Process system and method for removing volatile matter from polymer
A process system and polymer technology, which is applied in the field of process systems for removing volatile matter from polymers, can solve problems such as high manufacturing costs, high energy consumption and production costs, and complicated maintenance, so as to reduce maintenance and repair costs and prolong service life Longevity, avoiding the effect of equipment clogging
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Embodiment 1
[0098] The process system for removing volatilization of the polymer in Example 1 also includes a delivery pump, a condenser, a solvent recovery system, a static mixer 7 and a granulator; the wound tube heat exchanger also includes a thermometer 13 .
[0099] In order to more clearly present the schematic diagram of the process system for polymer removal of volatile matter in the embodiment, figure 1 Transfer pumps, condensers, solvent recovery systems, and pelletizers are not included in this document.
[0100] The delivery pump is connected to the first coiled heat exchanger 1 and is used to transport the materials in the polymerization section to the first coiled heat exchanger 1 .
[0101] The condenser is connected with the gas phase outlet of the devolatilizer to recover the solvent.
[0102] The static mixer 7 is connected with the second devolatilizer 5, and is used for mixing the additive with the devolatilized polymer and cooling the polymer containing the additive....
Embodiment 2
[0119] The method for polymer removal of volatile matter in the embodiment 2 adopts the above-mentioned process system; the steps are as follows:
[0120] (1) butene-1 homopolymer solution is discharged from the polymerization reactor (100Kg / h), and the butene-1 homopolymer solution containing butene-1 monomer is delivered to In the first coiled heat exchanger 1 of the first devolatilization unit; wherein, the polymer that carries out devolatilization treatment is butene-1 homopolymer solution, and its mass concentration is 25%, and melting index MIE is 0.4, butene The mass content of en-1 is 8%.
[0121] Setting the temperature and pressure of the polymer inlet connection of the coiled heat exchanger in the first devolatilization unit, the temperature and pressure of the polymer outlet connection of the coiled heat exchanger, and the temperature and pressure of the devolatilizer;
[0122] Wherein, the temperature of the first polymer inlet joint 11 of the first coiled tube h...
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