Method and device for making hydrogen using sewage plant residual mud to produce anaerobic fermentation
A technology of anaerobic fermentation and excess sludge, applied in fermentation, waste fuel, etc., 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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