A kind of hydroxyphenylglycine centrifugal mother liquor treatment device and method
A technology of hydroxyphenylglycine mother and p-hydroxyphenylglycine, which is applied in the field of resource recycling and utilization, can solve the problems of complicated equipment and inability to separate o-hydroxyphenylglycine, and achieves the effects of improving operation efficiency, good environmental protection and good economic benefits.
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Embodiment 1
[0034] The waste water is the mother liquor (para-hydroxyphenylglycine) obtained by centrifuging the reaction solution after synthesizing p-hydroxyphenylglycine by one-step method of phenol, glyoxylic acid and sulfamic acid, removing phenol and crystallizing the p-hydroxyphenylglycine after post-treatment. The mass concentration of glycine is 1.17%, the mass concentration of o-hydroxyphenylglycine is 2.85%, and the mass concentration of ammonium sulfate is 20%). 5m, each resin tower is filled with D113 resin, and the volume of filled resin is 5m 3 , the control mother liquor flow is 14m 3 / h, the total mother liquor volume is 140m 3 , the amount of mother liquor can make 3 to 4 resin towers saturated. After the adsorption tower is saturated, desorb with hot water, control the hot water temperature to be 50 °C, and the hot water elution flow rate to be 4 m 3 / h, the specific steps are as follows:
[0035] 1. Refer to Figure 4 , the first resin tower 3 and the second resin...
Embodiment 2
[0044] The hydroxyphenylglycine centrifugal mother liquor (para-hydroxyphenylglycine mass concentration 1.18%, o-Hydroxyphenylglycine mass concentration 2.87%, ammonium sulfate mass concentration 20%) was first passed through the filter to remove insoluble particles, and then entered the resin tower, as described in Example 1. The above method is operated, the difference is: the first resin tower 3 is filled with H103 type resin, the second resin tower 4 and the third resin tower 5 are filled with 105 type resin, and each tower is filled with 5m resin 3 , the control mother liquor flow is 14m 3 / h, the total mother liquor volume is 140m 3, p-hydroxyphenylglycine and o-hydroxyphenylglycine were adsorbed on the resin. The adsorbed wastewater enters the MVR, and is concentrated and crystallized to obtain ammonium sulfate solid (yield 99.0%, purity 99.3%). The resin saturated with adsorption is desorbed with hot water, the temperature of the hot water is controlled to be 55 °C, ...
Embodiment 3
[0046] The hydroxyphenylglycine centrifugal mother liquor (para-hydroxyphenylglycine mass concentration 1.23%, o-Hydroxyphenylglycine mass concentration 2.97%, ammonium sulfate mass concentration 18%) was first passed through the filter to remove insoluble particles, and then entered the resin tower, as described in Example 1. The above method is operated, the difference is: the first resin tower 3 is filled with H103 type resin, the second resin tower 4 and the third resin tower 5 are filled with 511 type resin, and each tower is filled with 5m resin 3 , the control mother liquor flow is 13m 3 / h, the total mother liquor volume is 130m 3 , p-hydroxyphenylglycine and o-hydroxyphenylglycine were adsorbed on the resin. The adsorbed wastewater enters the MVR, and the ammonium sulfate solid obtained by concentrating and crystallizing (98.9% yield, 99.2% purity). The resin saturated with adsorption is desorbed with hot water, the temperature of the hot water is controlled to be 6...
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