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Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester

a technology of catalyst and polyester, which is applied in the direction of catalyst activation/preparation, organic compound/hydride/coordination complex catalyst, physical/chemical process catalyst, etc., can solve the problems of high production cost of polyester, inferior polycondensation of polyester produced by the use of antimony compound as a polycondensation catalyst, and high cost of germanium compound. , to achieve the effect of low acetaldehyde content, high catalytic activity and high quality

Inactive Publication Date: 2002-09-26
MITSUI CHEM INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the polyester produced by the use of the antimony compound as a polycondensation catalyst is inferior to the polyester produced by the use of a germanium compound as a polycondensation catalyst in the transparency and the heat resistance.
On the other hand, the germanium compound is considerably expensive, so that the production cost of polyester becomes high.
However, when the conventional titanium compounds are used as the polycondensation catalysts, their activity is inferior to that of the antimony compounds or the germanium compounds.
In addition, the resulting polyester has a problem of being markedly colored yellow, and hence they have not been put into practical use yet.
In the industrial production of polyesters using these titanium compounds as the polycondensation catalysts, further, there is a problem of corrosion caused by elution of chlorine content in case of catalysts containing a large amount of chlorine, such as titanium tetrachloride and partial hydrolyzate of titanium tetrachloride.
Therefore, catalysts having low chlorine content are sometimes desired.
As for the molded product obtained from the conventional polyester such as conventional polyethylene terephthalate, however, the content of acetaldehyde is increased during the molding and the acetaldehyde remains in the resulting molded product, so that flavor or scent of the contents filled in the molded product is sometimes considerably deteriorated.
However, the increase of the acetaldehyde content in the polyethylene terephthalate obtained by these processes cannot be lowered down below a certain level.
In this method, however, the phosphoric acid functions as an acid catalyst to perform hydrolysis, and as a result, decrease of the intrinsic viscosity is accelerated during the melt molding.
The stain of the mold causes surface roughening or whitening of the resulting blow molded article.
In the production of a blow molded article using the conventional polyester, the stain of the mold must be frequently removed, and this results in conspicuous lowering of productivity of the blow molded article.
In addition, the polyester obtained by the use of the antimony compound or the germanium compound as a polycondensation catalyst sometimes has low melt flowability and is insufficient in the moldability.

Method used

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  • Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester
  • Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester
  • Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester

Examples

Experimental program
Comparison scheme
Effect test

example 495-1

Preparation of Solid Titanium Compound

[0728] Deionized water of 500 ml was weighed out and introduced into a 1000 ml glass beaker. The deionized water in the beaker was cooled in an ice bath, and thereto was dropwise added 5 g of titanium tetrachloride with stirring. When production of hydrogen chloride stopped, the beaker containing the reaction solution was taken out of the ice bath, and 25% aqueous ammonia was dropwise added with stirring, to adjust pH of the solution to 8. The precipitate of titanium hydroxide produced was separated from the supernatant liquid by centrifugation of 2500 revolutions for 15 minutes. Then, the resulting titanium hydroxide precipitate was washed five times with deionized water. After the washing, solid-liquid separation was carried out by centrifugation of 2500 revolutions for 15 minutes. The washed titanium hydroxide was vacuum dried at 70.degree. C. under a pressure of 10 Torr for 18 hours to remove water content, whereby a solid titanium compound ...

example 495-2

Preparation of Titanium-Containing Solid Compound

[0732] Deionized water of 500 ml was weighed out and introduced into a 1000 ml glass beaker. To the deionized water, 0.15 g of anhydrous magnesium hydroxide was added to give a dispersion. The dispersion in the beaker was cooled in an ice bath, and thereto was dropwise added 5 g of titanium tetrachloride with stirring. The liquid became acidic, and the magnesium hydroxide was dissolved. When production of hydrogen chloride stopped, the beaker containing the reaction solution was taken out of the ice bath, and 25% aqueous ammonia was dropwise added with stirring, to adjust pH of the solution to 8. The precipitate of titanium-containing complex hydroxide produced was separated from the supernatant liquid by centrifugation of 2500 revolutions for 15 minutes. Then, the precipitate of titanium-containing complex hydroxide was washed five times with deionized water. After the washing, solid-liquid separation was carried out by centrifugatio...

example 495-3

Preparation of Titanium-Containing Solid Compound

[0734] Deionized water of 500 ml was weighed out and introduced into a 1000 ml glass beaker. To the deionized water, 0.16 g of colloidal silica (trade name: Snowtex OXS) was added to give a dispersion. The dispersion in the beaker was cooled in an ice bath, and thereto was dropwise added 5 g of titanium tetrachloride with stirring. The liquid became acidic, and the colloidal silica was dissolved. When production of hydrogen chloride stopped, the beaker containing the reaction solution was taken out of the ice bath, and 25% aqueous ammonia was dropwise added with stirring, to adjust pH of the solution to 8. The precipitate of titanium-containing complex hydroxide produced was separated from the supernatant liquid by centrifugation of 2500 revolutions for 15 minutes. Then, the precipitate of titanium-containing complex hydroxide was washed five times with deionized water. After the washing, solid-liquid separation was carried out by cen...

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Abstract

The present invention provides a catalyst or polyester production capable of producing a polyester with high catalytic activity and a process For producing a polyester using the catalyst. The catalyst for polyester production comprises a solid titanium compound which is obtained by dehydro-drying a hydrolyzate obtained by hydrolysis of a titanium halide and which has a molar ratio (OH / Ti) of a hydroxyl group (OH) to titanium (Ti) exceeding 0.09 and less than 4. The present invention also provides a method to obtain a polyester having a small increase of the acetaldehyde content during the molding. This method comprises bringing a polyester, which is obtained by the use of a titanium compound catalyst and in which the reaction has been completed, into contact with a phosphoric ester aqueous solution or the like having a concentration of not less than 10 ppm in terms of phosphorus atom. The present invention further provides a polyester having excellent transparency and tint and molded products of the polyester such as a blow molded article, arm, a sheet and a fiber. The polyester is obtained by polycondensing an aromatic dicarboxylic acid or an ester-forming derivative thereof and an aliphatic diol or an ester-forming derivative thereof in the presence of a catalyst for polyester production which comprises a polycondensation catalyst component comprising a solid titanium compound and a co-catalyst component comprising a magnesium compound. This polyester has a titanium content of 1 to 100 ppm, a magnesium content of 1 to 200 ppm and a weight ratio (Mg / Ti) of magnesium to titanium of not less than 0.01.

Description

[0001] The present invention relates to a catalyst for polyester production, a process for producing a polyester using the catalyst, a polyester obtained by the process and uses of the polyester.[0002] Because of their excellent mechanical strength, heat resistance, transparency and gas barrier properties, polyesters such as polyethylene terephthalate are favorably used as not only materials of containers of various beverages such as juice, soft drinks and carbonated beverages but also materials of films, sheets and fibers.[0003] The polyesters can be generally produced using, as starting materials, dicarboxylic acids such as aromatic dicarboxylic acids and diols such as aliphatic diols. In more detail, a dicarboxylic acid and a diol are first subjected to esterification reaction to form a low condensate (low molecular weight polyester), and the low condensate is then subjected to deglycolation reaction (liquid phase polycondensation) to increase the molecular weight. In some cases,...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C08G63/183C08G63/82C08G63/85C08G63/88
CPCC08G63/183C08G63/82C08G63/85C08G63/88
Inventor OHMATSUZAWA, TAKESHIEHARA, FUJITOHORI, HIDESHITOYOTA, KAZUOFUKUTANI, KENZABUROUIMUTA, JUNICHISHIMIZU, AKIVOSHIONOGI, TAKAYUKINODA, SEIJISAKAI, SAYUKIHIRAOKA, SHOJINAKAMACHI, KOJITSUGAWA, MICHIOMIYAZOE, SATORU
Owner MITSUI CHEM INC
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