Device and method for removing volatile matter from polymer powder
A technology of polymer and volatile matter, which is applied in the field of polyolefin production equipment, can solve the problems of complex operation process and inability to guarantee the drying of polymer powder, and achieve the effects of improving devolatilization efficiency, keeping dryness and reducing product odor
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Embodiment 1
[0069] like figure 1 As shown, the device for removing volatile matter in the polymer powder includes a 300L intermediate storage tank and a 600L devolatilization tank. The pressure of the intermediate storage tank is 0.7MPa, and 30kg of polymer is stored. Keep it at 0.5MPa, and the temperature of the heat tracing insulation layer on the outer wall is 80°C. The hot nitrogen and steam are passed into the devolatilization tank at the same time, the temperature of the hot nitrogen is 100°C, and the flow rate is 60m 3 / h; the temperature of the steam is 160°C, and the flow rate is 5m 3 / h, the access time is 10min.
[0070] like image 3 The distribution plate in the devolatilization tank is shown as a direct current type. The two ends of the support shaft are connected with the rotating shaft in a keyed connection and supported by the container wall. One end is connected to the motor and controlled by a remote control unit. The control room is operated, and the seal between t...
Embodiment 2
[0073] like figure 2 As shown, the device for removing volatile matter in the polymer powder includes a 120L intermediate storage tank and a 300L devolatilization tank. The pressure of the intermediate storage tank is 0.5MPa, and 12kg of polymer is stored. Keep at 0.3MPa, there is paddle stirring inside, the rotation speed is 60r / h, and the temperature of the heat tracing insulation layer on the outer wall is 100°C. The hot nitrogen and steam are passed into the devolatilization tank at the same time, the temperature of the hot nitrogen is 80°C, and the flow rate is 35m 3 / h, the temperature of the steam is 160°C, and the flow rate is 1m 3 / h, the access time is 10min.
[0074] like image 3 The distribution plate in the devolatilization tank is shown as a direct current type. The two ends of the support shaft are connected to the rotating shaft in a pin connection and supported by the container wall. One end is connected to the motor and controlled by a remote control uni...
Embodiment 3
[0077] like figure 1 As shown, the device for removing volatile matter in the polymer powder includes a 300L intermediate storage tank and a 600L devolatilization tank. The pressure of the intermediate storage tank is 0.7MPa, and 35kg of polymer is stored. Keep it at 0.7MPa, and the temperature of the heat tracing insulation layer on the outer wall is 30°C. The hot nitrogen and steam are passed into the devolatilization tank at the same time, the temperature of the hot nitrogen is 90°C, and the flow rate is 100m 3 / h; the temperature of the steam is 160°C and the flow rate is 20m 3 / h, the access time is 30min.
[0078] like image 3 The distribution plate in the devolatilization tank is shown as a direct current type. The two ends of the support shaft are connected with the rotating shaft in a keyed connection and supported by the container wall. One end is connected to the motor and controlled by a remote control unit. The control room is operated, and the seal between th...
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