2016
DOI: 10.1016/j.ijhydene.2016.06.236
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Effects of fluid dynamics on enhanced biohydrogen production in a pilot stirred tank reactor: CFD simulation and experimental studies

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Cited by 30 publications
(11 citation statements)
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“…There are a number of technologies which have been applied at lab-scale to dark fermentation by bacteria to decrease product inhibition by H 2 and significantly increase H 2 production. Research in this area is ongoing but examples of these technologies include particular mixing regimes [ 152 ], gas sparging [ 153 ], ultrasonication [ 154 ], gas separation by membranes [ 155 ], the maintenance of low-pressure fermentation environments [ 156 ] and electrochemical removal [ 157 ]. For example, Mizuno et al [ 153 ] demonstrated that the H 2 yield from anaerobic communities growing on glucose could be increased from 0.85 mol-H 2 mol-hexose −1 to 1.43 mol-H 2 mol-hexose −1 by using a flow of N 2 gas to continuously sparge the fermentation system.…”
Section: Emerging Opportunities For Industrial Biofuel Productionmentioning
confidence: 99%
See 1 more Smart Citation
“…There are a number of technologies which have been applied at lab-scale to dark fermentation by bacteria to decrease product inhibition by H 2 and significantly increase H 2 production. Research in this area is ongoing but examples of these technologies include particular mixing regimes [ 152 ], gas sparging [ 153 ], ultrasonication [ 154 ], gas separation by membranes [ 155 ], the maintenance of low-pressure fermentation environments [ 156 ] and electrochemical removal [ 157 ]. For example, Mizuno et al [ 153 ] demonstrated that the H 2 yield from anaerobic communities growing on glucose could be increased from 0.85 mol-H 2 mol-hexose −1 to 1.43 mol-H 2 mol-hexose −1 by using a flow of N 2 gas to continuously sparge the fermentation system.…”
Section: Emerging Opportunities For Industrial Biofuel Productionmentioning
confidence: 99%
“…Other investigators have reported comparable improvements to H 2 yields when sparging with CO 2 [ 158 ]. In another study by Niño-Navarro et al [ 152 ], it was reported that a selection between the use of two common impeller designs resulted in a greater than 2-fold increase in fermentative H 2 productivity which the authors attributed to mass transfer of H 2 gas from the liquid phase. More recently, Ramírez-Morales et al [ 155 ] successfully implemented the use of polymeric membranes to separate H 2 from the headspace gas created during fermentation by a microbial consortium native to tobacco wastewater.…”
Section: Emerging Opportunities For Industrial Biofuel Productionmentioning
confidence: 99%
“…The density of medium is 1000 kg/m 3 and the viscosity is 0.001 kg m −1 s −1 . Using the MRF approach and k−ϵ model, the 3D turbulent flow field has been modeled in this study by Ninõ-Navarro et al 78 CSTR on the pilot scale after Rushon and PB4 turbines for (C/D t = 0.5 and D i = 1) gave the highest yield of 1.8 mol H 2 per mol of glucose substrate and 440.63 mL/Lh of 31.6% purity for PB4 OC impeller. 78 The studies performed on axial pumping impellers demonstrated a greater yield of biohydrogen (88.4% of the theoretical value), as shown in Figure 11.…”
Section: Simulation Of Pilot Scale Cstrmentioning
confidence: 99%
“…For the PFR model, no backmixing happened and it was conducive to product diffusion . From the experimental scale to the productive scale, CFD simulation reflects the flow patterns and mass transfer of actual operations. , Recently, it was widely utilized to explain the complex physical phenomenon in biochemical reactors for wastewater treatment. , …”
Section: Introductionmentioning
confidence: 99%
“…21 From the experimental scale to the productive scale, CFD simulation reflects the flow patterns and mass transfer of actual operations. 26,27 Recently, it was widely utilized to explain the complex physical phenomenon in biochemical reactors for wastewater treatment. 26,28−31 ■ MATERIALS AND METHODS Reactor Construction.…”
Section: ■ Introductionmentioning
confidence: 99%