BG31071A3 - Method for extraction of tereftalic acid by continuous ckystallisation - Google Patents

Method for extraction of tereftalic acid by continuous ckystallisation

Info

Publication number
BG31071A3
BG31071A3 BG027525A BG2752574A BG31071A3 BG 31071 A3 BG31071 A3 BG 31071A3 BG 027525 A BG027525 A BG 027525A BG 2752574 A BG2752574 A BG 2752574A BG 31071 A3 BG31071 A3 BG 31071A3
Authority
BG
Bulgaria
Prior art keywords
terephthalic acid
temperature
continuous
acid
crystallization
Prior art date
Application number
BG027525A
Other languages
Bulgarian (bg)
English (en)
Inventor
Jay Fisher
Original Assignee
The Standard Oil Co.
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 The Standard Oil Co. filed Critical The Standard Oil Co.
Publication of BG31071A3 publication Critical patent/BG31071A3/xx

Links

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
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
BG027525A 1973-08-20 1974-08-20 Method for extraction of tereftalic acid by continuous ckystallisation BG31071A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US05/389,717 US3931305A (en) 1973-08-20 1973-08-20 Terephthalic acid recovery by continuous flash crystallization

Publications (1)

Publication Number Publication Date
BG31071A3 true BG31071A3 (en) 1981-10-15

Family

ID=23539427

Family Applications (1)

Application Number Title Priority Date Filing Date
BG027525A BG31071A3 (en) 1973-08-20 1974-08-20 Method for extraction of tereftalic acid by continuous ckystallisation

Country Status (22)

Country Link
US (1) US3931305A (xx)
JP (1) JPS5324057B2 (xx)
BE (1) BE818228A (xx)
BG (1) BG31071A3 (xx)
BR (1) BR7406531D0 (xx)
CA (1) CA1019342A (xx)
CS (1) CS198150B2 (xx)
DD (1) DD115109A5 (xx)
DE (1) DE2437846A1 (xx)
EG (1) EG11555A (xx)
ES (1) ES429400A1 (xx)
FR (1) FR2241529B1 (xx)
GB (1) GB1476436A (xx)
HU (1) HU180065B (xx)
IN (1) IN142341B (xx)
IT (1) IT1018896B (xx)
NL (1) NL7409866A (xx)
PL (1) PL100195B1 (xx)
RO (1) RO66116A (xx)
SU (1) SU869554A3 (xx)
TR (1) TR18050A (xx)
YU (1) YU41043B (xx)

Families Citing this family (80)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51132395U (xx) * 1975-04-14 1976-10-25
GB1582255A (en) * 1976-08-11 1981-01-07 Ici Ltd Crystallisation of terephthalic acid
DE3037045C2 (de) * 1980-10-01 1987-02-26 Dynamit Nobel Ag, 5210 Troisdorf Verfahren zur Kristallisation in einem Lösungsmittel bis zur Sättigung gelöster Terephthalsäure und Kristallisationsvorrichtung
IT1163145B (it) * 1983-03-11 1987-04-08 Friuli Chim Spa Preparazione di acido benzoico puro
US5567842A (en) * 1994-11-16 1996-10-22 Mitsubishi Chemical Corporation Process for producing terephthalic acid
US5502247A (en) * 1994-11-17 1996-03-26 Amoco Corporation Process for recovery of aromatic acid or ester and polyol from waste polyester resins
US5929274A (en) * 1995-06-07 1999-07-27 Hfm International, Inc. Method to reduce carboxybenzaldehyde isomers in terephthalic acid or isophthalic acid
US6054610A (en) * 1995-06-07 2000-04-25 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid and isophthalic acid from mixed xylenes
US5840968A (en) * 1995-06-07 1998-11-24 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid
US5767311A (en) * 1995-06-07 1998-06-16 Glitsch International, Inc. Method and apparatus for preparing purified terephtalic acid
US6013835A (en) * 1995-06-07 2000-01-11 Hfm International, Inc. Method and apparatus for preparing purified terephthalic acid
US7485747B2 (en) * 2001-06-04 2009-02-03 Eastman Chemical Company Two stage oxidation process for the production of aromatic dicarboxylic acids
US7196215B2 (en) * 2001-06-04 2007-03-27 Eastman Chemical Company Process for the production of purified terephthalic acid
US6689903B2 (en) * 2001-06-04 2004-02-10 Eastman Chemical Company Crystallization method for production of purified 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
WO2004063135A1 (ja) * 2003-01-10 2004-07-29 Mitsubishi Chemical Corporation 芳香族カルボン酸の製造方法およびテレフタル酸の製造方法
US7193109B2 (en) * 2003-03-06 2007-03-20 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
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
US7546747B2 (en) * 2004-01-15 2009-06-16 Eastman Chemical Company Process for production of a dried carboxylic acid cake suitable for use in polyester production
US7214760B2 (en) * 2004-01-15 2007-05-08 Eastman Chemical Company Process for production of a carboxylic acid/diol mixture suitable for use in polyester production
TW200605867A (en) 2004-03-17 2006-02-16 Novartis Ag Use of organic compounds
US7572936B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7568361B2 (en) * 2004-09-02 2009-08-04 Eastman Chemical Company Optimized liquid-phase oxidation
US7608733B2 (en) * 2004-09-02 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US20060047153A1 (en) * 2004-09-02 2006-03-02 Wonders Alan G Optimized liquid-phase oxidation
US7495125B2 (en) * 2004-09-02 2009-02-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7507857B2 (en) * 2004-09-02 2009-03-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7371894B2 (en) * 2004-09-02 2008-05-13 Eastman Chemical Company Optimized liquid-phase oxidation
US7504535B2 (en) * 2004-09-02 2009-03-17 Eastman Chemical Company Optimized liquid-phase oxidation
US7390921B2 (en) * 2004-09-02 2008-06-24 Eastman Chemical Company Optimized liquid-phase oxidation
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7582793B2 (en) 2004-09-02 2009-09-01 Eastman Chemical Company Optimized liquid-phase oxidation
US7589231B2 (en) * 2004-09-02 2009-09-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7586000B2 (en) * 2004-09-02 2009-09-08 Eastman Chemical Company Optimized liquid-phase oxidation
US7692037B2 (en) * 2004-09-02 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7563926B2 (en) * 2004-09-02 2009-07-21 Eastman Chemical Company Optimized liquid-phase oxidation
US7399882B2 (en) * 2004-09-02 2008-07-15 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7482482B2 (en) * 2004-09-02 2009-01-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7741515B2 (en) 2004-09-02 2010-06-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7572932B2 (en) * 2004-09-02 2009-08-11 Eastman Chemical Company Optimized liquid-phase oxidation
US7361784B2 (en) * 2004-09-02 2008-04-22 Eastman Chemical Company Optimized liquid-phase oxidation
US7381836B2 (en) * 2004-09-02 2008-06-03 Eastman Chemical Company Optimized liquid-phase oxidation
US7692036B2 (en) 2004-11-29 2010-04-06 Eastman Chemical Company Optimized liquid-phase oxidation
US7910769B2 (en) * 2004-09-02 2011-03-22 Eastman Chemical Company Optimized liquid-phase oxidation
JP4747544B2 (ja) * 2004-09-30 2011-08-17 株式会社日立プラントテクノロジー テレフタル酸の精製方法
US7304178B2 (en) * 2005-05-19 2007-12-04 Eastman Chemical Company Enriched isophthalic acid composition
US7884231B2 (en) 2005-05-19 2011-02-08 Eastman Chemical Company Process to produce an enriched composition
US7880031B2 (en) * 2005-05-19 2011-02-01 Eastman Chemical Company Process to produce an enrichment feed
US7557243B2 (en) 2005-05-19 2009-07-07 Eastman Chemical Company Enriched terephthalic acid composition
US7834208B2 (en) * 2005-05-19 2010-11-16 Eastman Chemical Company Process to produce a post catalyst removal composition
US20060264656A1 (en) * 2005-05-19 2006-11-23 Fujitsu Limited Enrichment process using compounds useful in a polyester process
US7897809B2 (en) * 2005-05-19 2011-03-01 Eastman Chemical Company Process to produce an enrichment feed
US7741516B2 (en) 2005-05-19 2010-06-22 Eastman Chemical Company Process to enrich a carboxylic acid composition
US20060264664A1 (en) * 2005-05-19 2006-11-23 Parker Kenny R Esterification of an exchange solvent enriched composition
US7432395B2 (en) * 2005-05-19 2008-10-07 Eastman Chemical Company Enriched carboxylic acid composition
US20060264662A1 (en) * 2005-05-19 2006-11-23 Gibson Philip E Esterification of an enriched composition
US7919652B2 (en) * 2005-05-19 2011-04-05 Eastman Chemical Company Process to produce an enriched composition through the use of a catalyst removal zone and an enrichment zone
US7884232B2 (en) * 2005-06-16 2011-02-08 Eastman Chemical Company Optimized liquid-phase oxidation
US20070155987A1 (en) * 2006-01-04 2007-07-05 O'meadhra Ruairi S Oxidative digestion with optimized agitation
US7355068B2 (en) 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US7358389B2 (en) * 2006-01-04 2008-04-15 Eastman Chemical Company Oxidation system employing internal structure for enhanced hydrodynamics
US20070179312A1 (en) * 2006-02-02 2007-08-02 O'meadhra Ruairi Seosamh Process for the purification of a crude carboxylic axid slurry
US7462736B2 (en) * 2006-03-01 2008-12-09 Eastman Chemical Company Methods and apparatus for isolating carboxylic acid
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
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage 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
US7420082B2 (en) 2006-03-01 2008-09-02 Eastman Chemical Company Polycarboxylic acid production system employing hot liquor removal downstream of oxidative digestion
US7501537B2 (en) * 2006-03-01 2009-03-10 Eastman Chemical Company Polycarboxylic acid production system employing oxidative digestion with reduced or eliminated upstream liquor exchange
US7888529B2 (en) * 2006-03-01 2011-02-15 Eastman Chemical Company Process to produce a post catalyst removal composition
US7772424B2 (en) * 2006-03-01 2010-08-10 Eastman Chemical Company Polycarboxylic acid production system employing enhanced evaporative concentration downstream of oxidative digestion
US7847121B2 (en) * 2006-03-01 2010-12-07 Eastman Chemical Company Carboxylic acid production process
US7863483B2 (en) * 2006-03-01 2011-01-04 Eastman Chemical Company Carboxylic acid production process
US9205388B2 (en) * 2007-06-27 2015-12-08 H R D Corporation High shear system and method for the production of acids
US8614350B2 (en) 2008-01-15 2013-12-24 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
US8455680B2 (en) 2008-01-15 2013-06-04 Eastman Chemical Company Carboxylic acid production process employing solvent from esterification of lignocellulosic material
US8969404B2 (en) * 2012-06-22 2015-03-03 Eastman Chemical Company Purifying crude furan 2,5-dicarboxylic acid by hydrogenation
US9029580B2 (en) 2012-07-20 2015-05-12 Eastman Chemical Company Oxidation process to produce a purified carboxylic acid product via solvent displacement and post oxidation

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3639465A (en) * 1968-06-18 1972-02-01 Standard Oil Co Purification of aromatic polycarboxylic acids by catalytic reduction using prehumidified hydrogen
US3655729A (en) * 1968-07-18 1972-04-11 Gen Tire & Rubber Co Process for preparing esters of terephthalic acid
US3708532A (en) * 1968-11-04 1973-01-02 Teijin Ltd Process for the continuous purification of crude terephthalic acid
DE1925038C3 (de) * 1969-05-16 1980-10-23 Standard Oil Co., Chicago, Ill. (V.St.A.) Verfahren zur Gewinnung von Terephthalsäure

Also Published As

Publication number Publication date
IN142341B (xx) 1977-06-25
YU41043B (en) 1986-10-31
DE2437846C2 (xx) 1989-12-28
CA1019342A (en) 1977-10-18
JPS5049248A (xx) 1975-05-01
US3931305A (en) 1976-01-06
GB1476436A (en) 1977-06-16
PL100195B1 (pl) 1978-09-30
ES429400A1 (es) 1976-09-01
DE2437846A1 (de) 1975-03-06
FR2241529B1 (xx) 1978-08-11
EG11555A (en) 1977-08-15
IT1018896B (it) 1977-10-20
SU869554A3 (ru) 1981-09-30
JPS5324057B2 (xx) 1978-07-18
CS198150B2 (en) 1980-05-30
NL7409866A (nl) 1975-02-24
FR2241529A1 (xx) 1975-03-21
YU224174A (en) 1982-05-31
TR18050A (tr) 1976-09-23
BE818228A (fr) 1975-01-29
BR7406531D0 (pt) 1975-06-03
HU180065B (en) 1983-01-28
RO66116A (ro) 1980-03-15
DD115109A5 (xx) 1975-09-12

Similar Documents

Publication Publication Date Title
BG31071A3 (en) Method for extraction of tereftalic acid by continuous ckystallisation
KR880007542A (ko) 순수 결정성 생성물의 제조방법
GB1467171A (en) Apparatus and method for purifying contaminated liquids by freeze crystallisation
GB1199697A (en) Process for the Removal of Unreacted Ammonia in the Production of Acrylonitrile
GB1135063A (en) Process for the purification of malic acid
KR890000679A (ko) 광물 처리법
CN104310427B (zh) 一种氯乙酸法生产甘氨酸过程中母液的回收利用工艺
GB1415764A (en) Method of recovering tetraalkylammonium salts and preparation of adiponitrile
GB1323478A (en) Process of preparing polyalkylenglycol dibenzoates
SU484213A1 (ru) Способ очистки фолиевой кислоты
SU1393791A1 (ru) Способ получени нитрата кали и хлорида аммони
SU479755A1 (ru) Способ выделени адипиновой кислоты из отходов производства капролактама
BG27881A3 (en) Method of cobalt regenerating from destilation waste products by the dimethyltereptalate production
US2244253A (en) Separation of salts of aminoamidines
GB1387390A (en) Process for the purification of p-nitrophenol
SU422140A3 (xx)
GB915510A (en) Improvements in or relating to the production of trialkyladipic acids
ES378040A1 (es) Procedimiento para la fabricacion de acido borico.
US2745843A (en) Process for the purification of thiophene
SU140804A1 (ru) Способ получени бензоилацетила
SU442152A1 (ru) Способ извлечени хлорида натри из сточных вод установок электрообессоливани нефти
GB1429405A (en) Process for the manufacture of polyhalogenated nicotinic acids
SU455943A1 (ru) Способ получени этилового эфира =нитробензойной кислоты
SU553239A1 (ru) Способ получени дикарбоновых кислот с -с
SU144475A1 (ru) Способ получени хлорацетилхлорида