Process for continuous purification of polymer polyols
A purification method and polyol technology, which is applied in the continuous purification field of polymer polyols, can solve the problems of high odor, high VOC, and high residual acrylonitrile monomer, so as to improve the stripping effect, avoid fouling, and produce no yellowing change effect
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Embodiment 1
[0023] 1) The polymer polyol (CHP-2045D) I with a styrene content of 1.69% and acrylonitrile content of 1.86% is continuously fed into the first-stage flash tank with a capacity of 20T to control the polymerization. The liquid level of the polymer polyol I in the first-stage flash tank is 35%, and the flow rate of the polymer polyol I is 6t / h, then the residence time of the polymer polyol I in the first-stage flash tank is 1.17h ; The first-stage flash tank is bubbling with nitrogen at the same time, and the nitrogen flow is 150m 3 / h, control the pressure in the kettle to be -0.080Mpa, and the temperature in the tank to be 155°C to continuously obtain material I;
[0024] 2) Continuously feed the material I into the second-stage flash tank, the capacity of the first-level flash tank is 16T, the liquid level of the material I in the second-level flash tank is controlled to be 40%, and the flow rate of the material I is 6t / h, then the residence time of the material I in the s...
Embodiment 2
[0028] 1) The polymer polyol (CHP-H45) I with a styrene content of 1.80% and acrylonitrile content of 1.95% is continuously fed into the first-stage flash tank with a capacity of 20T to control the polymerization. The liquid level of the polymer polyol I in the first-stage flash tank is 50%, and the flow rate of the polymer polyol I is 8t / h, then the residence time of the polymer polyol I in the first-stage flash tank is 1.25h ; The first-stage flash tank is bubbling with nitrogen at the same time, and the nitrogen flow is 200m 3 / h, the pressure in the kettle is controlled to be -0.075Mpa, and the temperature in the tank is 160°C to continuously obtain material I;
[0029] 2) Continuously feed the material I into the second-stage flash tank, the capacity of the first-level flash tank is 16T, control the liquid level of the material I in the second-level flash tank to 50%, and the flow rate of the material I is 6t / h, the residence time of the material I in the second-stage f...
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