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The seed mixed microflora was obtained from a lab-scale agitated granular sludge bed bioreactor.
The time needed for full salt equilibrium with the bulk liquid took 1 min for small particles from the top of the sludge bed and up to 30 min for big granules from the bottom of the sludge bed.
Sludge bed development showed that sludge bed with high microbial activity was formed in the bottom and that the precipitation zone of effluents formed should preferably occupy 30% of the height of the IUSR.
Temperature effects on H2 production performance of a novel carrier-induced granular sludge bed (CIGSB) reactor were investigated.
In present study, the internal flow field of expanded granular sludge bed (EGSB) reactors was investigated using CFD simulation.
Biomethane production from the microalga Scenedesmus sp. AMDD was demonstrated in an upflow anaerobic sludge bed (UASB) reactor.
In a third phase the SRT was controlled by discharging biomass exclusively from the top of the sludge bed.
This phenomenon that salinity decreasing microbial diversity was also reported by other researchers that focused on granular sludge bed reactor (Miao et al. 2015).
Gross mixing distortions and localised stagnant zones, short-circuiting and bypass flows were found in the sludge bed and blanket zones for both extreme conditions (underloading and overloading).
The coupled model is verified and used to simulate the behavior of an expanded granular sludge bed (EGSB) reactor for biohydrogen production.
X-ray tomography is used to explore the structure evolution that a sludge bed undergoes in a convective pilot-scale fixed bed dryer.
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