Method and device for making hydrogen using sewage plant residual mud to produce anaerobic fermentation
A technology for anaerobic fermentation and excess sludge, which is applied in the fields of fermentation, anaerobic digestion treatment, chemical instruments and methods, etc., and can solve problems such as hydrogen consumption
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Embodiment 1
[0022] Concentration is that 10.36g / l residual activated sludge 50ml is packed under the alkaline condition that initial pH=11.0 directly regulates initial pH=11.0 with NaOH and packs in the serum bottle that total volume is 125ml, flushes pure nitrogen wherein to drive away the oxygen wherein, control temperature is 36°C, 150rpm, after 24-30 hours of anaerobic fermentation, the maximum hydrogen production rate can be obtained as 9.13LH 2 / kg-TS or 16.23LH 2 / kg-VS.
Embodiment 2
[0024] First, 50ml of excess activated sludge with a concentration of 12.60g / l was adjusted to pH = 12.0 with NaOH, treated with alkali at room temperature for 24 hours, then the initial pH value of the sludge was adjusted to 11.0, and the total volume was loaded into a serum bottle of 125ml , pour pure nitrogen into it to drive out the oxygen in it, control the temperature at 36°C, 150rpm, and get the maximum hydrogen production rate of 16.59LH after 24-30 hours of anaerobic fermentation 2 / kg-TS or 29.36LH 2 / kg-VS.
Embodiment 3
[0026] see figure 1 . At first the surplus activated sludge that concentration is 15.47g / l imports in sludge alkali treatment reactor 2 with sludge delivery pump 1, in this reactor 2, the pH=12.0 of sludge, process 24 hours at room temperature, then take 2.5 liters of sludge after treatment, adjust the sludge pH value to 11.0, put it into a closed sludge hydrogen production reactor 3 with a total volume of 3 liters, and fill the reactor 3 with nitrogen to drive away the oxygen therein. The temperature was controlled at 36°C, and after 24-30 hours of anaerobic fermentation, 379.93mlH 2 , the hydrogen production rate is 12.28LH 2 / kg-TS or 21.53LH 2 / kg-VS.
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