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- W2015095847 abstract "A mathematical model is proposed for the fluidized bed biofilm reactor (FBBR). For individual biofilm-covered particles (bioparticles) within the reactor, an analysis of intrabiofilm mass transfer and simultaneous intrinsic zero order reaction yields an effectiveness factor expression which is a function of the modified, zero order Thiele modulus, Φ0,m. This expression is linked to a one-dimensional reactor flow model and a fluidization model to yield an overall reactor model describing convective transport and simultaneous biochemical conversion of substrate within a FBBR. For Φ0,m<1.15, FBBR is mass transfer limited and 0.45 order kinetics are observed. For Φ0,m<1.15, mass transfer limitations are insignificant and intrinsic zero order kinetics are observed. A sensitivity analysis using the proposed mathematical model indicates that biofilm thickness and media size are the two most important operating parameters. These two parameters can be optimized simultaneously for a specific application. The proposed model provides a rational approach for FBBR design." @default.
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- W2015095847 date "1982-07-01" @default.
- W2015095847 modified "2023-09-23" @default.
- W2015095847 title "Mathematical model for the fluidized bed biofilm reactor" @default.
- W2015095847 doi "https://doi.org/10.1016/0141-0229(82)90043-6" @default.
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