A2/o-mbr composite treatment system and method based on efficient utilization of carbon sources
A composite treatment and high-efficiency technology, applied in the direction of water/sewage multi-stage treatment, biological water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem of low carbon-nitrogen ratio and high discharge standards for urban sewage treatment plants to stably meet the standards And energy saving and consumption reduction, denitrification is not fully utilized, carbon source is not used efficiently, etc., to achieve the effect of energy saving and consumption reduction, improve the utilization rate of carbon source, and improve the effect of energy saving and consumption reduction
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Embodiment 1
[0029] Embodiment 1: A kind of A based on efficient utilization of carbon source 2 The composite processing method of / O and MBR includes the following steps:
[0030] a, the pretreated sewage 7 enters the anaerobic pool 1 together with the first anoxic pool 2 mixed solution that is backflowed through the first internal reflux system 9, and stays for 1.5 hours under anaerobic stirring conditions. L) under the action of anaerobic phosphorus release reaction; wherein the return flow of the mixed solution of the first anoxic tank is 2 times of the influent flow of sewage 7;
[0031] B, the anaerobic tank 1 mixed solution that step a gained enters the first anoxic tank 2 together through the second internal reflux system 11 refluxed aerobic tank 4 mixed solution, stays 4 hours under anoxic stirring condition, in microorganism ( MLSS is 4.5g / L) to carry out denitrification reaction and denitrification phosphorus removal reaction; wherein the return flow of the mixed liquid in the ...
Embodiment 2
[0037] Embodiment 2: A kind of A based on efficient utilization of carbon source 2 The composite processing method of / O and MBR includes the following steps:
[0038] a, the pretreated sewage 7 enters the anaerobic pool 1 together with the mixed solution of the first anoxic pool 2 backflowed through the first internal reflux system 9, and stays for 1 hour under anaerobic stirring conditions. L) under the action of anaerobic phosphorus release reaction; wherein the return flow of the mixed solution of the first anoxic tank is 1 times of the influent flow of sewage 7;
[0039] B, the anaerobic tank 1 mixed solution that step a gained enters the first anoxic tank 2 together through the second internal reflux system 11 refluxed aerobic tank 4 mixed solution, stays 3 hours under anoxic stirring condition, in microorganism ( MLSS is 6g / L) to carry out denitrification reaction and denitrification phosphorus removal reaction; the return flow of the mixed liquid in the aeration tank ...
Embodiment 3
[0045] Embodiment 3: A kind of A based on efficient utilization of carbon source 2 The composite processing method of / O and MBR includes the following steps:
[0046] a, the pretreated sewage 7 enters the anaerobic pool 1 together with the first anoxic pool 2 mixed solution that is backflowed through the first internal reflux system 9, and stays for 1.5 hours under anaerobic stirring conditions. L) under the action of anaerobic phosphorus release reaction; wherein the return flow of the mixed solution of the first anoxic tank is 2 times of the influent flow of sewage 7;
[0047] B, the anaerobic tank 1 mixed solution that step a gained enters the first anoxic tank 2 together through the second internal reflux system 11 refluxed aerobic tank 4 mixed solution, stays 4 hours under anoxic stirring condition, in microorganism ( MLSS is 4.5g / L) to carry out denitrification reaction and denitrification phosphorus removal reaction; the return flow of the mixed liquid in the aeration...
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