Foamed plastic for low-density and high-flame-retardant continuous slab and preparation method for foamed plastic
A foam plastic and high flame-retardant technology, which is applied in the field of low-density high flame-retardant continuous board foam plastic and its preparation, can solve the problems of insufficient reaction of raw materials, high injection density, low foam strength, etc., and achieve low production cost , simple process, low thermal conductivity effect
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Embodiment 1
[0038] Preparation of polyether polyol A:
[0039] In a 2.5L 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 342g of sucrose, 39.5g of pentaerythritol, 3.81g of catalyst KOH, and replace with nitrogen 5 times, and evacuated to a pressure of -0.08MPa, then stirred (speed 500r / min) to raise the temperature, when the temperature increased to 85°C, add 88.75g of ethylene oxide, control the initial pressure of 0.20MPa, and react until the pressure is constant , then the temperature was raised to 100°C, the pressure was controlled at 0.20MPa, 399.375g of propylene oxide was continuously added, and the remaining 177.5g of ethylene oxide was continuously added after the reaction until the pressure did not change. After a period of aging, the remaining 221.875g of propylene oxide was added Propylene oxide is added continuously, the pressure is controlled at 0.20MP...
Embodiment 2
[0058] Preparation of polyether polyol A:
[0059] In a 2.5L 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 342g of sucrose, 39.5g of pentaerythritol, 3.81g of catalyst KOH, and replace with nitrogen 5 times, and evacuate to a pressure of -0.08MPa, then stir (speed 500r / min) to raise the temperature, when the temperature increases to 90°C, add 133.125g of ethylene oxide, control the initial pressure of 0.25MPa, and react until the pressure is constant , then the temperature was raised to 110°C, the pressure was controlled at 0.25MPa, 257.375g of propylene oxide was continuously added, and the remaining 337.25g of ethylene oxide was continuously added after the reaction until the pressure no longer changed, and the remaining 159.75g of ethylene oxide was added continuously after aging for a period of time. Add propane continuously, control the pressure at...
Embodiment 3
[0078] Preparation of polyether polyol A:
[0079] In a 2.5L 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 342g of sucrose, 39.5g of pentaerythritol, 3.81g of catalyst KOH, and replace with nitrogen 5 times, and evacuated to a pressure of -0.08MPa, then stirred (speed 500r / min) to raise the temperature, when the temperature increased to 85°C, add 177.5g of ethylene oxide, control the initial pressure of 0.20MPa, and react until the pressure is constant , then the temperature was raised to 120°C, the pressure was controlled at 0.20MPa, 133.125g of propylene oxide was continuously added, and the remaining 488.125g of ethylene oxide was continuously added after the reaction until the pressure did not change. After a period of aging, the remaining 88.75g of epoxy Add propane continuously, control the pressure at 0.20MPa, react until the pressure no longer c...
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