JP2006519257A5 - - Google Patents

Download PDF

Info

Publication number
JP2006519257A5
JP2006519257A5 JP2006508773A JP2006508773A JP2006519257A5 JP 2006519257 A5 JP2006519257 A5 JP 2006519257A5 JP 2006508773 A JP2006508773 A JP 2006508773A JP 2006508773 A JP2006508773 A JP 2006508773A JP 2006519257 A5 JP2006519257 A5 JP 2006519257A5
Authority
JP
Japan
Prior art keywords
product
zone
reactant
withdrawn
liquid fraction
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.)
Granted
Application number
JP2006508773A
Other languages
English (en)
Japanese (ja)
Other versions
JP5059400B2 (ja
JP2006519257A (ja
Filing date
Publication date
Application filed filed Critical
Priority claimed from PCT/US2004/004948 external-priority patent/WO2004078679A2/en
Publication of JP2006519257A publication Critical patent/JP2006519257A/ja
Publication of JP2006519257A5 publication Critical patent/JP2006519257A5/ja
Application granted granted Critical
Publication of JP5059400B2 publication Critical patent/JP5059400B2/ja
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

JP2006508773A 2003-02-28 2004-02-19 平衡制限反応の実施方法 Expired - Lifetime JP5059400B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US45074603P 2003-02-28 2003-02-28
US60/450,746 2003-02-28
PCT/US2004/004948 WO2004078679A2 (en) 2003-02-28 2004-02-19 Process for conducting equilibrium-limited reactions

Publications (3)

Publication Number Publication Date
JP2006519257A JP2006519257A (ja) 2006-08-24
JP2006519257A5 true JP2006519257A5 (https=) 2007-04-12
JP5059400B2 JP5059400B2 (ja) 2012-10-24

Family

ID=32962524

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006508773A Expired - Lifetime JP5059400B2 (ja) 2003-02-28 2004-02-19 平衡制限反応の実施方法

Country Status (9)

Country Link
US (1) US7569721B2 (https=)
EP (1) EP1611082B1 (https=)
JP (1) JP5059400B2 (https=)
KR (1) KR101136783B1 (https=)
CN (1) CN100345816C (https=)
BR (1) BRPI0408043B1 (https=)
DE (1) DE602004028591D1 (https=)
MX (1) MX256948B (https=)
WO (1) WO2004078679A2 (https=)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10357222A1 (de) * 2003-12-08 2005-06-30 Basf Ag Anschlussstutzen für Messgeräte und mit einem solchen Anschlussstutzen versehene Messsonde
DE102005043719A1 (de) * 2005-09-13 2007-03-15 Röhm Gmbh Vorrichtung und Verfahren für kontinuierlich durchgeführte Gleichgewichtsreaktionen
WO2012071158A1 (en) 2010-11-22 2012-05-31 Rohm And Haas Company Acrylate production process
SG11201510267TA (en) 2013-06-28 2016-01-28 Dow Global Technologies Llc Fouling-resistant distillation column and process for the manufacture of compounds
FR3014870B1 (fr) * 2013-12-13 2015-12-11 Arkema France Procede de production d'esters (meth)acryliques
SG11201703365VA (en) 2014-10-31 2017-05-30 Dow Global Technologies Llc Process for in situ water removal from an oxidative esterification reaction using a coupled reactor-distillation system
KR102151747B1 (ko) * 2018-11-23 2020-09-03 지에스칼텍스 주식회사 알킬 카르복실산 에스테르의 제조 방법 및 알킬 카르복실산 에스테르의 제조 장치
WO2022270495A1 (ja) * 2021-06-21 2022-12-29 旭化成株式会社 反応システム及び反応方法

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3776947A (en) 1972-10-10 1973-12-04 Nippon Catalytic Chem Ind Continuous esterification process
DE2548561C2 (de) 1975-10-30 1983-09-29 Hoechst Ag, 6230 Frankfurt Verfahren zur kontinuierlichen Herstellung dioctylätherfreien 2-Äthyl- hexylacrylats
JPS6317844A (ja) 1986-07-09 1988-01-25 Nippon Shokubai Kagaku Kogyo Co Ltd 不飽和カルボン酸エステルの製造方法
DE4019781A1 (de) 1990-06-21 1992-01-02 Basf Ag Verfahren zur herstellung von monoethylenisch ungesaettigten carbonsaeureestern
US5231222A (en) 1991-07-02 1993-07-27 Union Carbide Chemicals & Plastics Technology Corporation Esterification process
JP3346822B2 (ja) 1993-03-31 2002-11-18 三菱化学株式会社 アクリル酸エステル又はメタクリル酸エステルの製造法
FR2721313B1 (fr) 1994-06-17 1996-07-19 Atochem Elf Sa Procédé de fabrication d'acrylates d'alkyle par estérification directe.
DE19536178A1 (de) 1995-09-28 1997-04-03 Basf Ag Verfahren und Vorrichtung zur kontinuierlichen Herstellung von Alkylestern der (Meth)acrylsäure
DE19536191A1 (de) 1995-09-28 1997-04-03 Basf Ag Verfahren zum Verestern von (Meth)acrylsäure mit einem Alkanol
DE19604267A1 (de) * 1996-02-06 1997-08-07 Basf Ag Verfahren zur kontinuierlichen Herstellung von Alkylestern der (Meth)acrylsäure
DE19604253A1 (de) 1996-02-06 1997-08-07 Basf Ag Verfahren zur kontinuierlichen Herstellung von Alkylestern der (Meth)acrylsäure
WO1998052903A1 (en) * 1997-05-20 1998-11-26 Union Carbide Chemicals & Plastics Technology Corporation Processes for conducting equilibrium-limited reactions
BR9714713A (pt) 1997-05-20 2000-07-04 Union Carbide Chem Plastic Processos para o refino de acrilato de butila
DE69812682T2 (de) 1997-10-31 2003-12-18 Celanese International Corp., Dallas Entfernung von schwefel aus einem acrylatstrom
JP4242964B2 (ja) 1999-03-09 2009-03-25 株式会社日本触媒 (メタ)アクリル酸および/またはそのエステルの精製方法
JP3782607B2 (ja) * 1999-04-20 2006-06-07 株式会社日本触媒 エステル化物の製造方法
US6482976B1 (en) * 1999-06-17 2002-11-19 Union Carbide Chemicals & Plastics Technology Corporation Processes for conducting equilibrium-limited reactions
JP2003521478A (ja) 1999-06-17 2003-07-15 ユニオン・カーバイド・ケミカルズ・アンド・プラスティックス・テクノロジー・コーポレイション 平衡律速反応を行う方法

Similar Documents

Publication Publication Date Title
CN104024210B (zh) 通过直接酯化制造丙烯酸2-辛酯的方法
WO2009106550A9 (de) Verfahren zur herstellung von (meth)acrylaten von c10-alkoholgemischen
JP2014534972A5 (https=)
US10941103B2 (en) Process for continuously preparing n-butyl acrylate or isobutyl acrylate
JP6030564B2 (ja) ブチルアクリレートの製造方法
TW201802063A (zh) 用於生產(甲基)丙烯酸之改良方法
JP2019504078A (ja) (メタ)アクリル酸エステルの精製方法
JP2019163294A (ja) 軽質(メタ)アクリル酸エステルの製造方法
JP2002509905A (ja) アクリル酸およびアクリル酸エステルの製造方法
US20140105792A1 (en) Process for continuous recovering (meth) acrylic acid and apparatus for the process
CN105189440B (zh) 制备琥珀酸酯的方法
BR112015013542B1 (pt) Processo de produção de acrilato de alquila
CN105408299A (zh) 通过粗酯级丙烯酸的酯化连续生产轻质丙烯酸酯的方法
JP2003026633A (ja) メタクリル酸エステルの製造方法
Constantino et al. Butyl acrylate production: A review on process intensification strategies
WO2009013623A2 (en) Azeotropic distillation with entrainer regeneration
JP2006519257A5 (https=)
JP5559205B2 (ja) N,n−ジメチルアミノエチルアクリレート合成中に生じる共沸留分の精製方法
JP2003521478A5 (https=)
JP2001322968A (ja) メタクリル酸エステルの精製方法
US12098123B2 (en) Polymer grade acrylic acid production
CN104053643B (zh) 通过酯交换制备丙烯酸2-辛基酯的方法
JP2024506199A (ja) 高純度アルキルアクリレートを製造するための改善された方法
JP2003226668A (ja) (メタ)アクリル酸エステル製造時の副生物の分解方法
JP2003160530A (ja) (メタ)アクリル酸の精製方法