2004
DOI: 10.1016/j.bej.2004.02.009
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Determination of the optimal operational parameters for a three-phase fluidised bed bioreactor with a light biomass support when used in treatment of phenolic wastewaters

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Cited by 20 publications
(13 citation statements)
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“…In a reactor with low density particles, fluidisation can be conducted either by an upward cocurrent flow of gas and liquid through a bed or by a downward flow of liquid and countercurrent upward flow of gas ( Fig. 1) [1,8]. In the former, fluidisation is achieved by an upward flow of gas whereby the gas bubbles make the bed expanding downwards into the less dense mixture of gas and liquid [1,8].…”
Section: Introductionmentioning
confidence: 98%
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“…In a reactor with low density particles, fluidisation can be conducted either by an upward cocurrent flow of gas and liquid through a bed or by a downward flow of liquid and countercurrent upward flow of gas ( Fig. 1) [1,8]. In the former, fluidisation is achieved by an upward flow of gas whereby the gas bubbles make the bed expanding downwards into the less dense mixture of gas and liquid [1,8].…”
Section: Introductionmentioning
confidence: 98%
“…1) [1,8]. In the former, fluidisation is achieved by an upward flow of gas whereby the gas bubbles make the bed expanding downwards into the less dense mixture of gas and liquid [1,8]. In the latter, the bed is fluidised by a downward flow of a liquid counter to the net buoyancy force of the particles [7,9,10].…”
Section: Introductionmentioning
confidence: 98%
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