DNT (Dinitrotoluene) production wastewater recycling and treatment system and method
A technology for the production of wastewater and treatment methods, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of high treatment cost, secondary pollution, carcinogenicity, etc., and achieve The effect of reducing CODcr, avoiding environmental pollution, and simple operation process
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Embodiment 1
[0026] Embodiment 1: certain factory is maroon to DNT production waste water, CODcr (chemical oxygen demand) is 3072mg / L, nitro compound 400mg / L.
[0027] 1.1 Put 60ml (1BV=60ml in this example) of LS-200 resin into the resin column (Φ20ⅹ300mm) fixed by iron clips, and put 800ml of wastewater that has been precipitated and filtered at 0°C at 30ml / h (0.5BV / h ) through the resin bed, the CODcr measured in the column liquid is less than 500mg / L, and no nitro compounds are detected;
[0028] 1.2 Rinse the resin with 120ml of water at about 25-30°C to remove the residual DNT and inorganic salts in the resin pores;
[0029] 1.3 Drain the resin column until the liquid does not flow out, use 120ml (2BV) industrial methanol solution at 5°C to elute the resin at a rate of 30ml / h (0.5BV / h), and collect all the desorption solution, 120ml The content of nitro compounds in the eluent is 0.25%, equivalent to 0.30g of nitro compounds, and the comprehensive recovery rate is 93.7%;
[0030] 1...
Embodiment 2
[0032] The procedure is the same as in Example 1, but the waste water in step 2 is 180ml / h (3BV / h) through the resin bed, but after the adsorption is completed, the resin is rinsed with water at about 30°C, and after the desorption is completed, water at about 40°C is used for the resin Rinse, other conditions are constant, and its result is identical with embodiment 1.
Embodiment 3
[0034] The steps are the same as in Example 1, but the resin in step 1.1 is changed to Amberlite XDA-7 resin, 240ml (4BV) is used as the desorption solution, and the desorption is carried out at a flow rate of 120ml / L (2BV / h), and other conditions remain unchanged, except that each batch Except that the secondary treatment capacity has change, its result is identical with embodiment 1.
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