A method for synchronously increasing methane production and methane percentage content by adjusting alkali and carbon-nitrogen ratio
A technology of percentage content and carbon-nitrogen ratio, applied in biological sludge treatment, waste fuel, etc., can solve the problems of low methane percentage and low methane efficiency, achieve efficient recovery, improve efficiency, increase methane production and The effect of the percentage of methane
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Embodiment 1
[0018] Add 1kg of sewage plant surplus sludge and ryegrass mixture with a carbon-to-nitrogen ratio (C / N) of 9 / 1 into a 2L reactor (made of glass fiber reinforced plastic, with a working volume of 1.5L, an inner diameter of 10cm, a height of 26cm, and a cylindrical shape ), at a temperature of 35-37°C for anaerobic digestion to produce methane, control the anaerobic digestion time to 20-30d, and adjust the initial pH value to 4-13. It is found that the initial pH value is 4, and the anaerobic digestion time is At 30 days, the methane production was 159.6 L / kgVS add , the percentage content of methane at this time is 52.5%.
Embodiment 2
[0020] Add 1kg of sewage plant surplus sludge and ryegrass mixture with a carbon-to-nitrogen ratio (C / N) of 9 / 1 into a 2L reactor (made of glass fiber reinforced plastic, with a working volume of 1.5L, an inner diameter of 10cm, a height of 26cm, and a cylindrical shape ), anaerobic digestion at a temperature of 35-37°C to produce methane, the anaerobic digestion time is controlled to 20-30d, and the initial pH value is adjusted to 4-13. It is found that the initial pH value is 5, and the anaerobic digestion time is 30d , the methane production was 201.6 L / kgVS add , the percentage content of methane at this time is 55.6%.
Embodiment 3
[0022] Add 1kg of sewage plant surplus sludge and ryegrass mixture with a carbon-to-nitrogen ratio (C / N) of 9 / 1 into a 2L reactor (made of glass fiber reinforced plastic, with a working volume of 1.5L, an inner diameter of 10cm, a height of 26cm, and a cylindrical shape ), anaerobic digestion at a temperature of 35-37°C to produce methane, the anaerobic digestion time is controlled to 20-30d, and the initial pH value is adjusted to 4-13. It is found that the initial pH value is 6, and the anaerobic digestion time is 30d , the methane production is 225.5 L / kgVS add , the percentage of methane at this time is 61.5%.
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