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Extrusion blow molded pet resin and preparation method thereof

A technology of resin and ethylene glycol, which is applied in the field of PET resin, can solve the problems of inability to extrude and blown into film and low melt strength of PET, and achieve the effects of low production equipment, long film making cycle and improved melt strength

Active Publication Date: 2022-07-05
浙江凯普奇新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This technical solution adopts biaxial stretching to prepare highly transparent antistatic film. Because of the low melt strength of traditional PET, it cannot be extruded and blown into film.

Method used

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  • Extrusion blow molded pet resin and preparation method thereof
  • Extrusion blow molded pet resin and preparation method thereof
  • Extrusion blow molded pet resin and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] The components of the extrusion blow-molded PET resin include: a molar ratio of terephthalic acid: ethylene glycol of 1:1.25, a total of 22 kg, 20 g of dipentaerythritol, 2 g of a titanium-based catalyst, and 10 g of a phosphoric acid ethylene glycol solution.

[0031] The preparation method of the PET resin of extrusion blow molding comprises the following steps:

[0032] Esterification stage: add the components of PET resin to a 50L reactor, beat at 300KPa and 80°C for 10min, then heat up to 240°C for esterification reaction for 2h, after the end of esterification, slowly release the pressure to react The pressure in the kettle drops to normal pressure;

[0033] Prepolymerization stage: vacuumize the reactor, reduce the pressure in the reactor from normal pressure to 1KPa, and raise the temperature of the reactor to 260°C;

[0034] Polycondensation stage: continue to vacuum the reaction kettle to 80Pa, react for 60min, discharge and cut into pellets;

[0035] Thicke...

Embodiment 2

[0037] The components of the extrusion blow molded PET resin include: the molar ratio of terephthalic acid: ethylene glycol is 1:1.25, a total of 22kg, sorbitol 23g, Sb 2 O 3 4.2g, 42g of ethylene glycol solution of phosphoric acid.

[0038] The preparation method of the PET resin of extrusion blow molding comprises the following steps:

[0039] Esterification stage: add the components of PET resin into a 50L reaction kettle, beat at 250KPa and 70°C for 10min, then heat up to 240°C for esterification for 1.5h. The pressure in the reactor is reduced to normal pressure;

[0040] Prepolymerization stage: vacuumize the reactor, reduce the pressure in the reactor from normal pressure to 1.0KPa, and raise the temperature of the reactor to 260°C;

[0041] Polycondensation stage: continue to vacuumize the reactor to 50Pa, react for 60min, discharge and cut into pellets;

[0042] Thickening stage: put the obtained pellets into a solid-phase viscosity increasing reactor, and react ...

Embodiment 3

[0044] The components of the extrusion blow molded PET resin include: the molar ratio of terephthalic acid: ethylene glycol is 1:1.25, a total of 22kg, tetraol 13.7g, Sb2 O 3 4.2g, 42g of ethylene glycol solution of phosphoric acid.

[0045] The preparation method of the PET resin of extrusion blow molding comprises the following steps:

[0046] Esterification stage: add the components of PET resin to a 50L reactor, beat at 350KPa and 90°C for 15min, then heat up to 245°C for esterification reaction for 3h, after the end of the esterification, slowly release the pressure, and the reaction The pressure in the kettle is reduced to normal pressure;

[0047] Prepolymerization stage: vacuumize the reactor, reduce the pressure in the reactor from normal pressure to 1.1KPa, and raise the temperature of the reactor to 265°C;

[0048] Polycondensation stage: continue to vacuum the reaction kettle to 80Pa, react for 50min, discharge and cut into pellets;

[0049] Thickening stage: p...

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Abstract

The invention discloses an extrusion blow molding PET resin, which is characterized by comprising the following components: aromatic dibasic acid, aliphatic diol, third monomer polyol, catalyst, toner and stabilizer, Wherein the molar ratio of aromatic dibasic acid: aliphatic diol is 1:1~2, the addition amount of the third monomer polyol is 300~1000ppm of the molar weight of aliphatic diol; the addition amount of catalyst is aromatic 180-290 ppm of the weight of the family dibasic acid; the added amount of the stabilizer is 5-20 times the weight of the catalyst. The invention also discloses a preparation method of the extrusion blow molding PET resin. The improvement of the intrinsic viscosity of the PET resin and the reduction of the melt index MFR of the present invention greatly improve the strength of the PET resin in the molten state, so as to meet the requirements of extrusion blow molding. film requirements.

Description

technical field [0001] The invention relates to PET resin, in particular to an extrusion blow-molded PET resin and a preparation method thereof. Background technique [0002] Compared with other packaging materials, PET has excellent barrier properties, which gives it a natural advantage in packaging, especially in food packaging. And PET is non-toxic, harmless, easy to recycle and environmentally friendly, so it has been widely used in the market. [0003] At present, the PET packaging film is mainly biaxially stretched BOPET film, that is, ordinary PET is used. Ordinary PET has no strength in the molten state, so biaxial stretching must be used in the high elastic state, but the production of biaxial stretching The investment cost of equipment is high (from tens of millions to hundreds of millions), and the cycle of film making is long, resulting in a high price. [0004] For example, Patent No. ZL200810060021.7 (Announcement No. CN101235191B) discloses a special materia...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08G63/20C08G63/668C08G63/85C08G63/86
CPCC08G63/20C08G63/668C08G63/85C08G63/866
Inventor 郑兵刘青松肖海军沈志刚蒲新明章延举邱增明
Owner 浙江凯普奇新材料科技有限公司