Polyether glycol, polyurethane rigid foamed plastic and preparation methods thereof
A technology of rigid foam plastic and polyether polyol, which is applied in the fields of ether preparation, chemical instruments and methods, sugar derivative preparation, etc., can solve the problems of high viscosity of polyether polyol, affecting process performance and low functionality, etc. To achieve the effect of excellent flame resistance, good process performance and high functionality
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Embodiment 1
[0024] The preparation of embodiment 1 polyether polyol
[0025] In a 15L polyether reactor, add 25g of glycerin, 250g of dimethylolphenol, 350g of sucrose and 5g of potassium hydroxide, melt at 80°C, dehydrate at 115°C under vacuum (1500Pa) for 2h, and obtain potassium alkoxide solution. The temperature was lowered to 80° C., nitrogen replacement was carried out, and this was repeated three times.
[0026]Afterwards, add 1100g of propylene oxide in batches: add 80g of propylene oxide, start stirring and heat up to 80°C; then slowly add 70g of propylene oxide (adding in 2 times, taking 1 hour), and then keep warm at 80°C for 1 hour , the pressure in the kettle drops to 0.1MPa; continue to add 100g of propylene oxide, and raise the temperature to 110°C; when the pressure in the kettle drops to 0.1MPa, put in 100g of propylene oxide, and the temperature It will rise gradually. When it reaches 120°C, the pressure in the kettle will drop rapidly. Immediately pass circulating wate...
Embodiment 2
[0028] Embodiment 2 Preparation of polyether polyol
[0029] In the raw material formula, except that the addition of propylene oxide is 1300g, the type and consumption of other raw materials, as well as the process operation method and conditions are the same as in Example 1, and the polyether polyol of the present invention is obtained.
Embodiment 3
[0030] Embodiment 3 Preparation of polyether polyol
[0031] In the raw material formula, glycerin is 50g, dimethylolphenol is 125g, sucrose is 450g, propylene oxide is 1150g, other raw material types and consumption, and process operation method and conditions are the same as embodiment 1, and the polyether polyol of the present invention is obtained. alcohol.
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