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Process for production of polycarbonate diol diacrylate and high-purity polycarbonate diol diacrylate

A technology of polycarbonate diol diacrylate and polycarbonate diol, which is applied in the field of high-purity polycarbonate diol diacrylate, can solve problems such as ignorance, and achieve bridging density without reducing and inhibiting Excellent effect of exchange reaction, efficiency and safety

Inactive Publication Date: 2015-01-21
UBE IND LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there is no known example of acrylated polycarbonate diol as a substrate using lipase

Method used

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  • Process for production of polycarbonate diol diacrylate and high-purity polycarbonate diol diacrylate
  • Process for production of polycarbonate diol diacrylate and high-purity polycarbonate diol diacrylate
  • Process for production of polycarbonate diol diacrylate and high-purity polycarbonate diol diacrylate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0125] Acrylation of embodiment 1 polycarbonate diol

[0126] Add 5 mmol of vinyl acrylate to 1.0 g (0.5 mmol) of polycarbonate diol (UH200 manufactured by Ube Industries, (poly(hexamethylene carbonate)) diol: average molecular weight 2000 (polymerization degree 14.6)) and Toluene was added to 1 mg of p-methoxyphenol as a polymerization inhibitor, and the volume was fixed to 10 ml to prepare a reaction solution.

[0127] 2 ml of the above reaction solution and 20 mg of lipase immobilized in a resin porous body (Novozyme 435 (manufactured by Novozymes Co., Ltd.) derived from Candida antarctica (Candida antarctica) lipase) were added to a glass test tube, and stirred (1000 rpm) , and reacted at 70° C. for 24 hours.

[0128] After the reaction, the reaction solution was filtered with a filter with a pore size of 0.2 μm, and the solvent was distilled off from the filtrate under reduced pressure with a rotary evaporator, and the residue was dried in a desiccator at 60° C. under r...

Embodiment 5~7

[0136] Acrylation of embodiment 5~7 polycarbonate diol

[0137] To 3.0 g of polycarbonate diol shown in Table 2, vinyl methacrylate (1.35 g in Example 5 (UH100) and 1.35 g in Example 6 (UC100) and Example 7 (1.51 g in UM90 (1 / 1): polycarbonate diol with equimolar residues of 1,6-hexanediol and 1,4-cyclohexanedimethanol)) and as a polymerization inhibitor Toluene was added to 1 mg of p-methoxyphenol as the solvent, and the volume was fixed to 10 ml to prepare a reaction solution.

[0138] 2 ml of each reaction solution and 5 mg of lipase (Novozyme 435) were added to a glass test tube, and reacted for the time shown in Table 2 at 70° C. under stirring (1000 rpm).

[0139] After the completion of the reaction, each reaction liquid was filtered with a 0.2 μm filter, and the solvent was distilled off under reduced pressure with a rotary evaporator for each filtrate, and each residue was dried in a desiccator at 60° C. under reduced pressure for 2 hours to obtain each polycarbona...

Embodiment 8~10

[0145] Examples 8-10: Propylene based on polycarbonate diol for continuous reaction using immobilized enzyme Esterification

[0146] Add 67.5g of vinyl methacrylate and 0.05g of p-methoxyphenol as a polymerization inhibitor to 150g of polycarbonate diol (UH100, refer to Table 2), add toluene to it, and after the volume is set to 500ml, it is prepared The reaction solution.

[0147] 0.42 g of immobilized lipase (Novozyme 435) was filled in a glass column (a glass filter with an inner diameter of 5 mm × 50 mm and a pore size of 5 μm), kept at 70° C., and the reaction solution was delivered from below at the flow rate shown in Table 4 by a quantitative pump.

[0148] The reaction solution was fractionated according to the time shown in Table 4, and the solvent was distilled off the obtained reaction solution under reduced pressure with a rotary evaporator, and the residue was dried in a desiccator at 60° C. under reduced pressure for 2 hours, and supplied to 1 H-NMR analysis...

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Abstract

This is to provide a process for preparing a polycarbonate diol diacrylate from a polycarbonate diol and a vinyl acrylate compound without using a protonic acid or a metal component. This is a process for preparing a polycarbonate diol diacrylate which comprises reacting a polycarbonate diol represented by the formula (I) and a vinyl acrylate compound represented by the formula (II) in the presence of a hydrolase, and a polycarbonate diol diacrylate represented by the formula (III) having a terminal acrylated ratio of 97% or more.

Description

technical field [0001] The invention relates to a method for producing polycarbonate diol diacrylate. Furthermore, the invention relates to highly pure polycarbonate diol diacrylates. Background technique [0002] Polycarbonate diol diacrylate is a compound useful as a raw material for inks, paints, coating materials, adhesives, photocurable resins, crosslinking agents, electrolyte materials, and other resins. For example, Patent Document 1 discloses a film-shaped optical waveguide using polycarbonate diol diacrylate. [0003] As a method for producing polycarbonate diol diacrylate, a method of reacting polycarbonate diol and acrylic acid in the presence of a protonic acid catalyst such as p-toluenesulfonic acid is known (for example, refer to Patent Document 2). [0004] However, in this method, there is a big problem that the obtained polycarbonate diol diacrylate is colored brown, which affects the quality of the product. Furthermore, in this method, there is a problem...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08G64/42C12P7/62C12N9/20
CPCC08G64/42C08G64/0291C12P7/62C08G64/045C12N9/20
Inventor 吉田洋一山本康仁弘津健二
Owner UBE IND LTD