10-16 Eastman Chemical Company Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration
US7494641B2 (en) 2003-06-05 2009-02-24 Eastman Chemical Company Extraction process for removal of impurities from an oxidizer purge stream in the synthesis of carboxylic acid
US7351396B2 (en) 2003-06-05 2008-04-01 Eastman Chemical Company Extraction process for removal of impurities from an aqueous mixture
US7381386B2 (en) 2003-06-05 2008-06-03 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
US7470370B2 (en) 2003-06-05 2008-12-30 Eastman Chemical Company Process for removal of impurities from mother liquor in the synthesis of carboxylic acid using pressure filtration
US7410632B2 (en) 2003-06-05 2008-08-12 Eastman Chemical Company Extraction process for removal of impurities from mother liquor in the synthesis of carboxylic acid
US7556784B2 (en) 2004-09-02 2009-07-07 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
WO2006028815A3 (en) * 2004-09-02 2006-04-27 Eastman Chem Co Optimized liquid-phase oxidation
EP1784378B1 (en) * 2004-09-02 2014-09-24 Grupo Petrotemex, S.A. De C.V. PRODUCTION PROCESS OF crude terephthalic acid
US7959879B2 (en) 2004-09-02 2011-06-14 Grupo Petrotemex, S.A. De C.V. Optimized production of aromatic dicarboxylic acids
US7888530B2 (en) 2004-09-02 2011-02-15 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7897810B2 (en) 2004-09-02 2011-03-01 Eastman Chemical Company Optimized production of aromatic dicarboxylic acids
US7291270B2 (en) 2004-10-28 2007-11-06 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7273559B2 (en) 2004-10-28 2007-09-25 Eastman Chemical Company Process for removal of impurities from an oxidizer purge stream
US7569722B2 (en) 2005-08-11 2009-08-04 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7402694B2 (en) 2005-08-11 2008-07-22 Eastman Chemical Company Process for removal of benzoic acid from an oxidizer purge stream
US7759516B2 (en) 2006-03-01 2010-07-20 Eastman Chemical Company Versatile oxidation byproduct purge process
US7902395B2 (en) 2006-03-01 2011-03-08 Eastman Chemical Company Versatile oxidation byproduct purge process
US7897808B2 (en) 2006-03-01 2011-03-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7956215B2 (en) 2006-03-01 2011-06-07 Grupo Petrotemex, S.A. De C.V. Versatile oxidation byproduct purge process
US7880032B2 (en) 2006-03-01 2011-02-01 Eastman Chemical Company Versatile oxidation byproduct purge process
US7863481B2 (en) 2006-03-01 2011-01-04 Eastman Chemical Company Versatile oxidation byproduct purge process
WO2015186073A1 (en) * 2014-06-04 2015-12-10 Reliance Industries Limited Process for the purification of crude carboxylic acid

Also Published As

Publication number Publication date
EP1131276A1 (en) 2001-09-12
KR100642625B1 (ko) 2006-11-10
KR20010101068A (ko) 2001-11-14
WO2000031014A8 (en) 2000-08-17
EP1131276A4 (en) 2002-09-18
JP2003510247A (ja) 2003-03-18
CN1264798C (zh) 2006-07-19
CN1332714A (zh) 2002-01-23

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