Preparation method of flame-retardant polyether glycol
A flame-retardant polyether and polyol technology, which is applied in the field of preparation of flame-retardant polyether polyols, can solve the problems of poor hydrolysis resistance stability and reduced catalytic activity, and achieve high hydrolysis resistance stability, lower viscosity, and facilitate engineering construction Effect
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Embodiment 1
[0015] (1) Accurately weigh 150 g of tetrabromobisphenol A, 120 g of propylene glycol, and 1.65 g of KOH catalyst, and transfer them into a polymerization kettle.
[0016] (2) Start stirring, nitrogen replacement 3 times, slowly heat up to 80°C and mix well.
[0017] (3) Continue to heat up to 90° C., slowly drop in 42 g of propylene oxide and stop feeding.
[0018] (4) After the reaction starts to polymerize, the remaining 235 g of propylene oxide is added in a continuous feeding mode to prepare crude polyether. The reaction temperature is 90±5°C, the reaction is 20h, and the reaction pressure is 0.2MPa.
[0019] (5) Cool the crude polyether to 79°C, add water and phosphoric acid, and adjust the pH to 6.3.
[0020] (6) Activated carbon is added for adsorption, the temperature is raised to 90° C., nitrogen is pumped to remove water, and the finished polyether is obtained by circulating filtration.
[0021] The product yield is 86%.
[0022] Finished product indicators: hyd...
Embodiment 2
[0025] (1) Accurately weigh 200 g of tetrabromobisphenol A, 120 g of glycerin, and 2.0 g of KOH catalyst, and transfer them into a polymerization kettle.
[0026] (2) Start stirring, nitrogen replacement 3 times, slowly heat up to 90°C and mix well.
[0027] (3) Continue to heat up to 95°C, slowly drop in 45g of propylene oxide and stop feeding.
[0028] (4) After the reaction starts to polymerize, the remaining 255 g of propylene oxide is added in a continuous feed mode to obtain a crude polyether. The reaction temperature is 95±5°C, the reaction is 18h, and the reaction pressure is 0.2MPa.
[0029] (5) Cool down the crude polyether to 82°C, add water and phosphoric acid, and adjust the pH to 5.7.
[0030] (6) Activated carbon is added for adsorption, the temperature is raised to 90° C., nitrogen is pumped to remove water, and the finished polyether is obtained by circulating filtration.
[0031] The product yield is 88%.
[0032] Finished product indicators: hydroxyl val...
Embodiment 3
[0035] (1) Accurately weigh 100 g of tetrabromobisphenol A, 100 g of dipropylene glycol, and 1.16 g of KOH catalyst, and transfer them into a polymerization kettle.
[0036] (2) Start stirring, nitrogen replacement 3 times, slowly heat up to 80°C and mix well.
[0037] (3) Continue to heat up to 90° C., slowly drop in 5 g of epichlorohydrin, and then stop feeding.
[0038] (4) After the reaction starts to polymerize, the remaining 115 g of epichlorohydrin is added in a continuous feeding manner to prepare crude polyether. The reaction temperature is 85±5°C, the reaction is 16h, and the reaction pressure is 0.1MPa.
[0039] (5) Cool down the crude polyether to 79°C, add water and phosphoric acid, and adjust the pH to 6.7.
[0040] (6) Activated carbon is added for adsorption, the temperature is raised to 95° C., and the water is vacuumed with nitrogen, and the finished polyether is obtained by circulating filtration.
[0041] The product yield is 82%.
[0042] Finished prod...
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