Multiphase Bioreactor Design

(avery) #1

Scrit critical substrate concentration (kg.m−^3 )


Sf substrate concentration inside the biofilm (kg.m−^3 )


dimensionless concentration inside the biofilm (Sf^ /Si)


Si substrate concentration at the biofilm-liquid interface


Sox concentration of oxidant substance (kg.m−^3 )


Sred concentration of reductant substance (kg.m−^3 )


S 1 substrate concentration at reactor inlet (kg.m−^3 )


S 2 substrate concentration at reactor outlet (kg.m−^3 )


t time (s)


T temperature (°C)


VR reactor volume


(Xf)a active cell density in the biofilm (kg.m−^3 )


Xv cell density within the biofilm (kg.m−^3 )


y distance inside the biofilm measured from the liquid-biofilm interface (m)


y+ dimensionless distance in the biofilm (y/Lf)


Yf/s mass of dry biofilm (kg)


Z depth of the trickling filter (m)


Greek Symbols
α parameter defined by equation (33)


β degree of substrate penetration in the biofilm


ε reactor porosity


ø Thiele modulus


ηi biofilm internal efficiency


η biofilm efficiency based on external substrate concentration


λ external mass transfer rate/internal coupled diffusion-reaction rate


μ specific growth rate (s−^1 )


μmax maximum specific growth rate (s−^1 )


μp dry biofilm production rate per unit mass of biomass (s−^1 )


(μp)a specific dry biofilm production rate per unit mass of active biomass (s−^1 )


(μp)max maximum specific biofilm production rate (s−^1 )


ψ dimensionless observable modulus, defined in equation (34)


Biofilm reactors 321
Free download pdf