A method for treating wastewater generated during the production of molecular sieve catalysts
A technology for producing waste water and production process, applied in natural water body treatment, chemical instruments and methods, multi-stage water/sewage treatment, etc., to achieve the effect of low investment, less bacterial agent dosage, and low operating cost
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Embodiment 1
[0036] Using the technological process of the present invention to treat the wastewater produced by a catalyst production enterprise in the molecular sieve modification process, the COD concentration is 25000-26000mg / L, the BOD concentration is 7000-7500mg / L, and the organic nitrogen concentration is 2000-2200mg / L , the concentration of ammonia nitrogen is 6000-6500mg / L, the pH value is 10-11, and the concentration of suspended matter is 3000-3500mg / L. The main test device configuration, operating conditions and treatment effects of each treatment unit are shown in Table 3.
[0037] Table 3 Main processing unit composition and processing effect of embodiment 1
[0038]
[0039] As can be seen from Table 3, after being treated by the method of the present invention, the effluent COD concentration is less than 70mg / L, the organic nitrogen concentration is less than 10mg / L, the ammonia nitrogen concentration is less than 20mg / L, and the total nitrogen concentration is less tha...
Embodiment 2
[0041] The process flow of the present invention is used to treat the wastewater produced by a catalyst production enterprise in the molecular sieve modification process. The COD concentration is 28000-29000mg / L, the BOD concentration is 5000-6000mg / L, and the organic nitrogen concentration is 2000-2500mg / L. , the concentration of ammonia nitrogen is 2500-3000mg / L, the pH value is 10-11.6, and the concentration of suspended matter is 3000-4000mg / L. The main test device configuration, operating conditions and treatment effects of each treatment unit are shown in Table 4.
[0042] Table 4 Main processing unit composition and processing effect of embodiment 2
[0043]
[0044] As can be seen from Table 4, after being treated by the method of the present invention, the effluent COD concentration is less than 80mg / L, the organic nitrogen concentration is less than 15mg / L, the ammonia nitrogen concentration is less than 20mg / L, and the total nitrogen concentration is less than 30...
Embodiment 3
[0046] Using the technological process of the present invention to treat the wastewater produced by a catalyst production enterprise in the molecular sieve modification process, the COD concentration is 35000-38000mg / L, the BOD concentration is 8000-9000mg / L, and the organic nitrogen concentration is 6000-7000mg / L , the concentration of ammonia nitrogen is 1000-1500mg / L, the pH value is 10-11, and the concentration of suspended matter is 4000-5000mg / L. The main test device configuration, operating conditions and treatment effects of each treatment unit are shown in Table 5.
[0047] Table 5 Main processing unit composition and processing effect of embodiment 3
[0048]
[0049] As can be seen from Table 5, after adopting the method of the present invention to process, effluent COD concentration is less than 80mg / L, and organic nitrogen concentration is less than 25mg / L, and ammonia nitrogen concentration is less than 20mg / L, and total nitrogen concentration is less than 30m...
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