Treatment of wastewater from production of para-aminophenol and making it be resource
A technology for the production of p-aminophenol and wastewater, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., to achieve good regeneration performance, CODCr reduction, and lighten the pollution load.
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[0023] Example 1: Put each 10ml of NDA1800 (about 7 grams) and NDA-10 (about 7.5 grams) resin into a jacketed glass adsorption column (Φ12×160mm). Adjust the pH of the p-aminophenol production wastewater to 7 (which can be in the range of 5-9), after filtering, pass through at a flow rate of 80ml / h (ie 8 resin bed volumes) at room temperature (-10~30℃) NDA1800 resin bed, the processing capacity is 400ml / batch, and it is collected in a clean and dry container. Then the effluent from the first stage adsorption is passed through the NDA-10 composite functional adsorption resin bed at a flow rate of 20ml / h (that is, 2 resin bed volumes), and the wastewater treatment capacity is 100ml / batch. TOC of original wastewater is 6100mg / L, COD Cr 18000mg / L, the content of p-aminophenol is 7500mg / L, the TOC of the effluent after the secondary adsorption drops to 300mg / L, COD Cr Reduced to 950mg / L, the content of p-aminophenol is less than 10mg / L, and the adsorbed water is colorless and transpare...
Example Embodiment
[0025] Example 2: Two PVC adsorption columns (Φ200*1400) were used to replace the two glass adsorption columns in Example 1, and each column was filled with 25L of resin. The wastewater flow rate and treatment volume were 2500 times that of Example 1. By operation, the effect of adsorption treatment and resource recovery consistent with Example 1 was obtained.
Example Embodiment
[0026] Example 3: Waste water directly enters the composite functional resin NDA-10 resin column. Choose three PVC adsorption towers with the same specifications (Φ200*1400mm) (numbered I, II, and III respectively), and each tower is filled with 25L of NDA-10 resin (about 18Kg). At room temperature (-10~30℃), the p-aminophenol production wastewater (its p-aminophenol content is about 2500mg / l) after pH adjustment and filtration is pumped into the adsorption tower, and the two towers (I, II towers) are connected in series. It is a method of simultaneous desorption in a single column (Tower III) with flow adsorption. The adsorption flow rate is controlled at 50L / h, and each batch is controlled at 300L. After the wastewater is treated, the adsorbed effluent is colorless and transparent, and the content of p-aminophenol is less than 10mg / L. The sodium chloride in the effluent can be further recovered.
[0027] The No. I adsorption tower containing NDA-10 composite functional adsorptio...
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