Table 8.5 (continued)
Substrate
Type of
operation
Temperature
(
C)
H 2 yield
H 2
production
rate
References
Coffee drink
manufacturing
wastewater
0.32 mol/mol
hexose
Coffee drink
manufacturing
wastewater
UASBR
Mesophilic
1.78 mol/mol
hexose
2.76 L/L/h [134, 135]
Diluted sugarcane
vinasse
AFBR
Thermophilic 2.86 mmol/g
COD fed
[136]
Tequila vinasse
ASBR
Mesophilic
200 mL/g
COD
1.21 L/L/d [137]
Starch wastewater
EGSBR
Mesophilic
0.07 L/L/h [138]
Raw starch waste
Batch
Mesophilic
2.02 mL/g
COD
[106]
Brewery waste
Continuous Mesophilic
37.9 mL/g VS
fed
2.68 L/L/h [139, 140]
Beer lees waste
Batch
Mesophilic
68.6 mL/g
TVS
54.4 mL/g dry
substrate
[140]
Beer lees waste
Batch
Mesophilic
53.0 ml/g-dry
beer lees
[141]
Mushroom cultivation waste
Batch
Thermophilic 0.73 mmol/g
TVS
2.02 mmol/
g VSS/d
[142]
Bean crude
manufacturing
wastewater
Continuous Mesophilic
24.0 mL/g VS
fed
1.20 L/L/h [143]
Fresh leachate
EGSBR
Mesophilic
0.09 L/L/h [144]
Corn stalk
Batch
144.3 mL/g
corn stalk
3.6 mL/g
corn stalk/h
[145]
Corn stalk waste
Batch
Mesophilic
150 mL/g TVS
[146]
Coffee pulp
Batch
Mesophilic
4.18 L/kg
substrate
[147]
Sweet sorghum
syrup
Batch
6.9 L/L
[148]
Sweet sorghum
syrup
ASBR
1.6 mol/mol
hexose
0.13 L/L/h [149]
Sweet sorghum
CSTR
Mesophilic
10.4 L/kg
substrate
2.5 L/d
[150]
Cassava wastewater Batch
Ambient
9.4 mL/g COD 3.5 mL/g
VSS/h
[151]
Cassava wastewater AnSBBR
Mesophilic
1.1 mol/kg
carbohydrate
0.7 L/L/d
[152]
Cassava stillage
Batch
Mesophilic
50.4 mL/g
substrate
[153]
(continued)
8 Biohydrogen of Industrial Waste
341