Treatment system and method of ethanol process wastewater, and application of system
A treatment method and technology for wastewater, applied in multi-stage water treatment, water/sewage treatment, natural water treatment, etc., can solve problems such as poor treatment effect and low treatment efficiency, reduce operating costs, improve denitrification efficiency, and improve Effect of Total Nitrogen Removal Rate
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Embodiment 1
[0087] This embodiment is used to illustrate the treatment system and method of the ethanol process wastewater of the present invention
[0088] (1) Treatment system for ethanol process wastewater
[0089] like figure 1As shown, the ethanol process wastewater is transported to the anaerobic treatment unit (comprising CSTR unit 1, solid-liquid separation device 2 and USAB unit 3) for anaerobic treatment to obtain the first wastewater and biogas; the first wastewater and part of the The ethanol process wastewater is delivered to the A / O unit 4 for the first anaerobic / aerobic treatment to obtain the second wastewater; the second wastewater is delivered to the A / O-MBR unit 5 containing the domesticated sludge, Perform a second anaerobic / aerobic treatment and obtain a third wastewater; recycle the acclimatized sludge in the A / O-MBR unit to the A / O4 unit, and recycle the acclimatized excess sludge to the anaerobic In the CSTR unit 1 of the treatment unit, the third wastewater is s...
Embodiment 2
[0103] This embodiment is used to illustrate the treatment system and method of the ethanol process wastewater of the present invention
[0104] (1) Treatment system for ethanol process wastewater
[0105] The treatment system was operated as described in Example 1, except that UASB was not included.
[0106] (2) Treatment method of ethanol process wastewater
[0107] The operation was carried out according to the method described in Example 1, except that the obtained first wastewater was not treated by UASB, but was directly transported to the A / O unit, and the subsequent process remained unchanged.
[0108] In this case, the concentration of TSS in the influent water of the A / O unit is relatively high, about 3500mg / L, so that the COD in the effluent water of the A / O unit is about 1000mg / L, and the ammonia nitrogen is about 80mg / L.
Embodiment 3
[0110] This embodiment is used to illustrate the treatment system and method of the ethanol process wastewater of the present invention
[0111] (1) Treatment system for ethanol process wastewater
[0112] The processing system described in Example 1 was followed.
[0113] (2) Treatment method of ethanol process wastewater
[0114] The operation was carried out according to the method described in Example 1, except that the ratio of the injection amount of the first wastewater to part of the ethanol process wastewater was such that the COD / TN value of the water entering the A / O unit was 6.
[0115] The amount of wastewater injected into the ethanol process is so small that when the COD / TN is 6, the effluent TN of the A / O unit is about 110mg / l, and the final effluent TN is about 75mg / l.
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