Method for preparing hydrophilic polyether polyol by utilization of recycled solar silicon chip cutting liquid
A technology of solar silicon wafer and polyether polyol, which is applied in the field of polyester polyol synthesis, can solve the problems of increased processing cost, high energy consumption, and high cost of raw materials for finished products of diethylene glycol
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Embodiment 1
[0017] Put 2000g of recovered solar silicon chip cutting fluid (hydroxyl value 500mg KOH / g) and 3000g of sucrose into the polyether reactor, and replace it with nitrogen three times; Put 6200g of propylene oxide into the kettle, keep the pressure of the reactor at 0.2MPa, slowly raise the temperature to 90°C, react for 1h, continue to heat up to 105°C, and keep it warm for 4h; when the pressure drops below -0.04MPa, vacuumize For 1.5 hours, the pressure and temperature were maintained at -0.095MPa and 105°C respectively; cooled to below 85°C and filtered out to obtain viscous light yellow-brown transparent polyether polyol for hard foam. (Hydroxyl value 436mg KOH / g, moisture 0.04%).
Embodiment 2
[0019] Put 1600g of recycled solar wafer cutting fluid (hydroxyl value 600mg KOH / g) and 3100g of sucrose into the polyether reactor, and replace it with nitrogen three times; Put 6550g of propylene oxide into the kettle, keep the pressure of the reactor at 0.3MPa, slowly raise the temperature to 100°C, react for 0.5h, continue to raise the temperature to 110°C, and keep it warm for 3h; when the pressure drops below -0.04MPa, pump Vacuum for 0.5h, maintain the pressure and temperature at -0.095MPa and 110°C respectively; cool to below 85°C and filter the material to obtain viscous light yellow-brown transparent polyether polyol for hard foam. (Hydroxyl value 441mgKOH / g, moisture 0.03%).
Embodiment 3
[0021] Put 1000g of recycled solar wafer cutting fluid (hydroxyl value 750mg KOH / g) and 2000g of sucrose into the polyether reactor, and replace it with nitrogen three times; Put 4500g of propylene oxide into the kettle, keep the pressure of the reactor at 0.4MPa, slowly raise the temperature to 95°C, react for 0.5h, continue to raise the temperature to 105°C, and keep it warm for 3.5h; when the pressure drops below -0.04MPa, Vacuumize for 1 hour, maintain the pressure and temperature at -0.095MPa and 108°C respectively; cool to below 85°C and filter the material to obtain a viscous light yellow-brown transparent polyether polyol for hard foam. (Hydroxyl value 434mg KOH / g, moisture 0.03%).
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