A rapid construction method for methanogenesis under acidic conditions
A construction method and acidic condition technology, which is applied in the field of rapid construction of methanogens in acidic conditions and stable treatment of high-concentration organic matter, can solve the problems of spatial inhomogeneity and inability to determine whether the methanogens are acid-resistant, and achieve shortened debugging and obvious Economic value and development potential, the effect of increasing daily processing capacity
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Embodiment 1
[0028] (1) Take 10kg of anaerobic digestion treatment dehydration residue (solid content 20%, VS content 0.7) in the middle temperature 35 ℃ of urban sewage plant sludge, grind, and use 50 mesh screens to sieve, collect its sieve as Seed mud.
[0029] (2) Put 8.6kg of the above-mentioned seed sludge in the 250L anaerobic reactor (equivalent to 1.2kg of VS total amount), 1.2kg of acetic acid is used as a methane-producing substrate, and add base buffer solution until the total volume of the solution in the reactor is 200L. When the concentration of acetate is 100mM. The main composition of the base buffer is (1L): 6g Na 2 CO 3 , 0.2g MgCl 2 ·6H 2 O, 1g NH 4 Cl, 0.1g CaCl 2 , 0.2gNa 2 S·9H 2 O, 1.385g K 2 HPO 4 , 1.4g KH 2 PO 4 , 5mg Na 2 -EDTA·2H 2 O, 1.5mg CoCl 4 , 1mg MnCl 2 4H 2 O, 1mg FeSO 4 ·7H 2 O, 1mg ZnCl 2 , 0.4mg AlCl 3 ·6H 2 O, 0.3mg NaWo 4 2H 2 O, 0.2mg CuCl 2 2H 2 O, 0.2mg NiSO 4 ·6H 2 O, 0.1 mg H 2 SeO 4 , 1mg HBO 3 , 1mgNaMoO 4 2H ...
Embodiment 2
[0036] (1) Take 10kg of municipal solid waste dehydration residue from high-temperature 55°C anaerobic digestion treatment (solid content 30%, VS content 0.7), grind it, and sieve it with a 70-mesh sieve, and collect the under-sieve material as seed mud .
[0037] (2) Put 8.6kg of the above-mentioned seed sludge in the 250L anaerobic reactor (equivalent to 1.8kg of VS total amount), 2.16kg of acetic acid is used as the methane-producing substrate, and the base buffer solution is added until the total volume of the solution in the reactor is 200L. When the acetate concentration was 120mM. The main composition of the base buffer is (1L): 8g Na 2 CO 3 , 0.2g MgCl 2 ·6H 2 O, 1g NH 4 Cl, 0.1gCaCl 2 , 0.2g Na 2 S·9H 2 O, 1.385g K 2 HPO 4 , 1.4g KH 2 PO 4 , 5mg Na 2 -EDTA·2H 2 O, 1.5mg CoCl 4 , 1mg MnCl 2 4H 2 O, 1mg FeSO 4 ·7H 2 O, 1mg ZnCl 2 , 0.4mg AlCl 3 ·6H 2 O, 0.3mg NaWo 4 2H 2 O, 0.2mg CuCl 2 2H 2 O, 0.2mg NiSO 4 ·6H 2 O, 0.1 mg H 2 SeO 4 , 1mg H...
Embodiment 3
[0044] (1) Take 10kg of anaerobic granular sludge (solid content 20%, VS content 0.7) in the high temperature 60 ℃ anaerobic digestion reactor of the wastewater treatment device of the paper mill, grind it, and use a 50-mesh screen to sieve points, and collect the undersieve as seed mud.
[0045] (2) Put 8.6kg of the above-mentioned seed sludge in the 250L anaerobic reactor (equivalent to 1.2kg of VS total amount), 1.2kg of acetic acid is used as a methane-producing substrate, and add base buffer solution until the total volume of the solution in the reactor is 200L. When the concentration of acetate is 100mM. The main composition of the base buffer is (1L): 6g Na 2 CO 3 , 0.2g MgCl 2 ·6H 2 O, 1g NH 4 Cl, 0.1g CaCl 2 , 0.2gNa 2 S·9H 2 O, 1.385g K 2 HPO 4 , 1.4g KH 2 PO 4 , 5mg Na 2 -EDTA·2H 2 O, 1.5mg CoCl 4 , 1mg MnCl 2 4H 2 O, 1mg FeSO 4 ·7H 2 O, 1mg ZnCl 2 , 0.4mg AlCl 3 ·6H 2 O, 0.3mg NaWo 4 2H 2 O, 0.2mg CuCl 2 2H2 O, 0.2mg NiSO 4 ·6H 2 O, 0.1 m...
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