JP2004217575A5 - - Google Patents

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JP2004217575A5
JP2004217575A5 JP2003007540A JP2003007540A JP2004217575A5 JP 2004217575 A5 JP2004217575 A5 JP 2004217575A5 JP 2003007540 A JP2003007540 A JP 2003007540A JP 2003007540 A JP2003007540 A JP 2003007540A JP 2004217575 A5 JP2004217575 A5 JP 2004217575A5
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Japan
Prior art keywords
meth
mol
acrylic acid
acid ester
tin
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JP2003007540A
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Japanese (ja)
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JP4266645B2 (en
JP2004217575A (en
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Publication of JP2004217575A5 publication Critical patent/JP2004217575A5/ja
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【特許請求の範囲】
【請求項1】 スズ化合物(C1)を触媒として原料の(メタ)アクリル酸アルキルエステル(E1)とモノアルコール(A1)とをエステル交換反応(R1)させ、得られた反応液から蒸留により目的とする(メタ)アクリル酸エステル(T1)を留出させて取得し、その際に得られるスズ化合物を含む蒸留残渣(C2)を触媒として原料の(メタ)アクリル酸アルキルエステル(E2)とモノアルコール(A2)とをエステル交換反応(R2)させ、目的とする(メタ)アクリル酸エステル(T2)を取得する(メタ)アクリル酸エステルの製造方法において、次の(1)〜(3)の特徴を有する(メタ)アクリル酸エステルの製造方法。
(1)前記エステル交換反応(R1)中の反応液に含まれる水分量を前記スズ化合物(C1)に含まれるスズ原子1モルに対して0.0001〜5モルにする。
(2)前記蒸留残渣(C2)に含まれる水分量を、前記エステル交換反応(R2)に使用するまでの期間、スズ原子1モルに対して0.02〜5モルにする。
(3)前記エステル交換反応(R2)中の反応液に含まれる水分量を前記蒸留残渣(C2)に含まれるスズ原子1モルに対して0.0001〜5モルにする。
[Claims]
1. A transesterification reaction (R1) between a raw material alkyl (meth) acrylate (E1) and a monoalcohol (A1) using a tin compound (C1) as a catalyst, and the reaction mixture obtained is subjected to distillation by distillation. The (meth) acrylic acid ester (T1) is distilled off and obtained, and the distillation residue (C2) containing a tin compound obtained at that time is used as a catalyst and the raw material (meth) acrylic acid alkyl ester (E2) is used as a catalyst. In the method for producing a (meth) acrylic acid ester, which obtains a desired (meth) acrylic acid ester (T2) by subjecting the alcohol (A2) to a transesterification reaction (R2), the following (1) to (3) A method for producing a (meth) acrylic acid ester having characteristics.
(1) The amount of water contained in the reaction solution in the transesterification reaction (R1) is set to 0.0001 to 5 mol per 1 mol of tin atom contained in the tin compound (C1).
(2) The amount of water contained in the distillation residue (C2) is adjusted to 0.02 to 5 mol with respect to 1 mol of tin atom until it is used in the transesterification reaction (R2).
(3) The amount of water contained in the reaction solution in the transesterification (R2) is set to 0.0001 to 5 mol per 1 mol of tin atoms contained in the distillation residue (C2).

JP2003007540A 2003-01-15 2003-01-15 Method for producing (meth) acrylic acid ester Expired - Lifetime JP4266645B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003007540A JP4266645B2 (en) 2003-01-15 2003-01-15 Method for producing (meth) acrylic acid ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003007540A JP4266645B2 (en) 2003-01-15 2003-01-15 Method for producing (meth) acrylic acid ester

Publications (3)

Publication Number Publication Date
JP2004217575A JP2004217575A (en) 2004-08-05
JP2004217575A5 true JP2004217575A5 (en) 2006-03-02
JP4266645B2 JP4266645B2 (en) 2009-05-20

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Family Applications (1)

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JP2003007540A Expired - Lifetime JP4266645B2 (en) 2003-01-15 2003-01-15 Method for producing (meth) acrylic acid ester

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JP (1) JP4266645B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4678753B2 (en) * 2004-07-14 2011-04-27 三菱レイヨン株式会社 Method for producing carboxylic acid ester
JP4838538B2 (en) * 2005-05-31 2011-12-14 三菱レイヨン株式会社 Method for producing unsaturated carboxylic acid ester and method for producing catalyst therefor
JP2008106019A (en) * 2006-10-27 2008-05-08 Mitsubishi Rayon Co Ltd Method for producing (meth)acrylic ester
FR2946046B1 (en) * 2009-05-26 2012-04-20 Arkema France COMPOSITION COMPRISING A DIALKYL TIN OXIDE AND ITS USE AS A TRANSESTERIFICATION CATALYST FOR THE SYNTHESIS OF (METH) ACRYLIC ESTERS.
CN102260128A (en) * 2010-05-25 2011-11-30 南京凯时通新材料有限公司 Process for preparing acrylate monomer and derivative thereof by using transesterification method

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