Dynamic operation method of sludge advanced anaerobic digestion system based on argillaceous characteristics
An anaerobic digestion system, dynamic operation technology, applied in chemical instruments and methods, sludge treatment, biological sludge treatment, etc., can solve the problems of low organic matter degradation rate, low organic matter content, long residence time, etc., and achieve operability Strong, extensive engineering application value, the effect of improving performance and stability
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Embodiment 1
[0027] The organic content of dewatered sludge from an urban sewage treatment plant is 59.34-60%, C / N is about 7.3, and pH is 6.31-6.86. When sludge is used for anaerobic digestion alone, the water content, temperature and digestion time of the sludge are controlled to 88 ~90%, 35±0.5℃, and 19.8d, the organic matter degradation rate, unit sludge gas production, and unit organic matter removal gas yield of the digestive system were 19.3~20.9% (average 20.1%), 6.6~9.3 (average 7.6m 3 / m 3 ), 0.60~0.77 (mean 0.66m 3 / kgVS); using alkali thermal hydrolysis pretreatment, pressure, temperature, digestion time and alkali dosage are 0.14Mpa, 124℃, 45min and 0.04gNaOH / gVS respectively, the parameters of the anaerobic digestion unit are the same, the organic matter in the digestion system The degradation rate, gas production per unit of sludge, and gas production per unit of removal of organic matter were 23.8 to 26.3% (average 24.8%), 12.1 to 17.0 (average 13.7 m 3 / m 3 ), 0.75~1.04...
Embodiment 2
[0029] The organic content of sludge in an urban sewage treatment plant is 66.26-67.44%, C / N 5.6, and pH is 6.01-6.77. When sludge is used for separate anaerobic digestion, the water content, temperature and digestion time of the sludge are controlled to be 88-88 90%, 35±0.5℃, 20d, the organic matter degradation rate of the digestion system, the unit gas production of sludge, and the gas production per unit of removal of organic matter are 24.0~30.7% (average 27.6%), 10.03~12.2m 3 / m 3 (11.6m 3 / m 3 ), 0.58~0.72m 3 / kgVS (mean 0.66m 3 / kgVS); using alkaline thermal hydrolysis pretreatment, pressure, temperature, digestion time, alkali dosage were 0.14Mpa, 124℃, 40min, 0.02gNaOH / gVS, the parameters of the anaerobic digestion unit were the same, the organic matter in the digestion system was The degradation rate, gas production per unit of organic matter, and gas production per unit of organic matter removed are 34.2 to 41.8% (average 37.6%), 16.0 to 19.2 m 3 / m 3 (17.3m 3...
Embodiment 3
[0031] The dewatered sludge of an urban sewage treatment plant is treated with alkaline thermal hydrolysis pretreatment-advanced anaerobic digestion system. The processing performance of synergistic anaerobic digestion, sludge pretreatment alone and mixed with kitchen waste for synergistic digestion.
[0032] The pH of the dewatered sludge cake is 7.10-7.15, the moisture content is 81.89%-82.02%, the organic matter content is 57.53%-57.60%, the C / N is 7.27-7.32, the pH of the kitchen waste is 5.60-6.60, and the moisture content is 84.03 %~88.02%, organic matter content is 86.22%~88.92%, C / N is 22.12~23.10.
[0033] Sludge pretreatment was carried out by anaerobic digestion alone, and the pressure, temperature, residence time and alkali dosage of the alkaline thermal hydrolysis pretreatment unit were controlled to be 0.14MPa, 124℃, 45min, 0.02gNaOH / gVS, respectively, and the anaerobic digestion unit was fed into the sludge. The solid content, temperature, and digestion time ar...
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