Preparation method of rigid foam flame-retardant polyether polyol for all-water foaming

A technology of all-water foaming and flame-retardant polyether, which is applied in the field of polyurethane synthesis, can solve the problems of weak cohesive force, complex manufacturing process, and poor flame-retardant effect of the thermal insulation system, and achieve good thermal insulation and flame-retardant effects and excellent construction technology. The effect of simplicity and broad application prospects

Active Publication Date: 2020-01-03
BEFAR GROUP CO LTD +1
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the rigid foam polyether polyol synthesis process in the prior art has the following disadvantages: (1) the full water foamed rigid polyether polyol product prepared by this process has large viscosity, high hydroxyl value, and the full water foam In the polyether composite material, because there are no physical blowing agents such as CFC and HCFC that can be used as diluents, the viscosity of the compound composite material is high, and the mold filling property is poor when processing foam products; (2) rigid foam polyether in the prior art Ether polyol is when carrying out all-water foaming, and the speed that foaming gas carbon dioxide diffuses outwards from foam hole is 1.0 times faster than the speed that air enters foam hole, causes foam shrinkage, collapses easily; (3) in the prior art When the rigid foam polyether polyol is fully water-foamed, due to the large amount of water used, it reacts with isocyanate to form more urea bonds, resulting in brittle foam and weak adhesion to the insulation system; (4) The rigid polyether polyols used for full water foaming in the existing technology have the disadvantage of poor flame retardant effect, and mainly rely on the addition of non-reactive small molecule flame retardants containing halogens, phosphorus, and inorganic salts to improve the flame retardant properties of materials. Flame retardant performance, however, externally added non-reactive flame retardants have disadvantages such as poor storage stability in the composite material, affecting the strength of the product, and easy migration out of the product; (5) full water foaming in the prior art Using rigid polyether polyol, the production process is complicated and the cost is high, so its market share is very low, and it has encountered great resistance in the process of actual promotion and application

Method used

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  • Preparation method of rigid foam flame-retardant polyether polyol for all-water foaming
  • Preparation method of rigid foam flame-retardant polyether polyol for all-water foaming

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] In a 5L autoclave equipped with a stirrer, a meter, a heating temperature control device, a cooling device (including an outer jacket and an inner coil) and a pressure sensor, add 342 g of sucrose, 30 g of bromoneopentyl glycol, and 20 g of diethylene glycol , propylene glycol 30g, phenolic resin 22g, palm oil 225g, potassium hydroxide 7g, nitrogen replacement 3 times, heat up and turn on the vacuum pump, carry out vacuum dehydration at 100-105°C for 3 hours, then cool down to 80°C, and start adding propylene oxide dropwise , by controlling the feeding speed of propylene oxide and the temperature control device, the reaction temperature in the kettle is maintained at 80-110°C, and the pressure is in the range of 0.1-0.4MPa. When the propylene oxide is added to 1200g, then add propylene oxide and ring The mixture of oxyethane is 300g (propylene oxide 180g, ethylene oxide 120g), the temperature is 80-110°C and the pressure inside the kettle is controlled at 0.1-0.4MPa, aft...

Embodiment 2

[0034] In a 5L autoclave equipped with a stirrer, a meter, a heating temperature control device, a cooling device (including an outer jacket and an inner coil) and a pressure sensor, add 342 g of sucrose, 30 g of bromoneopentyl glycol, and 20 g of diethylene glycol , propylene glycol 30g, palm oil 225g, potassium hydroxide 7g, nitrogen replacement 3 times, heat up and turn on the vacuum pump to carry out vacuum dehydration at 100-105°C for 3 hours, then cool down to 80°C, start to drop propylene oxide continuously, through the control ring The feeding speed of propylene oxide and the temperature control device keep the reaction temperature in the kettle at 80-110°C, and the pressure is in the range of 0.1-0.4MPa, until the propylene oxide is added to 1200g, then add the mixture of propylene oxide and ethylene oxide. 300g of the mixture (180g of propylene oxide, 120g of ethylene oxide), the temperature is 80-110°C and the pressure inside the kettle is controlled at 0.1-0.4MPa. A...

Embodiment 3

[0037] In a 5L autoclave equipped with a stirrer, a meter, a heating temperature control device, a cooling device (including an outer jacket and an inner coil) and a pressure sensor, add 342 g of sucrose, 30 g of bromoneopentyl glycol, and 20 g of diethylene glycol , propylene glycol 30g, phenolic resin 22g, palm oil 225g, potassium hydroxide 7g, nitrogen replacement 3 times, heat up and turn on the vacuum pump, carry out vacuum dehydration at 100-105°C for 3 hours, then cool down to 80°C, and start adding propylene oxide dropwise , by controlling the feeding speed of propylene oxide and the temperature control device, the reaction temperature in the kettle is maintained at 80-110°C, and the pressure is in the range of 0.1-0.4MPa until the propylene oxide is added to 1500g. After the feeding is completed, the reaction is matured for 3 Hour. Adding water and acid to the matured product, adding an adsorbent, dehydrating and degassing in a vacuum, and press-filtering to obtain fu...

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Abstract

The invention belongs to the technical field of polyurethane synthesis, and in particular relates to a preparation method of a rigid foam flame-retardant polyether polyol for all-water foaming. The preparation method uses sucrose, a low-molecular-weight polyol, a halogenated alcohol, phenolic resin, and oil as initiators, and uses an alkali metal salt as a catalyst, and a section of propylene oxide is introduced for carrying out a reaction; and after the reaction is completed, a mixture of propylene oxide and ethylene oxide is introduced for carrying out a mixed polymerization reaction, and acrude ether is purified by post-treatment to obtain a finished product. The technological process is simple in operation, the obtained rigid foam flame-retardant polyether product for all-water foaming has low viscosity and good compatibility with water, a polyurethane foam plastic product prepared from the polyether product has relatively narrow density distribution, relatively high strength, good dimensional stability and bonding strength, and relatively low thermal conductivity, has certain flame-retardant effects, and is especially suitable for all-water foamed thermal insulation pipes andother thermal insulation fields.

Description

technical field [0001] The invention belongs to the technical field of polyurethane synthesis, and in particular relates to a preparation method of rigid foam flame-retardant polyether polyol for all-water foaming. Background technique [0002] In the prior art, various foaming agents are used for foaming rigid polyether polyols. At present, CFC systems are mostly used as foaming agents, among which HCFC-141B is the main one, and some even use Freon-11, which is banned by the state. etc., but this type of blowing agent is not friendly to the environment and brings certain environmental hazards. In recent years, many units or individuals have developed some all-water rigid polyether polyols, replacing the foaming agent with water. The technology of all-water foamed rigid polyether polyols uses carbon dioxide generated by the reaction of water and isocyanate as the foaming gas. The ODP (Ozone Depletion Potential) is zero, and the GWP (Greenhouse Gas Effect) is 1, which is fri...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G65/26C08G18/48C08J9/08C08G101/00
CPCC08G65/2612C08G65/2609C08G65/2639C08G65/2648C08G18/4837C08G2110/0083C08G2110/0025
Inventor 李海峰张宝银吕兴连张坤魏学福米新强周小光付文辉
Owner BEFAR GROUP CO LTD
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