Method for treating waste water in production of para-hydroxyphenyl hydantoin
A technology of p-hydroxybenzene hydantoin and a treatment method, which is applied in water/sewage treatment, water/sewage multi-stage treatment, adsorbed water/sewage treatment, etc., can solve the problem of high equipment requirements, high energy consumption of vacuum distillation, and increased treatment Cost and other issues, to achieve the effect of low pharmaceutical costs and operating costs, good environmental benefits, and good pretreatment effects
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Embodiment 1
[0034] First, add solid sodium sulfate to the phenol-containing mother liquor wastewater discharged from the production of p-hydroxyphenylhydantoin in an amount of 54g / 100mL(w / v), heat up to 40℃, stir for 35min, stand for 1h, separate the salt After precipitation, the water phase is separated and mixed with the material washing wastewater in the production process of p-hydroxyphenylhydantoin at a volume ratio of 1:3. The mixed solution is adsorbed in series by two columns, and the adsorption flow rate is controlled to 1BV / h. When the adsorption batch capacity reaches 20BV, the adsorption is stopped. The average phenol concentration in the adsorbed water was 3.92mg / L, CODcr=190.08mg / L (chemical oxygen consumption measured using potassium dichromate as the oxidant). Only the first column is desorbed: first configure 6% NaOH solution as a desorption agent, then add about 0.6BV of 6% NaOH solution to the column, heat to 70°C to soak the resin for 0.5h, then turn on the peristaltic pum...
Embodiment 2
[0036] First, add solid sodium sulfate to the mother liquor wastewater discharged from the production of p-hydroxyphenylhydantoin in the amount of 40g / 100mL(w / v), raise the temperature to 60℃, stir for 45min, stand for 1h, and separate the salt. The water phase is separated and mixed with the washing wastewater in a ratio of 1:1 by volume. Control the adsorption flow to 0.1BV / h. When the adsorption batch volume reaches 10BV, the adsorption is stopped, the temperature during desorption is 60°C, the flow rate is 0.1BV / h, and 4% NaOH is selected as the desorption agent. Add hydrochloric acid to adjust the pH of the desorption solution to about 4. Other conditions are the same as in Example 1. The average phenol content of the adsorbed water is 5.56mg / L, and CODcr=261.23mg / L.
[0037] The implementation shows that: solid potassium sulfate has similar effects, but the cost is higher, and the use of sodium chloride or potassium chloride also has similar effects.
Embodiment 3
[0039] First, add solid sodium sulfate in the amount of 42g / 100mL(w / v) to the high-concentration phenol-containing mother liquor wastewater, heat up to 50℃, stir for 50min, stand for 1h, separate the water phase after salting out, It is mixed with washing wastewater in a ratio of 1:3 by volume. Other conditions are the same as in Example 1. The average phenol content of the adsorbed water is 5.17mg / L, CODcr=217.67mg / L (chemical oxygen consumption measured using potassium dichromate as the oxidant).
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