A kind of preparation method of side chain chlorine-containing polypropylene carbonate polyol
A technology of polypropylene carbonate and polyols, which is applied in the field of preparation of polypropylene carbonate polyols, can solve the problems of poor solvent resistance, flame retardancy, and poor bonding strength of polyurethane, and achieve Excellent solvent resistance, avoid wall hanging on the top of the kettle, and high bonding strength
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Embodiment 1
[0023] Open the carbon dioxide feed valve of the reactor, add carbon dioxide to the 6L reactor until the pressure in the reactor is 1.5 MPa, and close the carbon dioxide feed valve of the reactor. Open the propylene oxide metering pump, pour 2100g propylene oxide and 210g epichlorohydrin into the reactor; open the discharge valve of the initiator storage tank, and pour 100g dipropylene glycol into the reactor; the reactor is heated to 60 ℃, add carbon dioxide until the pressure in the reactor is 2.5MPa; put 100g of the liquid double metal cyanide catalyst prepared according to Example 1 of CN103865052A into the reactor, react at a constant temperature for 30h, and remove unreacted rings under vacuum at 0.1Pa-1KPa. Propylene oxide and epichlorohydrin, obtain 3751g side chain chlorine-containing polypropylene carbonate polyols, product molecular weight is 2480, hydroxyl value 45.1, chlorine element content 2.0%.
Embodiment 2
[0025] Open the carbon dioxide feed valve of the reactor, add carbon dioxide into the 6L reactor until the pressure in the reactor is 1.0 MPa, and close the carbon dioxide feed valve of the reactor. Open the propylene oxide metering pump, put 1800g propylene oxide and 500g epichlorohydrin into the reactor; Ether 360g; heat the reactor to 60°C, add carbon dioxide until the pressure inside the reactor is 2.5MPa; put 50g of the liquid double metal cyanide catalyst prepared according to Example 1 of CN103865052A into the reactor, react at constant temperature for 30h, 0.1Pa-1KPa The unreacted propylene oxide and epichlorohydrin were removed under vacuum to obtain 3850 g of side chain chlorine-containing polypropylene carbonate polyol, the product molecular weight was 3020, the hydroxyl value was 37, and the chlorine element content was 0.42%.
Embodiment 3
[0027] Open the carbon dioxide feed valve of the reactor, add carbon dioxide to the 6L reactor until the pressure in the reactor is 1.5 MPa, and close the carbon dioxide feed valve of the reactor. Open the propylene oxide metering pump, pour 1200g propylene oxide and 1200g epichlorohydrin into the reactor; open the discharge valve of the initiator storage tank, and pour 50g dipropylene glycol into the reactor; the reactor is heated to 60 ℃, add carbon dioxide until the pressure in the reactor is 2.0MPa; put 200g of liquid double metal cyanide catalyst prepared according to CN103865052A Example 1 into the reactor, react at constant temperature for 20h, and remove unreacted epoxy under 0.1Pa-1KPa vacuum Propane and epichlorohydrin obtain 3800g side chain chlorine-containing polypropylene carbonate polyols, the product molecular weight is 2040, the hydroxyl value is 54.9, and the chlorine element content is 11.5%.
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