2012
DOI: 10.1016/j.ijhydene.2012.02.107
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Feasibility studies on continuous hydrogen production using photo-fermentative sequencing batch reactor

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Cited by 30 publications
(12 citation statements)
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“…The COD conversion coefficients are 1.5 g COD/g protein and 1.06 g COD/g carbohydrate . The measurement of SCFA was the same as described in the literature (Yuan et al, 2006), and the composition in biogas was analyzed by gas chromatograph equipped with a thermal conductivity detector according to the method documented in the literature (Xie et al, 2012;Wang et al, 2015). L-alanine was determined according to the method documented in the literature (Bergmeyer and Horder, 1980).…”
Section: 8mentioning
confidence: 99%
“…The COD conversion coefficients are 1.5 g COD/g protein and 1.06 g COD/g carbohydrate . The measurement of SCFA was the same as described in the literature (Yuan et al, 2006), and the composition in biogas was analyzed by gas chromatograph equipped with a thermal conductivity detector according to the method documented in the literature (Xie et al, 2012;Wang et al, 2015). L-alanine was determined according to the method documented in the literature (Bergmeyer and Horder, 1980).…”
Section: 8mentioning
confidence: 99%
“…Recently, biological hydrogen production processes, especially photo-fermentative hydrogen production by PFB has been attracting more and more attention, as it utilizes various renewable sources like biomass and sunlight to produce an ideal, renewable and carbon-free energy for the future [3]. However, it should be realized that most of photo-fermentative processes are based on suspended culture [4-6] in which it is difficult to achieve high biomass concentration, effective retention and separation of PFB biomass, resulting from poor flocculation of PFB [7]. For steady-state operation of photobioreactor, due to the poor flocculability, PFB cells cannot be efficiently separated from supernatant and rush out with effluent from reactor continuously.…”
Section: Introductionmentioning
confidence: 99%
“…And aerobic fluidized bed photo‐reactor compatible with the fluidization characteristics was designed for continuous hydrogen yielding (Ren et al ., ), which showed fairly stable and efficient hydrogen production. Moreover, sequencing batch (Xie et al ., ) and fed‐batch (Ren et al ., ) culture have been suggested as optimum operation modes due to high biomass retaining capacity, but have not been used widely in hydrogen production by photofermentation (Argun & Kargi, ). Therefore, enhancing the flocculation of PFB and using high biomass retaining operation modes are the promising strategies for maximum conversion of the feedstock into hydrogen.…”
Section: Resultsmentioning
confidence: 99%