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 PDFInfo
- 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
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- salt
- acid
- base compound
- derivative
- base
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/48—Separation; 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)
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)
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)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101144887B1 (ko) | 2009-12-16 | 2012-05-14 | 호남석유화학 주식회사 | 이소프탈산의 정제 방법 |
Citations (3)
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)
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 |
-
1999
- 1999-11-19 JP JP2000583843A patent/JP2003510247A/ja active Pending
- 1999-11-19 KR KR1020017006507A patent/KR100642625B1/ko not_active IP Right Cessation
- 1999-11-19 WO PCT/US1999/027604 patent/WO2000031014A1/en not_active Application Discontinuation
- 1999-11-19 CN CNB99813645XA patent/CN1264798C/zh not_active Expired - Fee Related
- 1999-11-19 EP EP99967120A patent/EP1131276A4/en not_active Withdrawn
Patent Citations (3)
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)
Title |
---|
See also references of EP1131276A4 * |
Cited By (28)
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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