Synchronous methanogenesis and aerobic methane oxidation coupling denitrification process control method
An oxidation coupling, aerobic methane technology, applied in aerobic and anaerobic process treatment, chemical instruments and methods, water treatment parameter control, etc., can solve problems such as high safety risks, high operating costs, and difficult operations, and achieve The effect of high removal efficiency, promotion of mass transfer efficiency, and prolongation of contact time
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Embodiment 1
[0038] A method for controlling synchronous methane production and aerobic methane oxidation coupling denitrification process, comprising the following steps:
[0039] (1) The establishment of a reaction system includes: an inlet water adjustment tank, an inlet water peristaltic pump, an expanded granular sludge bed biofilm reactor, an internal circulation pump, and an air compressor;
[0040] The expanded granular sludge bed biofilm reactor includes two parts: the main reaction area and the three-phase separator, the volume ratio is (1~1.2):1; the lower part of the main reaction area is a granular sludge bed, and the top of the main reaction area is arranged with a fixed packing bed , the fixed packing bed accounts for 50% of the volume of the main reaction zone; the three-phase separator is located at the top of the reactor, and its main function is to settle sludge, separate the treated wastewater and collect methane gas; both the main reaction zone and the three-phase separ...
Embodiment 2
[0054] A method for controlling synchronous methane production and aerobic methane oxidation coupling denitrification process, comprising the following steps:
[0055] (1) The establishment of a reaction system includes: an inlet water adjustment tank, an inlet water peristaltic pump, an expanded granular sludge bed biofilm reactor, an internal circulation pump, and an air compressor;
[0056] The expanded granular sludge bed biofilm reactor includes two parts: the main reaction area and the three-phase separator, the volume ratio is (1~1.2):1; the lower part of the main reaction area is a granular sludge bed, and the top of the main reaction area is arranged with a fixed packing bed , the fixed packing bed accounts for 45% of the volume of the main reaction zone; the three-phase separator is located at the top of the reactor, and its main function is to settle sludge, separate the treated wastewater and collect methane gas; both the main reaction zone and the three-phase separ...
Embodiment 3
[0070] A method for controlling synchronous methane production and aerobic methane oxidation coupling denitrification process, comprising the following steps:
[0071] (1) The establishment of a reaction system includes: an inlet water adjustment tank, an inlet water peristaltic pump, an expanded granular sludge bed biofilm reactor, an internal circulation pump, and an air compressor;
[0072] The expanded granular sludge bed biofilm reactor includes two parts: the main reaction area and the three-phase separator, the volume ratio is (1~1.2):1; the lower part of the main reaction area is a granular sludge bed, and the top of the main reaction area is arranged with a fixed packing bed , the fixed packing bed accounts for 40% of the volume of the main reaction zone; the three-phase separator is located at the top of the reactor, and its main function is to settle sludge, separate the treated wastewater and collect methane gas; both the main reaction zone and the three-phase separ...
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