2017
DOI: 10.1016/j.bej.2016.11.019
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Hydrodynamics and mass transfer in bubble column, conventional airlift, stirred airlift and stirred tank bioreactors, using viscous fluid: A comparative study

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Cited by 79 publications
(36 citation statements)
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“…Stirred tanks are predominantly used, due to their operability and ease of manufacturing. However, the impeller-mediated mixing can induce very high shear stresses on the cells [ 65 ], which is why many CM startups turn to rocking platform BRs, that causes lower shear stress, due to gentle wave-like fluid motion in the cellbag [ 66 ]. Other promising candidates include hollow fiber [ 8 ] and air-lift [ 67 ] bioreactors, but also modifications of the conventional stirred tank and rocking platform BRs, such as by other methods for inducing the wave-motion, e.g., by using a horizontal displacement in combination with a rocking motion, which can increase the mass transfer capacity [ 68 ].…”
Section: Bioreactors and Scaffoldingmentioning
confidence: 99%
“…Stirred tanks are predominantly used, due to their operability and ease of manufacturing. However, the impeller-mediated mixing can induce very high shear stresses on the cells [ 65 ], which is why many CM startups turn to rocking platform BRs, that causes lower shear stress, due to gentle wave-like fluid motion in the cellbag [ 66 ]. Other promising candidates include hollow fiber [ 8 ] and air-lift [ 67 ] bioreactors, but also modifications of the conventional stirred tank and rocking platform BRs, such as by other methods for inducing the wave-motion, e.g., by using a horizontal displacement in combination with a rocking motion, which can increase the mass transfer capacity [ 68 ].…”
Section: Bioreactors and Scaffoldingmentioning
confidence: 99%
“…El uso de biorreactores con agitación neumática ha resultado más eficiente ya que la agitación mecánica provoca un mayor esfuerzo de corte, y por lo tanto, la ruptura de los filamentos, provocando así la disminución de la actividad enzimática (Ahamed y Vermette, 2010). Es por ello que se han enfocado las investigaciones en el campo de la biotecnología de hongos utilizando biorreactores air-lift que favorecen la transferencia de masa, disminuyen el esfuerzo de corte, y minimizan el consumo de energía (Fontana et al, 2009;Mahmood et al, 2015;de Jesús et al, 2017), además, favorecen la formación de pellets que permiten periodos prolongados de producción de celulasas con biomasa fúngica retenida (Callow et al, 2016). En la Fig.…”
Section: Diseño De Bioprocesos Para La Producción De Biomasa Y Metabounclassified
“…The system heat load includes the heat loss of the slurry tank and MFD, and the heat load of slurry, which requires heating to reach the target digestion temperature. By neglecting the bio-heat and the heat removed by the biogas, the total heat demand can be expressed as [33]: (9) where QS is the heat required by the operation of the dynamic anaerobic digestion system, kW; QDemand is the heat duty from the dynamic anaerobic digestion system, kW; Q1 is the heat required for heating the biomass digestive fluid, kW; and Q2 is the heat loss from the MFD and slurry tank, kW.…”
Section: System Heat Load Calculationmentioning
confidence: 99%
“…De Jesus et al evaluated the hydrodynamic mass transfer of four bioreactors using a viscous Newtonian and non-Newtonian fluid. It was concluded that mechanical mixing has higher mass transfer coefficients and provides a better homogeneity of the digester contents [9]. Trad et al compared the three mixing methods and found that the mixing energy level (MEL) for mechanical mixing was the highest.…”
Section: Introductionmentioning
confidence: 99%