水解酸化罐(kg VS/ m3∙d)
给料 负荷(kg/d)
甲烷产量
(m3/kg VS)
水解酸化罐出料代谢产物组成、浓度
乙醇(mg/L)
乙酸(mg/L)
丙酸(mg/L)
丁酸(mg/L)
乳酸(mg/L)
-N (mg/L)
15.10
20
0
2320.55 ± 57.43
4355.41 ± 89.74
1241.13 ± 39.67
2641.08 ± 54.65
2345.62 ± 54.32
258.14 ± 24.62
22.65
30
0
2102.68 ± 64.39
4153.46 ± 93.45
1861.35 ± 47.49
2307.43 ± 74.01
3216.78 ± 34.53
350.87 ± 29.51
30.20
40
0
1748.62 ± 48.27
3623.16 ± 75.29
1743.84 ± 56.34
2411.23 ± 63.22
3645.38 ± 48.17
422.41 ± 31.95
37.75
50
0
1412.80 ± 72.63
3426.17 ± 64.76
1758.65 ± 48.65
2235.54 ± 74.83
4425.56 ± 51.68
427.52 ± 30.25
甲烷发酵 反应器
(kg VS/ m3∙d)
给料 负荷
(kg/d)
甲烷产量
(m3/kg VS)
甲烷发酵出料代谢产物组成、浓度
乙醇(mg/L)
乙酸(mg/L)
丙酸(mg/L)
丁酸(mg/L)
乳酸(mg/L)
-N (mg/L)
2.94
20
0.546 ± 0.001a
N/A
322.66 ± 38.87
76.73 ± 21.16
45.32 ± 12.63
12.46 ± 2.54
881.65 ± 40.81
4.61
30
0.551 ± 0.014a
N/A
338.28 ± 65.43
87.14 ± 16.76
48.16 ± 16.44
8.24 ± 1.27
1417.82 ± 65.63
6.28
40
0.525 ± 0.003a
N/A
398.41 ± 54.32
105.21 ± 19.32
67.98 ± 15.98
11.38 ± 3.12
2134.68 ± 43.54
8.15
50
0.480 ± 0.021b
N/A
432.09 ± 65.76
112.80 ± 17.71
76.25 ± 17.43
9.78 ± 2.68
2625.45 ± 96.14