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Preparation method of polyether polyol for rapid demoulding rigid polyurethane foams

A polyurethane rigid foam and polyether polyol technology, which is applied in the field of polyether polyol synthesis, can solve the problems of increasing production costs, short mold opening time, and affecting foam fluidity, so as to save energy, reduce usage, and reduce odor Effect

Inactive Publication Date: 2015-10-07
SHANDONG INOV NEW MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In polyurethane industrial products, different varieties have different requirements for the molecular weight, functionality and activity of the raw material polyether polyol. In the production of polyurethane flexible foam, the polyether polyol is generally required to have a functionality of 3 and a molecular weight of 3000. Even higher, and in order to shorten the mold opening time and reduce the mold temperature to save energy in polyurethane molded flexible foam products, it is often required to use polyether polyols with high activity, that is, high primary hydroxyl content, and the primary hydroxyl content is 70%. Above, the production process of cold molding requires more active polyether polyols. The primary hydroxyl content of the most commonly used high-primary hydroxyl polyether polyols is 75-80%; for the production of polyurethane rigid foam, polyether polyols are generally required. The functionality of alcohol is greater than 4, and the molecular weight is about 400-700. In order to improve production efficiency and save energy, various manufacturers also require a short mold opening time in the production process. At present, polyether polyols generally use high functionality, high The polyether system with hydroxyl value, even with the amine ether with special amines as the initiator, will not only affect the fluidity of the foam but also increase the production cost by using amine ether, while the use of primary hydroxyl groups in the production of flexible foam There are few reports on the patented technology of high-end highly active polyether

Method used

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  • Preparation method of polyether polyol for rapid demoulding rigid polyurethane foams

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Add solid sorbitol 182g, trimethylolpropane 122g, triethanolamine 122g, 33% trimethylamine aqueous solution 2.34g in the autoclave that agitator, meter, heating temperature control device, cooling unit and pressure transducer are housed, DMP-305.48g, 5 times of nitrogen replacement, stirring 968gPO into the reactor continuously when the temperature is raised to 100°C, the reaction temperature is controlled at 105-115°C, the reaction pressure is controlled at 0.1-0.3Mpa, and the reaction is performed until the pressure does not change. Continue aging under internal pressure for 1 hour, then add 171g of EO dropwise continuously when the temperature rises to 120°C, control the reaction temperature at 120-130°C, and control the reaction pressure at 0.15-0.3Mpa. Under the condition of ℃ and vacuum degree of -0.1Mpa, carry out the vacuum-pumping and monomer-removing drying reaction for 1 hour to obtain the polyether polyol for rapid demoulding polyurethane rigid foam.

[0022...

Embodiment 2

[0029] Add solid sorbitol 182g, trimethylolpropane 91g, triethanolamine 91g, 5.54g of trimethylamine aqueous solution 5.54g of 40% in the autoclave that agitator, meter, heating temperature control unit, cooling unit and pressure transducer are housed, DMP-308.3g, nitrogen replacement 7 times, stirring 816gPO into the reactor continuously when the temperature is raised to 100°C, the reaction temperature is controlled at 105-115°C, the reaction pressure is controlled at 0.1-0.3Mpa, and the reaction is performed until the pressure does not change. Continue the internal pressure aging for 1.5h, then add 204g of EO dropwise continuously when the temperature rises to 120°C, control the reaction temperature at 120-130°C, and control the reaction pressure at 0.15-0.3Mpa. Under the condition of 100°C and vacuum degree of -0.12Mpa, carry out the vacuum-pumping and monomer-removing drying reaction for 2 hours to obtain the polyether polyol for rapid mold release polyurethane rigid foam. ...

Embodiment 3

[0037] Add solid sorbitol 182g, trimethylolpropane 72g, triethanolamine 72g, 50% trimethylamine aqueous solution 5.08g in the autoclave that agitator, meter, heating temperature control unit, cooling unit and pressure sensor are housed, DMP-305.08g, nitrogen replacement 8 times, when the temperature is raised to 100°C with stirring, 709gPO is continuously added dropwise into the reactor, the reaction temperature is controlled at 105-115°C, the reaction pressure is controlled at 0.1-0.3Mpa, and the reaction is performed until the pressure does not change. Continue aging under internal pressure for 1 hour, then add 236g of EO dropwise continuously when the temperature rises to 120°C, control the reaction temperature at 120-130°C, and control the reaction pressure at 0.15-0.3Mpa. Under the condition of ℃ and vacuum degree of -0.10Mpa, carry out the vacuum pumping and monomer removal drying reaction for 1.5h to obtain the polyether polyol for rapid release polyurethane rigid foam. ...

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Abstract

Belonging to the technical field of polyether polyol synthesis, the invention specifically relates to a preparation method of polyether polyol for rapid demoulding rigid polyurethane foams. The method includes: taking solid sorbitol, trimethylolpropane and triethanolamine as the composite initiator, adopting a compounded system of a trimethylamine aqueous solution and DMP-30 as the catalyst, adding oxyalkylene to carry out polymerization and end capping reaction, and finally carrying out demonomerization and drying to obtain the polyether polyol for rapid demoulding rigid polyurethane foams. The polyether polyol prepared by the method provided by the invention has higher flowability, strength and dimensional stability, the rigid foam composite material prepared therefrom and isocyanate react to generate foams with the characteristics of fast curing and short demoulding time, thus greatly improving the production efficiency and saving energy. And compared with existing amidogen ether system composite materials using a special amine initiator, the cost is lower, thereby meeting the high standard requirements of energy saving, consumption reduction, and environmental protection.

Description

technical field [0001] The invention belongs to the technical field of polyether polyol synthesis, and in particular relates to a preparation method of polyether polyol for rapid release polyurethane rigid foam. Background technique [0002] Polyether polyol is one of the main raw materials of the polyurethane industry, which can be used in the manufacture of automotive interiors, medical equipment, furniture, home appliances, coatings, shoe leather and other fields. In polyurethane industrial products, different varieties have different requirements for the molecular weight, functionality and activity of the raw material polyether polyol. In the production of polyurethane flexible foam, the polyether polyol is generally required to have a functionality of 3 and a molecular weight of 3000. Even higher, and in order to shorten the mold opening time and reduce the mold temperature to save energy in polyurethane molded flexible foam products, it is often required to use polyeth...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G65/28C08G18/50C08G101/00
Inventor 刘军念以亭马海晶宁晓龙凌贞贞
Owner SHANDONG INOV NEW MATERIALS CO LTD