KR880003891A - 방향족 카르복시산의 제조방법 - Google Patents
방향족 카르복시산의 제조방법 Download PDFInfo
- Publication number
- KR880003891A KR880003891A KR1019870010681A KR870010681A KR880003891A KR 880003891 A KR880003891 A KR 880003891A KR 1019870010681 A KR1019870010681 A KR 1019870010681A KR 870010681 A KR870010681 A KR 870010681A KR 880003891 A KR880003891 A KR 880003891A
- Authority
- KR
- South Korea
- Prior art keywords
- carboxylic acid
- aromatic carboxylic
- acid
- producing
- liquid phase
- Prior art date
Links
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 title claims 9
- 238000004519 manufacturing process Methods 0.000 title claims 4
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims 3
- 150000001875 compounds Chemical class 0.000 claims 3
- 238000000034 method Methods 0.000 claims 3
- FYGHSUNMUKGBRK-UHFFFAOYSA-N 1,2,3-trimethylbenzene Chemical compound CC1=CC=CC(C)=C1C FYGHSUNMUKGBRK-UHFFFAOYSA-N 0.000 claims 2
- QNLZIZAQLLYXTC-UHFFFAOYSA-N 1,2-dimethylnaphthalene Chemical compound C1=CC=CC2=C(C)C(C)=CC=C21 QNLZIZAQLLYXTC-UHFFFAOYSA-N 0.000 claims 2
- QPUYECUOLPXSFR-UHFFFAOYSA-N 1-methylnaphthalene Chemical compound C1=CC=C2C(C)=CC=CC2=C1 QPUYECUOLPXSFR-UHFFFAOYSA-N 0.000 claims 2
- 239000007789 gas Substances 0.000 claims 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 claims 2
- 239000007791 liquid phase Substances 0.000 claims 2
- 230000003647 oxidation Effects 0.000 claims 2
- LNETULKMXZVUST-UHFFFAOYSA-N 1-naphthoic acid Chemical compound C1=CC=C2C(C(=O)O)=CC=CC2=C1 LNETULKMXZVUST-UHFFFAOYSA-N 0.000 claims 1
- 239000005711 Benzoic acid Substances 0.000 claims 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims 1
- 239000002253 acid Substances 0.000 claims 1
- 125000000217 alkyl group Chemical group 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 235000010233 benzoic acid Nutrition 0.000 claims 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims 1
- 229910052794 bromium Inorganic materials 0.000 claims 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims 1
- 229910001385 heavy metal Inorganic materials 0.000 claims 1
- 150000002736 metal compounds Chemical class 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000012071 phase Substances 0.000 claims 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims 1
- 150000003628 tricarboxylic acids Chemical class 0.000 claims 1
- 239000008096 xylene Substances 0.000 claims 1
- 238000010586 diagram Methods 0.000 description 1
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
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/00108—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/0011—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명에서 사용하는 산화반응장치를 표시한 계통도.
Claims (4)
- 알킬방향족 화합물을 액상으로 중금속화합물 및/또는 브롬 함유 화합물의 존재하에 산소함유가스로 산화하여 연속적으로 방향족 카르복시산을 제조하는 방법에 있어서 산화반응기로부터 배출된 증기로부터 응축성 성분을 제거하여 얻은 배출가스의 일부를 산화반응기의 기상부에 순환시키는 것을 특징으로 하는 방향족 카르복시산의 제조방법
- 제1항에 있어서 응축성 성분의 일부를 산화반응기의 액상부에 순화시키는 방향족 카르복시산의 제조방법
- 제1항 또는 제2항에 있어서, 알킬방향복 화합물은, 톨루엔, O-, m-및 P-크실렌, 트리메틸벤젠, 메틸나프탈렌, 디메틸나프탈렌, P-톨루알데히드 및 P-톨루일산으로 이루어진 군으로부터 선택되는 것인 방향족 카르복시산의 제조방법
- 제1항 내지 제3항의 어느 한 항에 있어서 방향족 카르복시산은 벤조산, 오르토프탈산, 이소프탈산, 텔레프탈산, 트리카르복시산, 나프토산 및 나프탈린디 카르복시산으로 이루어진 군으로부터 선택되는 것인 방향족 카르복시산의 제조방법※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61226131A JPH078821B2 (ja) | 1986-09-26 | 1986-09-26 | 芳香族カルボン酸の製造方法 |
JP226131 | 1986-09-26 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR880003891A true KR880003891A (ko) | 1988-06-01 |
KR900006705B1 KR900006705B1 (ko) | 1990-09-17 |
Family
ID=16840330
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019870010681A KR900006705B1 (ko) | 1986-09-26 | 1987-09-25 | 방향족 카르복시산의 제조방법 |
Country Status (8)
Country | Link |
---|---|
US (1) | US4827025A (ko) |
EP (1) | EP0261892B1 (ko) |
JP (1) | JPH078821B2 (ko) |
KR (1) | KR900006705B1 (ko) |
CN (1) | CN1021221C (ko) |
CA (1) | CA1289150C (ko) |
DE (1) | DE3775683D1 (ko) |
IN (1) | IN168387B (ko) |
Families Citing this family (68)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0483106B1 (de) * | 1987-11-24 | 1994-08-31 | Hoechst Aktiengesellschaft | Verfahren zur Herstellung teilfluorierter Tetracarbonsäuren |
JPH0613468B2 (ja) * | 1989-09-27 | 1994-02-23 | 新日本理化株式会社 | ジフェニルスルホンテトラカルボン酸の製造方法 |
US5371283A (en) * | 1993-12-22 | 1994-12-06 | Praxair Technology, Inc. | Terephthalic acid production |
IN182716B (ko) * | 1994-03-22 | 1999-07-03 | Mitsui Petrochemical Ind | |
US5523474A (en) * | 1994-05-11 | 1996-06-04 | Praxair Technology, Inc. | Terephthalic acid production using evaporative cooling |
US5693856A (en) | 1996-01-16 | 1997-12-02 | The Boc Group, Inc. | Production of terephthalic acid |
ID15851A (id) * | 1996-02-13 | 1997-08-14 | Mitsubishi Chem Corp | Proses untuk menghasilkan suatu asam aromatik karboksilik |
KR100437562B1 (ko) * | 1996-06-07 | 2004-10-02 | 주식회사 삼양사 | 테레프탈산제조공정에서발생되는폐기물로부터안식향산을회수하는방법 |
US6114575A (en) * | 1997-03-25 | 2000-09-05 | Bp Amoco Corporation | Process for preparing 2,6-naphthalenedicarboxylic acid |
KR20000005733A (ko) * | 1998-06-05 | 2000-01-25 | 나까니시 히로유끼 | 방향족카복실산의제조방법 |
JP3885373B2 (ja) * | 1998-07-28 | 2007-02-21 | 三井化学株式会社 | 芳香族カルボン酸の製造方法 |
US6649773B2 (en) | 2002-03-22 | 2003-11-18 | General Electric Company | Method for the manufacture of halophthalic acids and anhydrides |
US6657068B2 (en) | 2002-03-22 | 2003-12-02 | General Electric Company | Liquid phase oxidation of halogenated ortho-xylenes |
US6657067B2 (en) | 2002-03-22 | 2003-12-02 | General Electric Company | Method for the manufacture of chlorophthalic anhydride |
US7541489B2 (en) * | 2004-06-30 | 2009-06-02 | Sabic Innovative Plastics Ip B.V. | Method of making halophthalic acids and halophthalic anhydrides |
US20060004223A1 (en) * | 2004-06-30 | 2006-01-05 | General Electric Company | Method of making halophthalic acids and halophthalic anhydrides |
US7507857B2 (en) * | 2004-09-02 | 2009-03-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7381836B2 (en) * | 2004-09-02 | 2008-06-03 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US20060047153A1 (en) * | 2004-09-02 | 2006-03-02 | Wonders Alan G | Optimized liquid-phase oxidation |
US7572932B2 (en) | 2004-09-02 | 2009-08-11 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7910769B2 (en) * | 2004-09-02 | 2011-03-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7399882B2 (en) * | 2004-09-02 | 2008-07-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7495125B2 (en) * | 2004-09-02 | 2009-02-24 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7586000B2 (en) * | 2004-09-02 | 2009-09-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7504535B2 (en) * | 2004-09-02 | 2009-03-17 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7608733B2 (en) * | 2004-09-02 | 2009-10-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7692037B2 (en) | 2004-09-02 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7390921B2 (en) | 2004-09-02 | 2008-06-24 | 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 |
US7589231B2 (en) * | 2004-09-02 | 2009-09-15 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7683210B2 (en) * | 2004-09-02 | 2010-03-23 | 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 |
US7563926B2 (en) * | 2004-09-02 | 2009-07-21 | 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 |
US7361784B2 (en) * | 2004-09-02 | 2008-04-22 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7582793B2 (en) * | 2004-09-02 | 2009-09-01 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US7692036B2 (en) * | 2004-11-29 | 2010-04-06 | Eastman Chemical Company | Optimized liquid-phase oxidation |
US20060116531A1 (en) * | 2004-11-29 | 2006-06-01 | Wonders Alan G | Modeling of liquid-phase oxidation |
US20060205974A1 (en) * | 2005-03-08 | 2006-09-14 | Lavoie Gino G | Processes for producing aromatic dicarboxylic acids |
US7550627B2 (en) * | 2005-03-08 | 2009-06-23 | Eastman Chemical Company | Processes for producing aromatic dicarboxylic acids |
US7432395B2 (en) * | 2005-05-19 | 2008-10-07 | Eastman Chemical Company | Enriched carboxylic acid composition |
US7741516B2 (en) | 2005-05-19 | 2010-06-22 | Eastman Chemical Company | Process to enrich a carboxylic acid composition |
US7897809B2 (en) * | 2005-05-19 | 2011-03-01 | Eastman Chemical Company | Process to produce an enrichment feed |
US7884231B2 (en) * | 2005-05-19 | 2011-02-08 | Eastman Chemical Company | Process to produce an enriched composition |
US20060264664A1 (en) * | 2005-05-19 | 2006-11-23 | Parker Kenny R | Esterification of an exchange solvent enriched composition |
US7557243B2 (en) | 2005-05-19 | 2009-07-07 | Eastman Chemical Company | Enriched terephthalic acid 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 |
US7304178B2 (en) * | 2005-05-19 | 2007-12-04 | Eastman Chemical Company | Enriched isophthalic acid 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 |
US20060264662A1 (en) * | 2005-05-19 | 2006-11-23 | Gibson Philip E | Esterification of an enriched composition |
US7834208B2 (en) * | 2005-05-19 | 2010-11-16 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
US7884232B2 (en) * | 2005-06-16 | 2011-02-08 | Eastman Chemical Company | Optimized liquid-phase oxidation |
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 |
US7888529B2 (en) | 2006-03-01 | 2011-02-15 | Eastman Chemical Company | Process to produce a post catalyst removal composition |
CN100417633C (zh) * | 2006-07-17 | 2008-09-10 | 中国石油化工股份有限公司 | 一种多元芳香羧酸的制备方法 |
US8115029B2 (en) * | 2006-11-02 | 2012-02-14 | University Of Kansas | Cobalt-catalyzed oxidations in volumetrically expanded liquids by compressed gases |
CN101244996B (zh) * | 2007-02-16 | 2012-11-21 | 北京石油化工学院 | 一种合成萘二甲酸用的立式鼓泡氧化反应装置 |
CN101279904A (zh) * | 2007-04-03 | 2008-10-08 | 波克股份有限公司 | 制造芳族羧酸的改进方法 |
CN105503583A (zh) * | 2014-10-29 | 2016-04-20 | 张湉 | 一种安息香酸的制备方法 |
WO2018104986A1 (ja) * | 2016-12-08 | 2018-06-14 | カンケンテクノ株式会社 | 脱臭装置 |
CN110128260A (zh) * | 2019-02-26 | 2019-08-16 | 沅江华龙催化科技有限公司 | 一种节能环保的环己烷空气氧化合成己二酸的方法 |
CN110105192A (zh) * | 2019-02-26 | 2019-08-09 | 沅江华龙催化科技有限公司 | 一种节能环保的甲苯衍生物空气氧化合成苯甲酸衍生物的方法 |
CN115634642A (zh) * | 2021-07-19 | 2023-01-24 | 河北大景大搪化工设备有限公司 | 一种氯代脂肪酸甲酯反应塔及其所构成的制备装置 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE562538A (ko) * | 1956-11-21 | 1900-01-01 | ||
US3086993A (en) * | 1958-12-31 | 1963-04-23 | Standard Oil Co | Liquid phase oxidation process |
DE1768899A1 (de) * | 1968-07-11 | 1972-01-13 | Basf Ag | Verfahren zur Herstellung von Benzolcarbonsaeuren |
GB2072162B (en) * | 1980-03-21 | 1984-03-21 | Labofina Sa | Process for the production and the recovery of terephthalic acid |
JPS5852243A (ja) * | 1981-09-24 | 1983-03-28 | Mitsubishi Gas Chem Co Inc | テレフタル酸の製造法 |
JPS6036439A (ja) * | 1983-08-09 | 1985-02-25 | Mitsubishi Chem Ind Ltd | テレフタル酸の製法 |
US4777287A (en) * | 1984-10-29 | 1988-10-11 | Amoco Corporation | Recycle of vaporized solvent in liquid phase oxidation of an alkyl aromatic |
-
1986
- 1986-09-26 JP JP61226131A patent/JPH078821B2/ja not_active Expired - Lifetime
-
1987
- 1987-09-16 US US07/097,800 patent/US4827025A/en not_active Expired - Fee Related
- 1987-09-18 EP EP87308288A patent/EP0261892B1/en not_active Expired - Lifetime
- 1987-09-18 DE DE8787308288T patent/DE3775683D1/de not_active Expired - Fee Related
- 1987-09-24 CA CA000547742A patent/CA1289150C/en not_active Expired - Fee Related
- 1987-09-25 KR KR1019870010681A patent/KR900006705B1/ko not_active IP Right Cessation
- 1987-09-26 CN CN87106585A patent/CN1021221C/zh not_active Expired - Fee Related
- 1987-11-30 IN IN939/CAL/87A patent/IN168387B/en unknown
Also Published As
Publication number | Publication date |
---|---|
CA1289150C (en) | 1991-09-17 |
JPH078821B2 (ja) | 1995-02-01 |
KR900006705B1 (ko) | 1990-09-17 |
EP0261892B1 (en) | 1992-01-02 |
EP0261892A3 (en) | 1989-03-15 |
IN168387B (ko) | 1991-03-23 |
EP0261892A2 (en) | 1988-03-30 |
DE3775683D1 (de) | 1992-02-13 |
US4827025A (en) | 1989-05-02 |
CN87106585A (zh) | 1988-06-01 |
JPS6383046A (ja) | 1988-04-13 |
CN1021221C (zh) | 1993-06-16 |
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