Process for the polymerisation of vinyl-containing monomers
A polymerization method, vinyl technology, applied in the direction of chemical recycling, etc., to achieve a well-controlled effect
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Embodiment 1
[0041] S-PVC, K value 70
[0042] Polymerization of vinyl chloride was carried out in an aqueous reaction mixture at a temperature of 53° C. in a reactor using the method shown in FIG. 1 . After degassing, the resulting reaction mixture was mechanically dehydrated in a centrifuge and the polymer product was separated off. The reaction mixture from the centrifuge was filtered through a conventional plate module. The filtered solids were removed and the filtered reaction mixture was returned to the reactor and reused for further polymerization. Repeat the steps described several times for this PVC type. The quality of the filtered reaction mixture (Table 3) and the quality of the product (Table 4) obtained as a result of using the reaction mixture several times varied only very little; in particular the powder properties of the product did not produce any significant changes.
[0043] Table 3: Test data for filtered reaction mixture
[0044] PVC type: S-PVC, K valu...
Embodiment 2
[0048] S-PVC, K value 68
[0049] Polymerization of vinyl chloride was carried out in an aqueous reaction mixture at a temperature of 53° C. in a reactor using the method shown in FIG. 1 . After degassing, the resulting reaction mixture was mechanically dehydrated in a centrifuge and the polymer product was isolated. The reaction mixture from the centrifuge was filtered through a conventional plate module. The filtered solids were removed and the filtered reaction mixture was returned to the reactor and reused for further polymerization. Repeat the steps described several times for this PVC type. The quality of the filtered reaction mixture (Table 5) and the quality of the product (Table 6) resulting from using the reaction mixture several times varied only very slightly; in particular the powder properties of the product did not undergo any significant changes.
[0050] Table 5: Test data for filtered reaction mixture
[0051] PVC type: S-PVC, K value 68
un...
Embodiment 3
[0055] S-PVC, K value 70
[0056] Polymerization of vinyl chloride was carried out in an aqueous reaction mixture at a temperature of 53° C. in a reactor using the method shown in FIG. 2 . After degassing, the resulting reaction mixture was mechanically dehydrated in a centrifuge and the polymer product was isolated. The reaction mixture from the centrifuge was filtered through a conventional tubular module. The filtered solids were removed and the filtered reaction mixture was returned to the reactor and reused for further polymerization. Repeat the steps described several times for this PVC type. The quality of the filtered reaction mixture (Table 7) and the quality of the product (Table 8) resulting from using the reaction mixture several times varied only very slightly; in particular the powder properties of the product did not undergo any significant changes.
[0057] Table 7: Test data for filtered reaction mixture
[0058] PVC type: S-PVC, K value 70
u...
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