A kind of wet process polyurethane resin with high astringency feeling and preparation method thereof
A wet-process polyurethane and astringent technology, which is applied in the field of high-astringency wet-process polyurethane resin and its preparation, can solve the problems of poor water absorption of synthetic rubber, slippery grip, poor hydrolysis resistance, etc., and achieves good hydrolysis resistance and improved water absorption. Good effect of sex and hydrophilicity
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Embodiment 1
[0030] A component:
[0031] Diphenylmethane-4,4-diisocyanate 5kg;
[0032] Polyoxypropylene diol (number average molecular weight 3000g / mol) 95kg;
[0033] B component:
[0034]
[0035] 1) Preparation of component A: Put 95kg of polyoxypropylene glycol and 5kg of MDI into the reaction kettle, and the reaction temperature is 100-120°C. After 3-4 hours of reaction in an inert gas atmosphere, it is measured that the NCO of the system is zero. Material, namely get A component.
[0036] 2) Preparation of component B: Prepolymerize 118kg of polytetrahydrofuran diol, 59kg of polyadipate polyester diol, 18.68kg of MDI and 347kg of DMF at a reaction temperature of 75-85°C for 2-4 hours. When the viscosity reaches 50°C, after 200-220Pa·s, put in 13.92kg of ethylene glycol, 17.7kg of polyoxyethylene glycol, 395kg of DMF, stir evenly and put in 54.4kg of MDI, control the reaction temperature at 75-85°C, and react for 1-2 hours , add the remaining amount of MDI in batches, and rea...
Embodiment 2
[0039] A component:
[0040] Diphenylmethane-4,4-diisocyanate 1.53kg;
[0041] Polyoxypropylene diol (number average molecular weight 4000g / mol) 49kg;
[0042] B component:
[0043]
[0044]
[0045] 1) Preparation of component A: Put 49kg of polyoxypropylene glycol and 1.53kg of MDI into the reactor, the reaction temperature is 100-120°C, and the reaction is carried out in an inert gas atmosphere for 3-4 hours, and the NCO of the system is measured to be zero. The material is discharged, and the A component is obtained.
[0046] 2) Preparation of component B: Prepolymerize 100kg of polytetrahydrofuran diol, 100kg of polyadipate polyester diol, 21.5kg of MDI and 275kg of DMF at a reaction temperature of 75-85°C for 2-4 hours. When the viscosity reaches 50°C, after 240-260Pa·s, put in 13.42kg of ethylene glycol, 25kg of polyoxyethylene glycol, 416kg of DMF, stir well and put in 54.3kg of MDI, control the reaction temperature at 75-85°C, and react for 1-2 hours. Add th...
Embodiment 3
[0049] A component:
[0050] Diphenylmethane-4,4-diisocyanate 4.875kg;
[0051] Polyoxypropylene diol (number average molecular weight 2000g / mol) 65kg;
[0052] B component:
[0053]
[0054] 1) Preparation of component A: Put 65kg of polyoxypropylene glycol and 4.875kg of MDI into the reactor, the reaction temperature is 100-120°C, and the reaction is carried out in an inert gas atmosphere for 3-4 hours, and the NCO of the system is measured to be zero. The material is discharged, and the A component is obtained.
[0055] 2) Preparation of component B: Prepolymerize 132kg of polytetrahydrofuran diol, 88kg of polyadipate polyester diol, 21.1kg of MDI and 393kg of DMF at a reaction temperature of 75-85°C for 2-4 hours. When the viscosity of the liquid reaches 50°C, after 200-220Pa·s, put in 13.8kg of ethylene glycol, 24.4kg of polyoxyethylene glycol, 329kg of DMF, stir evenly and put in 54kg of MDI, control the reaction temperature at 75-85°C, and react for 1-2 hours , add...
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