Application method of modified charcoal in production of methane by anaerobic digestion of kitchen waste
A technology for kitchen waste and anaerobic digestion, applied in chemical instruments and methods, iron compounds, inorganic chemistry, etc., can solve the problems of small particle size of biochar, waste of biochar, difficult to recycle, etc. Yield, simple process effect
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Embodiment 1
[0025] A method for preparing modified biochar and applying it in anaerobic digestion of food waste to produce methane, such as figure 1 shown, including the following steps:
[0026] (1) Take coconut shell as raw material, pulverize and sieve after drying at 105°C for 24 hours, the sieving specification is 100 mesh, put it into a tube furnace, and slowly pyrolyze at a heating rate of 10°C / min under a nitrogen atmosphere. The biochar was obtained by pyrolysis at 500 °C for 1 h, and then the biochar was washed with 1 mol / L HCl solution and then repeatedly washed with deionized water until the pH value was neutral, and then dried in an oven at 105 °C for 24 h ;
[0027] (2) The Ni (NO 3 ) 2 .6H 2 O and Fe (NO 3 ) 3 .9H 2 O put in deionized water and mix well, in which Ni(NO 3 ) 2 .6H 2 O concentration is 0.1mol / L, Fe(NO 3 ) 3 .9H 2 The O concentration is 0.2mol / L, then citric acid is added as a complexing agent (the concentration of citric acid is 0.3mol / L after add...
Embodiment 2
[0041] The method is the same as in Example 1, except that:
[0042] Loaded nickel-iron composite oxide NiFe added to food waste anaerobic digestion system 2 O 4 The modified coconut shell biochar was added in an amount of 1.0g / L;
[0043] The final methane gas production rate was 313 mL / g VS, which was 25% higher than that of Comparative Example 1-1 without biochar addition.
Embodiment 3
[0045] The method is the same as in Example 1, except that:
[0046] Loaded nickel-iron composite oxide NiFe added to food waste anaerobic digestion system 2 O 4 The modified coconut shell biochar was added in an amount of 10g / L;
[0047] The final methane gas production rate was 326 mL / g VS, which was 30% higher than that of Comparative Example 1-1 without biochar addition.
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