Waste water treating and resourcelization method for tobias acid production
A technology for the production of wastewater and tunic acid, which is applied in chemical instruments and methods, multi-stage water/sewage treatment, adsorption water/sewage treatment, etc., can solve the problems that the technology has not been reported in the literature, and achieve the effect of reducing the chroma of the effluent
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Embodiment 1
[0016] Example 1: Put 10mL (about 7 grams) of ND-900 complex adsorption resin into a jacketed glass adsorption column (Φ12×160mm), in five copies, marked as A, B, C, D, E , where A, B, and C are primary adsorption columns, and D and E are secondary adsorption columns. Use NaOH aqueous solution to adjust the pH to 1-5. After filtering, pass it through the first-stage adsorption ND-900 resin bed at 20±5°C at a flow rate of 20mL / h, and in three columns A, B, and C. Two columns are sucked in series, and the third column is desorbed. The treatment capacity is 70mL / batch. The primary effluent is collected in a clean and dry container; after collecting several batches, the primary effluent is subjected to secondary adsorption at a flow rate of 25mL / h , Among the two columns D and E, one column is adsorbed and the other column is desorbed, the treatment capacity is 160ml / batch, the color of the effluent is 10-50, the concentration of sulfonated tunic acid is 700-1000mg / L, tunic acid a...
Embodiment 2
[0018] Example 2: Put 10mL (about 7 grams) of ND-900 complex adsorption resin into a jacketed glass adsorption column (Φ12×160mm), in triplicate; put 10ml (about 7.5 grams) of NDA-99 ultrahigh The cross-linked adsorption resin was loaded into a jacketed glass adsorption column (Φ12×160 mm), in duplicate. Adjust the pH of the waste water to 2-3. After filtering, pass it through the ND-900 resin bed at 20±5°C at a flow rate of 20mL / h. The two columns are sucked in series, and the third column is desorbed. Batches, the primary effluent is collected in a clean and dry container; after collecting several batches, the primary effluent is subjected to secondary adsorption by NDA-99 resin at a flow rate of 25mL / h, the treatment volume is 160ml / batch, and the effluent color The degree is 10 to 50, the concentration of sulfonated toric acid is <560mg / L, the concentration of toric acid and 2,1-acid is <60mg / L, and the COD is <1500mg / L.
[0019] Use 10mL of 12% NaOH aqueous solution and ...
Embodiment 3
[0020] Example 3: 100mL (about 70 grams) of ND-900 adsorption resin was loaded into a jacketed glass adsorption column (Φ32×360mm), in triplicate; 100ml (about 75 grams) of NDA-99 ultra-high crosslinking The adsorption resin was loaded into a jacketed glass adsorption column (Φ32×360mm) in duplicate; the pH of the wastewater was adjusted to 2-3, and after filtration, it was first passed through the ND at 20±5°C at a flow rate of 200mL / h. -900 resin bed, two columns are connected in series for adsorption, and the third column is desorbed. The processing capacity is 700mL / batch. The primary effluent is collected in a clean and dry container; The flow rate is carried out by NDA-99 resin for secondary adsorption, the treatment capacity is 1600ml / batch, the color of the effluent is 20-50, the concentration of sulfonated tunic acid is less than 560mg / L, the concentration of tunic acid and 2,1-acid <60mg / L, COD<1500mg / L.
[0021] Use 100mL 12% NaOH aqueous solution and 300mL deioniz...
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