Production method of SAN resin through polymerization in two serially-connected kettles
A resin and polymerization kettle technology, applied in the petrochemical field, can solve the problems of widening distribution, destroying the appearance of products, long residence time, etc., to avoid the problem of uneven concentration, good heat and mass transfer efficiency, and short residence time. Effect
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Embodiment 1
[0045] Two tanks in series continuous process, the volume of the first polymerization tank is 12L, the volume of the second polymerization tank is 40L, and both polymerization tanks are vertical stirred tank reactors. In the monomer preparation tank connected with the first kettle, the monomer mixture is prepared, composed of 35 parts by weight of acrylonitrile, 66 parts by weight of styrene, introduced in the static mixer before the first reactor by flow meter and liquid pump, and reacted with The circulating material sucked up by the high-viscosity gear pump from the bottom of the reactor is completely mixed and then enters the reactor. Prepare the monomer mixture in the monomer preparation tank connected to the second kettle, which is composed of 32 parts by weight of acrylonitrile and 68 parts by weight of styrene, which are introduced into the condenser through a flow meter and a liquid pump, and mixed with the evaporation material in the condenser After entering the stat...
Embodiment 2
[0053] The preparation process of SAN is the same as in Example 1, except that the residence time of the control material in the first kettle is 0.5hr, and the residence time in the second kettle is 1.5hr. The obtained SAN polymer characterization analysis results are shown in Table 2.
Embodiment 3
[0055] The preparation process of SAN is the same as in Example 1, except that the residence time of the control material in the first kettle is 0.4hr, and the residence time in the second kettle is 1.6hr. The obtained SAN polymer characterization analysis results are shown in Table 2.
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