Continuous production method and device for high-purity alkali metal catalysis of polyether polyol
A technology of metal-catalyzed polyether and polyether polyol, which is applied in the field of continuous production method and device of high-purity alkali metal-catalyzed polyether polyol, can solve the problems of lengthy preparation process and long production cycle, and achieve production process The effect of simplicity, high production efficiency, and simple device structure
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Embodiment 1
[0040] (1) Preparation of alkali metal catalyzed polyether polyol crude polymer:
[0041] at 15m 3 230kg of glycerin was added to the stainless steel reaction kettle 1 for nitrogen replacement, and the oxygen content in the reaction kettle 1 was measured to be lower than 100ppm, and 80kg of potassium hydroxide aqueous solution with a mass concentration of 45% was sucked in airtightly, and then the temperature was raised to 90°C for nitrogen blowing. Soak decompression dehydration. Keep the temperature in the kettle at 90°C, continuously add 9970kg propylene oxide and 1800kg ethylene oxide, after the feeding is completed, react with internal pressure for 1 hour to prepare KOH catalyzed polyether polyol crude polymer, and then discharge it into the buffer tank In 2, the temperature of the buffer tank 2 is maintained at 90°C, filled with nitrogen, and maintained at a slightly positive pressure.
[0042] (2) Post-treatment of polyether polyol crude polymer:
[0043] The polyeth...
Embodiment 2
[0046] (1) Preparation of alkali metal catalyzed polyether polyol crude polymer:
[0047] at 15m 3 230kg of glycerin was added to the stainless steel reaction kettle 1 for nitrogen replacement, and the oxygen content in the reaction kettle 1 was measured to be lower than 100ppm, and 80kg of potassium hydroxide aqueous solution with a mass concentration of 45% was sucked in airtightly, and then the temperature was raised to 90°C for nitrogen blowing. Soak decompression dehydration. Keep the temperature in the kettle at 110°C, continuously add 9970kg propylene oxide and 1800kg ethylene oxide, after the addition, react under internal pressure for 1 hour to prepare KOH catalyzed polyether polyol crude polymer, and then discharge it into the buffer tank In step 2, the temperature of the buffer tank 2 was maintained at 130°C, filled with nitrogen, and kept at a slightly positive pressure.
[0048] (2) Post-treatment of polyether polyol crude polymer:
[0049] The polyether polyol...
Embodiment 3
[0052] (1) Preparation of alkali metal catalyzed polyether polyol crude polymer:
[0053] at 15m 3 230kg of glycerin was added to the stainless steel reaction kettle 1 for nitrogen replacement, and the oxygen content in the reaction kettle 1 was measured to be lower than 100ppm, and 80kg of potassium hydroxide aqueous solution with a mass concentration of 45% was sucked in airtightly, and then the temperature was raised to 90°C for nitrogen blowing. Soak decompression dehydration. Keep the temperature in the kettle at 100°C, continuously add 9970kg propylene oxide and 1800kg ethylene oxide, after the feeding is completed, react with internal pressure for 1 hour to prepare KOH catalyzed polyether polyol crude polymer, and then discharge it into the buffer tank In 2, the temperature of the buffer tank 2 is maintained at 100°C, filled with nitrogen, and maintained at a slightly positive pressure.
[0054] (2) Post-treatment of polyether polyol crude polymer:
[0055] The polye...
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