KR920018005A - 테레프탈산의 제조방법 - Google Patents
테레프탈산의 제조방법 Download PDFInfo
- Publication number
- KR920018005A KR920018005A KR1019920003690A KR920003690A KR920018005A KR 920018005 A KR920018005 A KR 920018005A KR 1019920003690 A KR1019920003690 A KR 1019920003690A KR 920003690 A KR920003690 A KR 920003690A KR 920018005 A KR920018005 A KR 920018005A
- Authority
- KR
- South Korea
- Prior art keywords
- zone
- terephthalic acid
- band
- aqueous medium
- slurry
- Prior art date
- Legal status (The legal status 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 status listed.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C63/00—Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
- C07C63/14—Monocyclic dicarboxylic acids
- C07C63/15—Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
- C07C63/26—1,4 - Benzenedicarboxylic acid
-
- 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
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/255—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of compounds containing six-membered aromatic rings without ring-splitting
- C07C51/265—Preparation 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
-
- 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
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
-
- 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
- C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
Claims (10)
- 아세트산을 함유하는 반응 매질내에서 파라크실렌을 산화시켜 반응 매질내에 테레프탈산의 슬러리를 만들고; 이 슬러리를 이동가능한 필터밴드에 침척시키고; 제1구역에서 필터 밴드를 통해 슬러리로부터 반응 매질을 제거하여 젖은 상태의 첫번째 침적물을 만들고; 필터 밴드위에 침적물을 제2구역으로 이동시켜 제1수성 매질로 세척하고; 젖어있는 첫번째 침적물 내에 존재하는 반응 매질 및 제1수성 매질을 상기 밴드를 통해 제거하여 젖은 상태의 두번째 침적물을 만드고; 젖어있는 두번째 침적물을 제3구역으로 이동시키고; 제3구역에서 필터 밴드에서 부터 젖어있는 두번째 침적물을 제거하고; 제3구역에서 젖어있는 두 번째 침적물을 제거하는 중이나 또는 이과정을 행한후 곧바로 젖어있는 두 번째 침적물을 제2수성 매질과 혼합하여 제2수성 매질내에 테레프탈산의 슬러리를 만들고; 제2수성 매질로부터 테레프탈산을 회수하고; 제1구역에서 필터 밴드를 통해 제거한 반응 매질을 회수하여 이중 최소 일부의 반응 매질을 산화 단계에 직접 또는 간접적으로 재순환시키는 것으로 구성된, 테레프탈산을 제조하는 방법.
- 제1항에 있어서, 제2 구역에서 필터 밴드를 통해 제거된 제1수성 매질 및 반응 매질의 최소 일부를 임의적으로 제1구역에서부터 회수한 반응 매질을 최소 일부와 함께 산화단계로 되돌려보내고 및/또는 증류시키는 방법.
- 제1항 또는 제2항에 있어서, 제2구역이 연속식 단계로 이루어지는데, 최종 단계 이외의 각 단계에서 고체와 밴드를 통해 유입된 수성 매질이 연속한 단계에서 고체와 밴드를 통과한 수성 매질인 방법.
- 전기한 항의 어느 한 항에 있어서, 슬러릭 침적된 이동가능한 밴드면의 압력이 슬러리가 침적되지않은 밴드면의 압력보다 높은 방법.
- 제4항에 있어서, 밴드 면의 압력보가 0.1-15바인 방법.
- 전기한 항의 어느 한 항에 있어서, 아세트산중의 테레프탈산의 슬러리가 최소한60℃의 온도에서 이동가능한 밴드에 침적된 방법.
- 전기한 항의 어느 한 항에 있어서, 이동가능한 밴드가 테레프탈산으로 이루어진 물질을 제1구역에서부터 제2구역을 통해 제3구역으로 연속적으로 또는 간헐적으로 이동시키는 연속식 밴드인 방법.
- 전기한 항의 어느 한 항에 있어서, 제2수성 매질이 거의 순수한 물인 방법.
- 전기한 항의 어느 한 항에 있어서, 테레프탈산을 제2수성 매질내에 용해시켜 테레프탈산을 포함하는 용액을 만들고, 이 용액을 환원 조건하에서 최소한 약간의 불순물을 환원시키기위한 불균질 촉매 및 수소와 접촉시킨 다음에 냉각시켜 정제된 테레프탈산 고체 생성물을 침전시킨뒤 용액에서 회수하여 제2수성 매질중의 테레프탈산 슬러리를 정제시킨후 테레프탈산을 회수하는 방법.
- 제9항에 있어서, 용액을 냉각시키고 및/또는 증발시켜 덜 순수한 침전물 및 모액을 얻고, 침전물을 모액으로부터 분리해낸뒤 이 모액을 집접 또는 간접적으로 증류 컬럼에 보내고 및/또는 제2 수성 매질중의 크루드한 테레프탈산 재슬러리로 보내고 임의적으로 덜 순수한 침전물을 산화단계에 재순환시키는 방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB919104776A GB9104776D0 (en) | 1991-03-07 | 1991-03-07 | Process for the production of terephthalic acid |
| GB9104776.1 | 1991-03-07 | ||
| IDP97064092A ID19108A (id) | 1991-03-07 | 1992-06-08 | Proses produksi asam tereftalat (pecahan dari p-002451) |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| KR920018005A true KR920018005A (ko) | 1992-10-21 |
| KR100225371B1 KR100225371B1 (ko) | 1999-10-15 |
Family
ID=32599058
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| KR1019920003690A Expired - Fee Related KR100225371B1 (ko) | 1991-03-07 | 1992-03-06 | 테레프탈산의 제조방법 |
Country Status (15)
| Country | Link |
|---|---|
| US (4) | US5527957A (ko) |
| EP (3) | EP0722927A1 (ko) |
| JP (1) | JPH0565246A (ko) |
| KR (1) | KR100225371B1 (ko) |
| CN (2) | CN1038409C (ko) |
| CA (1) | CA2062063C (ko) |
| DE (2) | DE69230569T2 (ko) |
| EG (1) | EG19876A (ko) |
| ES (2) | ES2142006T3 (ko) |
| GB (2) | GB9104776D0 (ko) |
| ID (1) | ID19108A (ko) |
| MX (1) | MX9200997A (ko) |
| RU (1) | RU2106337C1 (ko) |
| SG (1) | SG66231A1 (ko) |
| ZA (1) | ZA921380B (ko) |
Families Citing this family (103)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB9310070D0 (en) * | 1992-05-29 | 1993-06-30 | Ici Plc | Process for the production of purified terephthalic acid |
| GB9400570D0 (en) * | 1994-01-13 | 1994-03-09 | Ici Plc | Handling of materials at elevated pressure |
| TW299318B (ko) * | 1994-11-15 | 1997-03-01 | Mitsubishi Chem Corp | |
| US5961942A (en) * | 1995-06-05 | 1999-10-05 | E. I. Du Pont De Nemours And Company | Effluent gas treatment |
| WO1996039595A1 (en) * | 1995-06-05 | 1996-12-12 | Imperial Chemical Industries Plc | Effluent gas treatment |
| 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 |
| 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 |
| KR100463612B1 (ko) * | 1996-02-22 | 2005-02-28 | 이.아이,듀우판드네모아앤드캄파니 | 방향족폴리카르복실산의제조방법 |
| TW442461B (en) * | 1996-02-22 | 2001-06-23 | Du Pont | Process for the production of an aromatic carboxylic acid |
| GB9705349D0 (en) | 1997-03-14 | 1997-04-30 | Ici Plc | Treatment of effluent streams |
| EP1287913B1 (en) * | 1997-12-12 | 2004-03-24 | Mitsubishi Heavy Industries, Ltd. | Rolling system and rolling method |
| HUP0100656A3 (en) * | 1997-12-15 | 2002-03-28 | Shell Int Research | Method for produce aromatic carboxylic acids |
| TW483886B (en) * | 1998-08-11 | 2002-04-21 | Du Pont | Method for recovering methyl acetate and residual acetic acid in the production of pure terephtalic acid |
| IT1311976B1 (it) * | 1999-03-25 | 2002-03-22 | Franco Codignola | Procedimento per la produzione di acidi aromatici. |
| IT1319169B1 (it) | 2000-07-14 | 2003-09-26 | Eurotecnica Dev & Licensing Sr | Procedimento per la purificazione di acidi carbossilici aromatici. |
| US6765113B2 (en) | 2000-07-19 | 2004-07-20 | E.I. Du Pont De Nemours And Company | Production of aromatic carboxylic acids |
| US6420589B1 (en) | 2000-12-14 | 2002-07-16 | General Electric Company | Process for the production of diaryl carbonates |
| US6384262B1 (en) | 2000-12-14 | 2002-05-07 | General Electric Company | Process for the production of diaryl carbonates |
| US6521777B2 (en) | 2000-12-14 | 2003-02-18 | General Electric Company | Process for the production of diaryl carbonates |
| AU2003256359A1 (en) * | 2002-07-09 | 2004-01-23 | Invista Technologies S.A.R.L. | Process for producing aromatic dicarboxylic acids under supercritical conditions |
| 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 |
| 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 |
| US7074954B2 (en) * | 2002-12-09 | 2006-07-11 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
| AU2003293251A1 (en) * | 2002-12-09 | 2004-06-30 | Eastman Chemical Company | Process for the oxidative purification of terephthalic acid |
| KR100498490B1 (ko) * | 2003-02-28 | 2005-07-01 | 삼성전자주식회사 | 인페이스 신호와 쿼드러쳐 신호 간의 위상차를 가변시킬수 있는 쿼드러쳐 전압제어 발진기 |
| 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 |
| US20050059709A1 (en) * | 2003-09-15 | 2005-03-17 | Meythaler Jay M. | Treatment of a neuropathy with rapid release aminopyridine |
| 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 |
| 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 |
| US20050283022A1 (en) * | 2004-06-18 | 2005-12-22 | Sheppard Ronald B | Filtrate preparation process for terephthalic acid filtrate treatment |
| US7495125B2 (en) | 2004-09-02 | 2009-02-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7692037B2 (en) * | 2004-09-02 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7589231B2 (en) * | 2004-09-02 | 2009-09-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7582793B2 (en) | 2004-09-02 | 2009-09-01 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7683210B2 (en) * | 2004-09-02 | 2010-03-23 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7390921B2 (en) | 2004-09-02 | 2008-06-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7381836B2 (en) * | 2004-09-02 | 2008-06-03 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7608732B2 (en) | 2005-03-08 | 2009-10-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7572932B2 (en) * | 2004-09-02 | 2009-08-11 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7399882B2 (en) * | 2004-09-02 | 2008-07-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US20060047153A1 (en) * | 2004-09-02 | 2006-03-02 | Wonders Alan G | Optimized liquid-phase oxidation |
| US7504535B2 (en) * | 2004-09-02 | 2009-03-17 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7361784B2 (en) | 2004-09-02 | 2008-04-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7692036B2 (en) | 2004-11-29 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7371894B2 (en) * | 2004-09-02 | 2008-05-13 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7741515B2 (en) | 2004-09-02 | 2010-06-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7482482B2 (en) | 2004-09-02 | 2009-01-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7507857B2 (en) | 2004-09-02 | 2009-03-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7563926B2 (en) | 2004-09-02 | 2009-07-21 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| 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 |
| US7586000B2 (en) * | 2004-09-02 | 2009-09-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7910769B2 (en) | 2004-09-02 | 2011-03-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7608733B2 (en) | 2004-09-02 | 2009-10-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| DE602006015446D1 (de) * | 2005-03-21 | 2010-08-26 | Bp Corp North America Inc | Verfahren und vorrichtung zur herstellung aromatischer carboxyl-säuren einschliesslich reiner formen davon |
| US20060264664A1 (en) * | 2005-05-19 | 2006-11-23 | Parker Kenny R | Esterification of an exchange solvent enriched composition |
| US20060264662A1 (en) * | 2005-05-19 | 2006-11-23 | Gibson Philip E | Esterification of an enriched composition |
| US7897809B2 (en) | 2005-05-19 | 2011-03-01 | Eastman Chemical Company | Process to produce an enrichment feed |
| US7432395B2 (en) | 2005-05-19 | 2008-10-07 | Eastman Chemical Company | Enriched carboxylic acid composition |
| 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 |
| US7741516B2 (en) | 2005-05-19 | 2010-06-22 | Eastman Chemical Company | Process to enrich a carboxylic acid composition |
| 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 |
| US20060264656A1 (en) * | 2005-05-19 | 2006-11-23 | Fujitsu Limited | Enrichment process using compounds useful in a polyester process |
| US7880031B2 (en) | 2005-05-19 | 2011-02-01 | Eastman Chemical Company | Process to produce an enrichment feed |
| 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 |
| KR100708919B1 (ko) * | 2005-05-30 | 2007-04-17 | 삼성석유화학(주) | 테레프탈산의 회수 방법 |
| US7884232B2 (en) * | 2005-06-16 | 2011-02-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| CA2626033C (en) | 2005-12-29 | 2013-09-03 | Bp Corporation North America Inc. | Ethanolysis of pet to form det and oxidation thereof |
| US7358389B2 (en) * | 2006-01-04 | 2008-04-15 | Eastman Chemical Company | Oxidation system employing internal structure for enhanced hydrodynamics |
| US7355068B2 (en) | 2006-01-04 | 2008-04-08 | Eastman Chemical Company | Oxidation system with internal secondary reactor |
| US20070179312A1 (en) * | 2006-02-02 | 2007-08-02 | O'meadhra Ruairi Seosamh | Process for the purification of a crude carboxylic axid slurry |
| US8697906B2 (en) * | 2006-03-01 | 2014-04-15 | Grupo Petrotemex, S.A. De C.V. | Methods and apparatus for producing a low-moisture carboxylic acid wet cake |
| US7888529B2 (en) | 2006-03-01 | 2011-02-15 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
| US7462736B2 (en) * | 2006-03-01 | 2008-12-09 | Eastman Chemical Company | Methods and apparatus for isolating carboxylic acid |
| US7847121B2 (en) * | 2006-03-01 | 2010-12-07 | Eastman Chemical Company | Carboxylic acid production process |
| US20070208199A1 (en) * | 2006-03-01 | 2007-09-06 | Kenny Randolph Parker | Methods and apparatus for isolating carboxylic acid |
| US7863483B2 (en) * | 2006-03-01 | 2011-01-04 | Eastman Chemical Company | Carboxylic acid production process |
| US8173836B2 (en) * | 2006-03-01 | 2012-05-08 | Grupo Petrotemex, S.A. De C.V. | Method and apparatus for drying carboxylic acid |
| CN100368370C (zh) * | 2006-03-29 | 2008-02-13 | 中国石化仪征化纤股份有限公司 | 对二甲苯氧化母液中悬浮物的回收系统装置 |
| US8115029B2 (en) | 2006-11-02 | 2012-02-14 | University Of Kansas | Cobalt-catalyzed oxidations in volumetrically expanded liquids by compressed gases |
| RU2463096C2 (ru) * | 2007-12-20 | 2012-10-10 | Хитачи Плант Текнолоджиз, Лтд. | Способ фильтрации кристаллической суспензии |
| 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 |
| CN101417943B (zh) * | 2008-12-08 | 2010-11-10 | 中国纺织工业设计院 | 高效回收利用pta装置精制母液的简易方法和系统 |
| CN101914013B (zh) * | 2010-07-30 | 2015-03-18 | 浙江大学 | 一种节水的对苯二甲酸生产方法 |
| US8466312B2 (en) * | 2010-08-20 | 2013-06-18 | Grupo Petrotemex, S.A. De C.V. | Terephthalic acid purge filtration rate by controlling % water in filter feed slurry |
| WO2012130827A1 (en) * | 2011-03-28 | 2012-10-04 | Dsm Ip Assets B.V. | Process for the preparation of condensation products of melamine |
| US20140175025A1 (en) * | 2012-12-21 | 2014-06-26 | Eastman Chemical Company | Generation of low-solids second mother liquor from terephthalic acid production filter |
| CN104338499B (zh) * | 2013-07-31 | 2016-01-20 | 沅江华龙催化科技有限公司 | 一种液固多相反应分离同步反应器 |
| CN104338500B (zh) * | 2013-07-31 | 2015-12-02 | 沅江华龙催化科技有限公司 | 一种气液固多相反应分离同步反应器 |
| RU2687489C1 (ru) * | 2013-12-18 | 2019-05-14 | Бипи Корпорейшен Норт Америка Инк. | Улучшенный способ и устройство для производства ароматических карбоновых кислот |
| BR112016015320A2 (pt) | 2013-12-30 | 2017-10-10 | Bp Corp North America Inc | misturas de alimentação de ácido carboxílico aromático bruto pressurizado |
| CN103772182B (zh) * | 2014-01-26 | 2015-06-17 | 沅江华龙催化科技有限公司 | 基于气液固多相反应分离同步反应器的利用空气氧化对二甲苯生产对苯二甲酸的方法 |
| JP2015140342A (ja) * | 2014-01-30 | 2015-08-03 | 株式会社日立製作所 | 精製テレフタル酸の製造方法 |
| CN103936581A (zh) * | 2014-04-24 | 2014-07-23 | 天华化工机械及自动化研究设计院有限公司 | 一种提高cta溶剂交换效率的方法 |
| CN105085231A (zh) * | 2014-05-20 | 2015-11-25 | 天华化工机械及自动化研究设计院有限公司 | 一种pta工业装置氧化单元中醋酸溶剂的处理方法 |
| EP4196618A1 (en) | 2020-08-14 | 2023-06-21 | Koch Technology Solutions UK Limited | Recovery of metal catalysts from oxidizer purge streams |
| WO2023021347A1 (en) | 2021-08-20 | 2023-02-23 | Koch Technology Solutions UK Limited | Nickel and cobalt separation in a pta process |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE926605C (de) * | 1953-07-22 | 1955-04-21 | Heinz Dipl-Volksw Hoening | Waschband fuer Drehfilter |
| GB970492A (en) * | 1960-10-18 | 1964-09-23 | Standard Oil Co | Production of aromatic carboxylic acids |
| GB926605A (en) * | 1961-03-24 | 1963-05-22 | Atomic Energy Authority Uk | Improvements in or relating to fire-detection apparatus |
| GB1152575A (en) * | 1965-05-17 | 1969-05-21 | Standard Oil Co | Purification of Aromatic Polycarboxylic Acids. |
| NL6606774A (ko) * | 1965-05-17 | 1966-11-18 | ||
| NL7210541A (ko) * | 1972-08-01 | 1974-02-05 | ||
| US4786753A (en) * | 1987-05-18 | 1988-11-22 | Amoco Corporation | Oxidation process for the manufacture of aromatic acids from alkylaromatic compounds |
| US4782181A (en) * | 1987-06-04 | 1988-11-01 | Amoco Corporation | Process for removal of high molecular weight impurities in the manufacture of purified terephthalic acid |
| JP2545103B2 (ja) * | 1987-12-17 | 1996-10-16 | 三井石油化学工業株式会社 | テレフタル酸スラリ―の分散媒交換方法 |
| JP2595657B2 (ja) * | 1988-05-27 | 1997-04-02 | 三井石油化学工業株式会社 | スラリーから結晶を回収する方法 |
| US4939297A (en) * | 1989-06-05 | 1990-07-03 | Eastman Kodak Company | Extraction process for removal of impurities from terephthalic acid filtrate |
| GB9102393D0 (en) * | 1991-02-05 | 1991-03-20 | Ici Plc | Production of terephthalic acid |
| BR9205881A (pt) * | 1991-04-12 | 1994-08-23 | Amoco Corp | Processo para a preparação de um ácido policarboxílico aromático bruto |
| US5200557A (en) * | 1991-04-12 | 1993-04-06 | Amoco Corporation | Process for preparation of crude terephthalic acid suitable for reduction to prepare purified terephthalic acid |
| US5175355A (en) * | 1991-04-12 | 1992-12-29 | Amoco Corporation | Improved process for recovery of purified terephthalic acid |
-
1991
- 1991-03-07 GB GB919104776A patent/GB9104776D0/en active Pending
-
1992
- 1992-02-02 ES ES96115916T patent/ES2142006T3/es not_active Expired - Lifetime
- 1992-02-02 DE DE69230569T patent/DE69230569T2/de not_active Expired - Lifetime
- 1992-02-20 EP EP96105413A patent/EP0722927A1/en not_active Withdrawn
- 1992-02-20 ES ES92301413T patent/ES2093189T3/es not_active Expired - Lifetime
- 1992-02-20 EP EP92301413A patent/EP0502628B1/en not_active Expired - Lifetime
- 1992-02-20 GB GB929203674A patent/GB9203674D0/en active Pending
- 1992-02-20 SG SG1996002186A patent/SG66231A1/en unknown
- 1992-02-20 DE DE69214859T patent/DE69214859T2/de not_active Expired - Lifetime
- 1992-02-20 EP EP96115916A patent/EP0754673B1/en not_active Expired - Lifetime
- 1992-02-25 ZA ZA921380A patent/ZA921380B/xx unknown
- 1992-02-28 CA CA002062063A patent/CA2062063C/en not_active Expired - Fee Related
- 1992-03-04 EG EG290192A patent/EG19876A/xx active
- 1992-03-05 JP JP4048527A patent/JPH0565246A/ja active Pending
- 1992-03-06 MX MX9200997A patent/MX9200997A/es not_active IP Right Cessation
- 1992-03-06 KR KR1019920003690A patent/KR100225371B1/ko not_active Expired - Fee Related
- 1992-03-06 RU SU5011176A patent/RU2106337C1/ru active
- 1992-03-07 CN CN92101553A patent/CN1038409C/zh not_active Expired - Fee Related
- 1992-06-08 ID IDP97064092A patent/ID19108A/id unknown
-
1995
- 1995-06-06 US US08/470,965 patent/US5527957A/en not_active Expired - Lifetime
- 1995-06-06 US US08/470,955 patent/US5563293A/en not_active Expired - Lifetime
-
1996
- 1996-07-17 US US08/682,424 patent/US5679846A/en not_active Expired - Lifetime
- 1996-08-15 CN CN96109974A patent/CN1067977C/zh not_active Expired - Fee Related
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1997
- 1997-05-22 US US08/861,595 patent/US5877346A/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| DE69214859D1 (de) | 1996-12-05 |
| JPH0565246A (ja) | 1993-03-19 |
| KR100225371B1 (ko) | 1999-10-15 |
| US5877346A (en) | 1999-03-02 |
| EP0754673A1 (en) | 1997-01-22 |
| DE69230569D1 (de) | 2000-02-17 |
| US5527957A (en) | 1996-06-18 |
| MX9200997A (es) | 1992-10-01 |
| GB9104776D0 (en) | 1991-04-17 |
| ES2142006T3 (es) | 2000-04-01 |
| US5679846A (en) | 1997-10-21 |
| CN1067977C (zh) | 2001-07-04 |
| DE69214859T2 (de) | 1997-02-27 |
| EG19876A (en) | 1996-06-30 |
| SG66231A1 (en) | 1999-10-19 |
| CA2062063A1 (en) | 1992-09-08 |
| GB9203674D0 (en) | 1992-04-08 |
| DE69230569T2 (de) | 2000-07-27 |
| CN1150945A (zh) | 1997-06-04 |
| EP0754673B1 (en) | 2000-01-12 |
| ZA921380B (en) | 1993-08-25 |
| ES2093189T3 (es) | 1996-12-16 |
| US5563293A (en) | 1996-10-08 |
| RU2106337C1 (ru) | 1998-03-10 |
| EP0502628A2 (en) | 1992-09-09 |
| CN1038409C (zh) | 1998-05-20 |
| EP0722927A1 (en) | 1996-07-24 |
| CA2062063C (en) | 2002-07-09 |
| EP0502628A3 (en) | 1993-01-27 |
| CN1064676A (zh) | 1992-09-23 |
| ID19108A (id) | 1998-06-18 |
| EP0502628B1 (en) | 1996-10-30 |
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