Preparation method of polyether polyol with high molecular weight, low unsaturation degree and high primary hydroxyl group content
A polyether polyol, high molecular weight technology, used in the chemical industry, can solve the problems of narrow molecular weight distribution, uneven molecular chain length, low viscosity, etc., and achieve the effects of short demoulding time, good physical and mechanical properties, and high activity.
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Embodiment 1
[0023] (1) 320g polyoxypropylene glycerol ether initiator, 0.0125g bimetallic complex catalyst, 14.4mg sulfuric acid (diluted into mass concentration is 10%) is made auxiliary agent, joins the pressure-resistant reactor of 4 liters , the contents of the reactor were vacuum dehydrated at 25° C. for 15 minutes while stirring (450 rpm) and nitrogen (50 ml / min). Vacuumize to vacuum degree -0.080Mpa, after heating up to 90°C, start nitrogen bubbling and continue heating up to 130°C, add 100g of propylene oxide to initiate. Add the remaining 2000g of propylene oxide while maintaining the temperature of the reactor at 130±3°C. After the propylene oxide is added, when the pressure of the reactor does not change, it indicates that the reaction is over, and polyether triol A is obtained. 2420g.
[0024] (2) make solvent with water, preparation mass fraction is 25% CaH 2 Aqueous solution forms a treatment agent.
[0025] (3) get the treatment agent 19.36g (CaH 2 The mass fraction of ...
Embodiment 2
[0028] (1) 125g polyoxypropylene propylene glycol ether initiator, 0.0125g bimetallic complex catalyst, 5.6mg sulfuric acid (diluted into mass concentration is 10%) is made auxiliary agent, joins in the pressure-resistant reactor of 4 liters, The contents of the reactor were vacuum dehydrated at 25° C. for 15 minutes while stirring (450 rpm) and nitrogen sparging (50 ml / min). Vacuumize to vacuum degree -0.080Mpa, after heating up to 90°C, start nitrogen bubbling and continue heating up to 130°C, add 100g of propylene oxide to initiate. Add the remaining 2000g of propylene oxide while maintaining the temperature of the reactor at 130±3°C. After the propylene oxide is added, when the pressure of the reactor does not change, it indicates that the reaction is over, and polyether diol A is obtained. 2225g.
[0029] (2) Use water as a solvent to prepare an aqueous solution of sodium carbonate with a mass fraction of 30% to form a treatment agent.
[0030] (3) Get 8.9g of the treat...
Embodiment 3
[0033] (1) 208g polyoxypropylene glycerol ether initiator, 0.0125g bimetallic complex catalyst, 9.4mg sulfuric acid (diluted into a mass concentration of 10%) is used as an auxiliary agent, and is added to a pressure-resistant reactor of 4 liters , the contents of the reactor were vacuum dehydrated at 25° C. for 15 minutes while stirring (450 rpm) and nitrogen (50 ml / min). Vacuumize to vacuum degree -0.080Mpa, after heating up to 90°C, start nitrogen bubbling and continue heating up to 130°C, add 100g of propylene oxide to initiate. Add the remaining 1892g of propylene oxide while maintaining the temperature of the reactor at 130±3°C. After the propylene oxide is added, when the pressure of the reactor does not change, it indicates that the reaction is over, and polyether triol A is obtained. 2300g.
[0034] (2) Using methanol as a solvent, prepare a methanol solution with a mass fraction of 10% tetramethylammonium hydroxide to form a treatment agent.
[0035] (3) Get 73.6g ...
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