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Transesterification process for production of (meth)acrylate ester monomers

A technology of alkyl acrylate and transesterification, which is used in catalyst activation/preparation, reaction preparation of ester groups and hydroxyl groups, chemical instruments and methods, etc., and can solve problems such as catalysts failing to function.

Inactive Publication Date: 2011-08-03
ROHM & HAAS CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Catalysts are not effective when the reaction mixture contains a large amount of water

Method used

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  • Transesterification process for production of (meth)acrylate ester monomers
  • Transesterification process for production of (meth)acrylate ester monomers
  • Transesterification process for production of (meth)acrylate ester monomers

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0062] Example 1 describes a single one-shot mixed salt transesterification catalyst capable of producing the desired product even when the dehydration step used to reduce the water content of the reaction mixture is omitted.

[0063] Add the mixture of the following components into the equipment equipped with temperature display / temperature controller, magnetic stirrer, mixed gas (8% O 2 to 92%N 2 ) injection inlet, 1 inch diameter 10-plate Oldershaw column equipped with distillation head, proportional removal of distillate-vapor pressure thermostat and stepwise distillate receiver in a 2-liter 4-neck flask: 260.3 grams (2.0 moles ) 1-hydroxyethylene urea (HEEU), 680.8 g (6.8 moles) methyl methacrylate (MMA), 1.0 g (0.006 moles) 4-hydroxy-2,2,6,6-tetramethylpiperidine Oxygen radical (4-hydroxy TEMPO, free radical), 2.77 grams (0.02 mole) of potassium carbonate and 1.49 grams (0.02 mole) of potassium chloride. The mixture was then heated (at a rate of 2.3°C / min) to 98°C whil...

Embodiment 2

[0065] Example 2 demonstrates the re-use of used recovered catalyst in subsequent reactions.

[0066] Add the mixture of the following components into the equipment equipped with temperature display / temperature controller, magnetic stirrer, mixed gas (8% O 2 to 92%N 2 ) injection inlet, 1 inch diameter 10-plate Oldershaw column with distillation head, distillation rate of distillate-vapor pressure thermostat and stepwise distillate receiver in a 2-liter 4-neck flask: 260.3 grams (2.0 moles) 1-hydroxyethyleneurea (HEEU), 680.8 grams (6.8 moles) methyl methacrylate (MMA), 1.0 grams (0.006 moles) 4-hydroxy-2,2,6,6-tetramethyl piperidinyloxy radical (4-hydroxy TEMPO, free radical), 2.77 grams (0.02 moles) of potassium carbonate and 1.49 grams (0.02 moles) of potassium chloride. The mixture was then heated (at a rate of 2.3°C / min) to 98°C while removing the reaction azeotrope MMA-methanol. During the reaction, the mixture was stirred, sprayed with a mixed gas, and continuously h...

Embodiment 3

[0068] Example 3 shows how the above heterogeneous catalyst system prepares MEEU with a lower ratio of MMA:HEEU (3.2:1).

[0069] Add the mixture of the following components into the equipment equipped with temperature display / temperature controller, magnetic stirrer, mixed gas (8% O 2 to 92%N 2 ) injection inlet, 1 inch diameter 10-plate Oldershaw column equipped with distillation head, distillation rate of distillate-vapor pressure thermostat and step-by-step distillate receiver in a 2-liter 4-neck flask: 260.3 g ( 2.0 moles) 1-hydroxyethyleneurea (HEEU), 640.5 grams (6.4 moles) methyl methacrylate (MMA), 1.0 grams (0.006 moles) 4-hydroxy-2,2,6,6-tetramethyl Piperidinyloxy radical (4-hydroxy TEMPO, free radical). The mixture was then heated (at a rate of 2.3°C / min) to 98°C while removing the reaction azeotrope MMA-methanol. During the reaction, the mixture was stirred, sprayed with a mixed gas, and continuously heated to reflux under a vacuum of 700 mm Hg, while removing ...

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Abstract

This invention utilizes a mixed salt transesterification catalyst in a transesterification process for the production of esters of alkyl (meth)acrylate monomers.

Description

technical field [0001] The present invention relates to a transesterification process for the preparation of (meth)acrylate monomers from alkyl (meth)acrylates and alcohols. More specifically, the present invention is an improved transesterification process comprising adding a mixed salt catalyst for transesterification during the reaction. Background technique [0002] Herein, the term "(meth)" followed by another term such as acrylate means both acrylate and methacrylate. For example, the term "(meth)acrylate" means acrylate or methacrylate; the term "(meth)acrylic" means acrylic or methacrylic; the term "(meth)acrylic" means acrylic or methacrylic base acrylic. [0003] (Meth) acrylates can be converted into an azeotropic mixture with alkyl (meth)acrylates by transesterification reaction of alkyl (meth)acrylates with selected alcohols in the presence of a transesterification catalyst. form to remove the existing by-product low boiling point alcohols. [0004] More spe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C69/533B01J27/232C07C67/03B01J27/08C07D233/34
CPCB01J35/0006B01J27/232B01J27/10C07C67/03C07D233/32B01J37/04Y02P20/582B01J35/19C07C69/54C07C69/653
Inventor A·本德利M·R·瑞安D·R·威勒
Owner ROHM & HAAS CO