Method and device for condensing rubber polymer
A technology of rubber polymer and coagulation kettle, which is applied in the field of polymer reprocessing, can solve the problems of poor solvent removal rate and high energy consumption, and achieve the effects of improving solvent recovery rate, reducing pollution and reducing solvent content
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[0057] According to a preferred embodiment of the present invention, a first colloidal water pump is provided on the connecting pipeline between the colloidal water outlet at the bottom of the first coagulation tank F1 and the colloidal water inlet of the first water diversion pipeline G1 P1, such as figure 1 As shown; or the communication pipeline between the colloidal water outlet of the first water-dividing pipeline G1 and the colloidal water inlet of the second coagulation kettle F2 is provided with a first colloidal water pump P1, such as figure 2 shown.
[0058] According to a preferred embodiment of the present invention, a second colloidal water pump is provided on the communication pipeline between the colloidal water outlet at the bottom of the second coagulation tank F2 and the colloidal water inlet of the second water diversion pipeline G2 P3, such as figure 1 As shown; or the communication pipeline between the colloidal water outlet of the second water distribu...
Embodiment 1
[0075] The total volume of the first condensation kettle F1, the second condensation kettle F2 and the third condensation kettle F3 is 60m respectively 3 、100m 3 , 100m 3 . The length of the first water distribution pipe G1 is 2 meters, the diameter of the inner pipe 1 is DN400, the diameter of the jacket pipe 2 is DN600, and a row of drainage holes 3 with a diameter of 200mm are opened on both sides of the inner pipe 1, and the drainage holes 3 The distance between the holes is 600mm, and 7 drainage holes are opened on the 2-meter-long pipeline. The drainage holes are covered with wire mesh 4. The connection method between the wire mesh 4 and the drainage holes 3 is welding, and the mesh number of the wire mesh 4 is 20 mesh. The length of the second water diversion pipe G2 is 1.6 meters, the diameter of the inner pipe 1 is DN350, the diameter of the jacket pipe 2 is DN600, and a row of drain holes 3 with a diameter of 150mm are opened on both sides of the inner pipe 1, and ...
Embodiment 2
[0084] Coagulate the polyisoprene solution according to the method described in Example 1. The difference is that the operating conditions of the first coagulation tank F1 include: gauge pressure 0.01MPa, temperature 92°C, residence time 25.5min; The operating conditions of F2 include: gauge pressure 0.09MPa, temperature 109°C, residence time of colloidal water is 44min; the operating conditions of the third coagulation tank F3 include: gauge pressure 0.005MPa, temperature 93°C, residence time of colloidal water The time is 51.8min; the flow rate of the first colloidal water pump P1 is 112500kg / h; the flow rate of the second colloidal water pump P3 is 102160kg / h.
[0085] The result after condensation is: the total residence time of the condensation system is 2.02h, the system consumes a total of 45000kg of water and 1800kg of steam, and processes 7500kg of polyisoprene solution. Collect the vapor water that obtains 9345kg (the hexane content is 72.22% by weight), the third co...
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