A kind of polyurethane filling material with high water content and low heat generation for coal mine and its preparation method
A filling material and low heat generation technology, which is applied in the field of high water content and low heat generation polyurethane filling material for coal mines and its preparation field, can solve the problems of insufficient compressive strength, high foaming temperature, pollute the environment, etc., and can achieve adjustable foaming ratio , the effect of strong permeability and low viscosity
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Embodiment 1
[0032] Component A selects polyether polyol 220A: 350kg and 330N: 500kg; polyester polyol 3152: 200kg; triethanolamine: 100kg; amine catalyst triethylenediamine: 1.5kg; organometallic catalyst T-12: 0.6kg ; plasticizer dibutyl phthalate 5kg; flame retardant TCEP: 150kg and DMMP: 50kg; emulsifier phenylethylphenol polyoxyethylene ether: 5kg; physical foaming agent 141B: 200kg; chemical foaming agent water : 20kg; water: 300kg. Add each monomer material into the reaction kettle in turn, and mix for 2.5 hours at a temperature of 25° C. and a stirring speed of 100 r / min to obtain a combined material.
[0033] Component B is polymethylene polyphenylisocyanate PM200: 700kg, PM400: 300kg and dichloromethane: 50kg; acetate: 50kg from Yantai Wanhua Polyurethane Co., Ltd. The monomer materials were sequentially added into the reactor, and mixed for 2.5 hours at a temperature of 25° C. and a stirring speed of 100 r / min to obtain a combined material.
[0034] Mix components A and B with...
Embodiment 2
[0036] Component A: polyether polyol 210: 300kg and 330N: 400kg; polyester polyol AK-POL-3002: 200kg; flame retardant polyether polyol FR-7190: 100kg; triethanolamine: 80kg; amine catalyst triethylene Diamine: 1.0kg; organometallic catalyst T-12: 0.8kg; plasticizer dibutyl phthalate: 5kg; flame retardant TCEP: 150kg and TEP: 80kg; antistatic agent emulsifier phenethylphenol Polyoxyethylene ether: 10kg; physical blowing agent: 150kg; water: 150kg. The monomer materials were sequentially added into the reactor, and the combined materials obtained were mixed for 2.5 hours at a temperature of 15° C. and a stirring speed of 200 r / min.
[0037] Component B is polymethylene polyphenyl isocyanate PM200: 800kg, PM400: 200kg and acetate: 50kg from Yantai Wanhua Polyurethane Co., Ltd. The monomer materials were sequentially added into the reactor, and the combined materials obtained were mixed for 1.5 hours at a temperature of 30° C. and a stirring speed of 300 r / min.
[0038] Mix comp...
Embodiment 3
[0040] Component A takes polyether polyol 210: 150kg, 220A: 210kg and 330N: 440kg; polyester polyol AK-POL-3002: 100kg; flame-retardant polyether polyol FR-7190: 100kg; triethanolamine: 85kg; Catalyst triethylenediamine: 2.5kg; organometallic catalyst T-12: 0.6kg; flame retardant TCPP: 170kg and DMMP: 50kg; emulsifier phenylethylphenol polyoxyethylene ether: 15kg; physical blowing agent: 50kg; chemical blowing agent: 180kg; water: 150kg. The monomer materials were sequentially added into the reactor, and the combined materials obtained were mixed for 3 hours at a temperature of 20° C. and a stirring speed of 250 r / min.
[0041] Component B is polymethylene polyphenylisocyanate PM200: 750kg, PM400: 250kg and acetate: 50kg from Yantai Wanhua Polyurethane Co., Ltd. The monomer materials were sequentially added into the reactor, and mixed at a temperature of 25° C. and a stirring speed of 240 r / min for 1.5 hours to obtain a combined material.
[0042] Mix components A and B at h...
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