Skip to main content
. 2021 Aug 11;11:16350. doi: 10.1038/s41598-021-95615-1

Table 6.

Comparison of hydrogen yields obtained in this study in continuous and batch mode with the ones reported in literature.

Process Operation mode HRT (h) Inoculum Substrate Zeolite Hydrogen yielda (mmol mmol−1) References
Dark fermentation Continuous 12 Granular sludge Glucose and arabinose (12.5 + 12.5 mM) 2.33 This study
6 0.19
6 Zeolite type 13X 0.53
Batch Granular sludge Glucose and arabinose (12.5 + 12.5 mM) 0.53 ± 0.02 This study
Zeolite type 13X 0.70 ± 0.03
Granular sludge Sargassum sp. 2.63 ± 0.03b
Zeolite type 13X 3.37 ± 0.16b
Continuous 8 Heat treated sludge granules Glucose and arabinose (12.5 + 12.5 mM) 0.77 ± 0.05 20
10 Granular sludge Glucose (13.8 mM) 0.80 ± 0.03 39
10 Granular sludge Arabinose (33.3 mM) 1.10 ± 0.01 39
Dark fermentation and AD Batch Caldicellulosiruptor saccharolyticus Sargassum sp. 91.30 ± 3.30c 3
Dark- and photo-fermentation Batch Heat-treated anaerobic sludge Arthrospira platensis wet biomass Natural zeolite 337d 13
Lactobacillus delbrueckii NBRC13953 and R. sphaeroides RV Glucose 7.10 40

ammole of H2 per mmole of substrate.

bH2 produced per mass of Sargassum sp. (in VS) (mmol g−1).

cVolume of H2 produced per mass of Sargassum sp. (in VS) (L kg−1).

dVolume of H2 produced per mass of cellular dry weight (in VS) (L kg−1).

emmol of H2 produced per bioreactor culture volume per hour of operation.