Treatment method for desorption liquid by process of deeply treating coking wastewater to adsorb resin
A technology for advanced treatment and resin adsorption, applied in the field of desorption liquid treatment and adsorption resin desorption liquid treatment, can solve the problems of dark color, poor biodegradability and high chemical oxygen demand, and achieve simple process, low cost, The effect of low processing cost
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Embodiment 1
[0017] A treatment method for coking wastewater advanced treatment adsorption resin desorption liquid, using such as figure 1 The regulating pool 1 and the reaction pool 2 shown are connected through the intermediate pump 3 between the regulating pool 1 and the reaction pool 2, and the reaction pool 2 is connected with an efflux pump 4, and the volumes of the regulating pool 1 and the reaction pool 2 are both 80 cubic meters , a plurality of bronchi 105 are respectively installed at the bottom of the regulating pool 1 and the reaction pool 2, and each bronchus 105 is provided with a plurality of air holes, and each bronchus 105 is connected with the gas supply device through the main air pipe 104; the regulating pool 1 and the reaction pool 2 are respectively equipped with a plurality of material conveying pipes, the regulating tank 1 is equipped with coking wastewater advanced treatment adsorption resin desorption liquid conveying pipe 101, sodium hydroxide conveying pipe 102 ...
Embodiment 2
[0023] The difference between this embodiment and embodiment 1 is:
[0024] Specific steps are as follows:
[0025] A. Transport the coking wastewater advanced treatment adsorption resin desorption liquid to the adjustment tank 1, check its pH value, and if the pH value is less than 7, add sodium hydroxide to the adjustment tank 1, start the gas supply device and input nitrogen gas into the adjustment tank 1 for stirring , to obtain an intermediate solution with a pH value of 7;
[0026] B, step A gained intermediate liquid is transported to reaction tank 2 by intermediate pump 3, in reaction tank 2, add ferrous sulfate solution and hydrogen peroxide and carry out aeration reaction, the concentration of ferrous sulfate solution is 250mg / L, and the concentration of hydrogen peroxide is 28%, the volume ratio of the intermediate solution, ferrous sulfate solution and hydrogen peroxide is 100:1:6, start the gas supply device to input nitrogen into the reaction tank 2 for stirring...
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