2017
DOI: 10.1016/j.applthermaleng.2017.05.153
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Exergetic and economic evaluation of incorporation of hydrogen production in a cassava wastewater plant

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Cited by 23 publications
(11 citation statements)
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“…[17]. Livestock manure 13.9 [16] 110 [18] 80 [18] 140 [18] Cassava 19 [17] 250 [19] 70 [19] 30 [19] The biodigester produced gas with an average concentration of 62% and the accumulation of biogas volume was 115,776 cm 3 . The Figure 3 shows the volume of biogas produced during the HRT.…”
Section: Resultsmentioning
confidence: 99%
“…[17]. Livestock manure 13.9 [16] 110 [18] 80 [18] 140 [18] Cassava 19 [17] 250 [19] 70 [19] 30 [19] The biodigester produced gas with an average concentration of 62% and the accumulation of biogas volume was 115,776 cm 3 . The Figure 3 shows the volume of biogas produced during the HRT.…”
Section: Resultsmentioning
confidence: 99%
“…Simulation of the biological processes of AD and DF was performed in Aspen Plus V9 software, the Soave-Redlich-Kwong (SRK) method was chosen as it correlates and calculates the mole fractions and activity coefficients. In addition, the SRK model is suitable for vapor-liquid equilibrium (VLE) (Madeira et al, 2017). The starting point for the simulation of AD was the ADM1 model, which relates the stoichiometric equations for the stages of hydrolysis, acidogenesis, acetogenesis, and methanogenesis (Serrano, 2010).…”
Section: Model Development and Simulation Designmentioning
confidence: 99%
“…These differences in biogas production yields are probably primarily related to the different compositions of proteins, fats, and carbohydrates considered for CFM and SM (Table 1). Higher carbohydrate content of CFM resulted in higher H 2 production yields for blend 7, as carbohydrates represent the most suitable substrate for DF (pathways n°39 and 40, Supplementary Table S2), whereas higher protein content of SM resulted to lower C/N ratios that may inhibit DF as described by the ammonia inhibition modules integrated into the model (Madeira et al, 2017;Serrano, 2011). These results are in good agreement with the findings of previous experimental studies (Zhu et al, 2008;Ghimire et al, 2015), which have indicated that low C/N ratio and high concentration of ammonium ion (NH 4 + ) inhibit H 2 production during DF when SM is used as the only substrate, with maximum production yields of 3.65 ml H 2 •VS −1 .…”
Section: Simulated Biogas Production Performancesmentioning
confidence: 99%
“…There are many studies addressing exergy analysis of hydrogen production by steam reforming, 20‐22 the main difference of the study presented in this study in relation to the studies described in the literature is the crossing of different biogas (different concentrations of methane), that allows an analysis that relates the production of hydrogen with the input biogas, showing how the variation of hydrogen is related to input biogas in the steam reforming, pointing out ways to improve the exergy efficiency of the plant, enabling improvements in the production potential of hydrogen.…”
Section: Introductionmentioning
confidence: 99%