Prepn of polyether-type polyurethane as shoe sole material
A polyether polyurethane and shoe sole material technology, applied in shoe soles, footwear, clothing and other directions, can solve the problems of weakened tensile strength, complex process, difficult processing, etc., and achieve improved mechanical properties, simple processing technology, and environment-friendly. Effect
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Embodiment 1
[0037] 1. Preparation of low unsaturation polyether polyol (I):
[0038]60g of polyoxypropylene triol (molecular weight is 700) starter and double metal cyanide complex catalyst (see the invention patent " double metal cyanide compound catalyst" applied by Kang Maoqing and Wang Xinkui in a 1 liter reactor with stirring) Its preparation method and application, the application number is 00122073.X) 0.0065g (catalyst content 25ppm in the final polyol).The mixture is stirred and heated to 105 ℃, vacuumize nitrogen bubble replacement to remove the trace amount in this initiator Water and oxygen in the reactor. When the reactor is filled with nitrogen to normal pressure, propylene oxide 15 is pre-cast to enter the "induction period" of the catalyst, and the pressure of the reactor is 3.0kg / cm 2 . Then pay attention to observe the pressure of the reactor. Catalyst activation is indicated when there is an accelerated pressure drop in the reactor - the end of the "induction period". ...
Embodiment 2
[0047] 1, low unsaturation polyether polyol (I) preparation, with embodiment 1.
[0048] 2. Preparation of high activity and low unsaturation polyether polyol (III)
[0049] 40g polyoxypropylene triol (molecular weight is 700) initiator and double metal cyanide complex catalyst (see the invention patent " double metal cyanide compound catalyst of Kang Maoqing, Wang Xinkui application) in 1 liter of band stirring reactor Its preparation method and application, the application number is 00122073.X) 0.0110g (catalyst content 25ppm in the final polyol).The mixture is stirred and heated to 110 ℃, vacuumize nitrogen bubble replacement to remove the trace amount in this initiator Water and oxygen in the reactor. When the reactor is filled with nitrogen to normal pressure, propylene oxide 18 is pre-cast to enter the "induction period" of the catalyst, and the pressure of the reactor is 3.2kg / cm 2 . Then pay attention to observe the pressure of the reactor. Catalyst activation is in...
Embodiment 3
[0056] 1, low unsaturation polyether polyol (I) preparation, with embodiment 1.
[0057] 2. Preparation of polyether polyol (II) with high activity and low degree of unsaturation. With embodiment 1.
[0058] 3. Preparation of polyether polyol (III) with high activity and low degree of unsaturation. With embodiment 2.
[0059] 4. Preparation of polyol mixture (component A)
[0060] 80 parts of high activity and low unsaturation polyether polyol (II), 10 parts of high activity and low unsaturation polyether polyol (III), 10 parts of polymer polyether polyol POP9328 (OHV=42-44mgKOH / g, solid content 28-30%, f=3, primary hydroxyl content 70-75%), 11 parts of 1,4-butanediol, 0.4 part of water, 1.8 parts of 33% (weight) triethylenediamine Dipropylene glycol solution, 0.5 parts of organosiloxane-polyether copolymer foam stabilizer (Dabco DC 3042 / 3043) from American Gas Chemical Company are fully mixed in the container for 2.0 hours, and the temperature is kept at 60-65 ° C. After...
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