A kind of process device and method for the production of cation exchange resin
A kind of technology of cation exchange, process device
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Embodiment 1
[0074] A kind of processing method of cation exchange resin production, comprises the following steps:
[0075] (1) Put 500kg of D001 type macroporous white ball and 300kg dichloroethane produced by our company (Kerry Environmental Technology Co., Ltd.) into the 3000 liter sulfonation reactor 1 through white ball inlet 14 and solvent inlet 15; then open the mother liquor Acid metering tank 4 outlet 23, mother liquor acid circulation pump 5, mother liquor acid inlet 13, 2960kg concentration is the mother liquor acid of 92.5%wt by mother liquor acid metering tank 4 and flows to sulfonation reactor 1; Carry out swelling in chemical reactor, and swelling time is 4 hours;
[0076] (2) After the swelling described in step (1) ends, open the heating steam of the sulfonation reactor 1 and heat it to 120° C., then open the discharge port 21 of the sulfur trioxide metering tank 2 and the sulfur trioxide feed pump 3, through Sulfur trioxide inlet 17 puts 280kg of sulfur trioxide into th...
Embodiment 2
[0085] A kind of processing method for the production of cation exchange resin, operation steps are basically the same as embodiment 1, difference is, in step (1), the dichloroethane of 210kg is replaced into 210kg massfraction and be the concentrated sulfuric acid of 98%, will The D001 type white ball produced by Kairui Environmental Protection Technology Co., Ltd. was replaced with commercially available 001×7 gel-type white ball; 2250kg of 001×7 type hydrogen-type cation exchange resin was obtained, and 180kg of waste acid with a concentration of 69.5% was produced.
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