2001
DOI: 10.1016/s0304-386x(00)00161-4
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The design of bioreactors

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Cited by 43 publications
(15 citation statements)
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“…Conventional STRs are prone to impeller flooding, a phenomenon characterized by gas rapidly flowing axially upwards past the impeller with no radial discharge, and the formation of stagnant zones [98,99]. There are also other acknowledged limitations when using STRs including gas channelling, resulting in reduced gas dissolution and poor bulk mixing [17,100]. This requires implementation of different scale-up strategies depending on the specific bioprocess [101,102].…”
Section: Barriersmentioning
confidence: 99%
“…Conventional STRs are prone to impeller flooding, a phenomenon characterized by gas rapidly flowing axially upwards past the impeller with no radial discharge, and the formation of stagnant zones [98,99]. There are also other acknowledged limitations when using STRs including gas channelling, resulting in reduced gas dissolution and poor bulk mixing [17,100]. This requires implementation of different scale-up strategies depending on the specific bioprocess [101,102].…”
Section: Barriersmentioning
confidence: 99%
“…The rotating drum bioreactor (Biorotor) [157,158] is a baffled cylindrical barrel with an aeration inlet (CO2 and O2) at one end and an air outlet at the other end. The cylinder sits on rollers and during rotation the baffles lift solids and then discharge them to fall through the solution, maximising mixing, eliminating "dead" zones and minimising shear stresses on bacterial cells.…”
Section: Technology Developmentsmentioning
confidence: 99%
“…The cylinder sits on rollers and during rotation the baffles lift solids and then discharge them to fall through the solution, maximising mixing, eliminating "dead" zones and minimising shear stresses on bacterial cells. Tests carried out with 30% solids suspension of pyrite yielded solubilisation rates an order of magnitude greater than thought possible [158]. The rotating bioreactor has attracted recent attention with the development of a modified continuous reactor capable of processing a 40% solids suspension [159].…”
Section: Technology Developmentsmentioning
confidence: 99%
“…Sin embargo, operar con densidades de pulpa mayores al 20% en reactores de tanque agitado no ha tenido buenos resultados (Rossi, 2001;Deveci, 2004) debido a un excesivo número de partículas de mineral para un inóculo de tamaño constante, ya que la fricción entre las partículas disminuye la relación bacteria/sólido y la velocidad de solubilización; debido a que estos factores causan daño celular y limitan las velocidades de transferencia de oxígeno incrementando a su vez el tiempo de biooxidación (Hansford et. al., 1995, Rossi, 2001Deveci, 2004;Arroyave, 2008).…”
Section: Introductionunclassified