Method for treating waste water generated by washing of tert-butyl peroxybenzoate with weakly alkaline saline solution
A technology of tert-butyl peroxybenzoate and brine solution, which is applied in heating water/sewage treatment, peroxy compound preparation, chemical instruments and methods, etc. There is no reusable value, etc.
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Embodiment 1
[0022] The present embodiment provides a kind of treatment method of the waste water that adopts 1.0wt% sodium carbonate solution washing tert-butyl peroxybenzoate to produce, specifically comprises the steps:
[0023] (1) the purity of 700kg is 98.7wt% tert-butyl peroxybenzoate and the mixture of the 1.0wt% sodium carbonate solution used for washing is introduced into the layered tank from the weakly alkaline brine washing kettle, the upper strata 489.6kg organic phase obtains tert-butyl peroxybenzoate finished product 486.7Kg (purity is 99.52wt%) after drying, lower floor 210.4kg water phase (being the said waste water of the present invention, containing 0.98wt% sodium carbonate, 0.21wt% tert-butyl peroxybenzoate) Butanol), enters the evaporator;
[0024] (2) In the evaporator, after the waste water is evaporated at 65°C for 4.5h, 208.53kg of distilled raffinate (containing 0.99wt% sodium carbonate and 0.025wt% tert-butanol) is obtained, which is directly introduced into th...
Embodiment 2
[0027] The present embodiment provides a kind of treatment method of the waste water that adopts 3.0wt% sodium bicarbonate solution washing tert-butyl peroxybenzoate to produce, specifically comprises the steps:
[0028] (1), the tert-butyl peroxybenzoate of 98.7wt% with the purity of 700kg and the mixture of the 3.0wt% sodium bicarbonate solution used for washing are introduced into the layered tank from the washing kettle, and the upper floor is 497.2kg Organic phase obtains tert-butyl peroxybenzoate finished product 495.9Kg (purity is 99.68wt%) after drying, and lower floor 202.8kg water phase (containing 2.97wt% sodium bicarbonate, 0.24wt% tert-butyl alcohol) enters evaporator; Evaporated at 75°C for 4.0h;
[0029] (2) In the evaporator, after the waste water is evaporated at 75°C for 4 hours, 200.89kg of distilled raffinate (containing 3.00wt% sodium bicarbonate and 0.043wt% tert-butanol) is obtained, which is directly introduced into the weak alkaline brine washing tank ...
Embodiment 3
[0032] The present embodiment provides a kind of treatment method of the waste water that adopts 5.0wt% potassium carbonate solution to wash tert-butyl peroxybenzoate to produce, specifically comprises the steps:
[0033] (1), the purity of 700kg is 98.7wt% tert-butyl peroxybenzoate and the mixture of the 5.0wt% potassium carbonate solution used for washing is introduced into the layered tank from the washing kettle, and the upper 499.7kg organic Obtain tert-butyl peroxybenzoate finished product 496.1Kg (purity is 99.71wt%) after phase is dried, and lower floor 200.3kg water phase (containing 4.96wt% potassium carbonate, 0.24wt% tert-butyl alcohol) enters evaporator;
[0034] (2), in the evaporating device, the waste water was evaporated at 85° C. for 3.5 hours to obtain 198.28 kg of distilled raffinate (containing 5.01wt% potassium carbonate and 0.027wt% tert-butanol), which was directly introduced into the weak alkaline brine washing kettle; In addition, 2.02kg of evaporated...
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