A kind of catalyst for preparing polyol, its preparation method and application
A catalyst and polyol technology, applied in the field of catalysts for preparing polyols, can solve the problems of low catalytic activity of the catalyst, inability to take into account high carbonate unit content and low cyclic carbonate content, etc.
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[0033] The invention provides a kind of preparation method that is used to prepare the catalyst of polyhydric alcohol, comprises the following steps:
[0034] Under the action of the first initiator, the double metal cyanide compound and the epoxide are polymerized to obtain a catalyst for preparing polyol;
[0035] The first initiator includes one or more of active hydrogen-containing compounds and active hydrogen-containing polymers.
[0036] In some embodiments of the present invention, the preparation method of the catalyst comprises the following steps:
[0037] A) Evacuate the weighing bottle at 75-85°C, fill with protective gas for 1.5-2.5 hours, and cool to room temperature;
[0038] B) under the atmosphere of protective gas, add the first starter and double metal cyanide in the weighing bottle to obtain a mixture;
[0039] C) Evacuate the reactor at 75-85°C, fill it with a protective gas for 1.5-2.5 hours, cool to room temperature, and add epoxy to the cooled reacto...
Embodiment 1
[0106] Evacuate the weighing bottle at 80°C and fill with CO 2 Gas treatment 2h (inflated 6 times), and cooled to room temperature; 2 Under the protection of air, add 10.0g of DMC (based on Zn 3 [Co(CN) 6 ] 2 double metal cyanide) and 25.0g sebacic acid to obtain a mixture;
[0107] Put the 500mL reactor at 80°C, after evacuation, fill with CO 2 Treat for 2h (inflate 6 times), and cool to room temperature, add the mixture in the reaction kettle, then add 100g propylene oxide to the reaction kettle through the connection of the catalyst weighing bottle, stir at a speed of 500rpm, pass carbon dioxide The pressure regulator feeds carbon dioxide into the reactor, and the reactor is placed in a constant temperature bath for polymerization. The carbon dioxide pressure for polymerization is 4.0Mpa, the polymerization reaction temperature is 80°C, and the polymerization reaction time is 4h. After the end of the polymerization reaction, unreacted monomers and carbon dioxide are s...
Embodiment 2
[0111] Evacuate the weighing bottle at 80°C and fill with CO 2 Gas treatment 2h (inflated 6 times), and cooled to room temperature; 2 Add 10.0g of DMC (based on Zn 3 [Co(CN) 6 ] 2 double metal cyanide) and 25.0g adipic acid to obtain a mixture;
[0112] Put the 500mL reactor at 80°C, after evacuation, fill with CO 2 Treat for 2h (inflate 6 times), and cool to room temperature, add the mixture in the reaction kettle, then add 100g propylene oxide to the reaction kettle through the connection of the catalyst weighing bottle, stir at a speed of 500rpm, pass carbon dioxide The pressure regulator feeds carbon dioxide into the reactor, and the reactor is placed in a constant temperature bath for polymerization. The carbon dioxide pressure for polymerization is 2.0Mpa, the polymerization reaction temperature is 80°C, and the polymerization reaction time is 4h. After the end of the polymerization reaction, unreacted monomers and carbon dioxide are slowly discharged, and the reac...
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