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A maximum cumulative hydrogen yield of 60.2 mL/g-dry soybean straw was achieved, which was approximately 11-fold greater than that in raw soybean straw.
The maximum cumulative hydrogen production of 3501 mL/L was achieved under the optimum conditions of the initial pH of 6.05, sweet potato starch concentration of 27.63 g/L, and FeSO4 concentration of 63.17 mg/L.
The maximum cumulative hydrogen production and % substrate conversion efficiencies were observed at 300 mg/L Fe SO4 OH(H2O)2 concentration (Fe-concentration) with nano as well as bulk form.
Under these conditions, the maximum cumulative hydrogen volume, hydrogen yield and maximum H2 production rate were 1.58 L H2 L−1 medium, 1.46 mol H2 mol−1 glucose and 25.7 mmol H2 g−1 cell dry weight (CDW) h−1, respectively.
The maximum cumulative hydrogen production from coconut milk wastewater was at initial pH 6.5 under mesophilic condition.
However, snack wastewater supported maximum cumulative hydrogen production, but it could not be used as the representative substrate because of the discontinuous biohydrogen production.
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The maximum predicted cumulative hydrogen production and COD reduction obtained under these conditions was 1.05 ml H2/ml POME and 31.71% respectively.
Subsequent verification experiments at optimal process values gave the maximum yield of cumulative hydrogen at 0.66 ± 0.07 ml H2/ml POME and COD reduction at 30.54 ± 9.85%.
Maximum cumulative H2 production (CHP) and hydrogen production rate (HPR) of 39.35 ml and 0.057 mmol/h was observed at 0.6 V.
The maximum cumulative dose over the first 24 h should not exceed 600 mg.
Studies with Rhodobacter sphaeroides O.U. 001 resulted in a cumulative hydrogen production of 492 ± 10 mL with maximum production rate of 11 mL L−1 h−1, substrate (malic acid) conversion efficiency of 44.4% and light conversion efficiency of 3.31%.
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