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Basic Models of Computational Mass Transfer

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Introduction to Computational Mass Transfer

Part of the book series: Heat and Mass Transfer ((HMT))

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Abstract

The computational mass transfer (CMT) aims to find the concentration profile in a process equipment, which is the most important basis for evaluating the process efficiency, as well as, the effectiveness of an existing mass transfer equipment. This chapter is dedicated to the description of the fundamentals and the recently published models of CMT for obtaining simultaneously the concentration, velocity and temperature distributions. The challenge is the closure of the differential species conservation equation for the mass transfer in turbulent flow. Two models are presented. The first is a two-equation model termed as \(\overline{{c^{\prime 2} }} - \varepsilon_{{c^{\prime}}}\) model, which is based on the Boussinesq postulate by introducing an isotropic turbulent mass transfer diffusivity. The other is the Reynolds mass flux model, in which the variable covariant term in the equation is modeled and computed directly, and so it is anisotropic and rigorous. Both methods are proved to be validated by comparing with experimental data.

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Abbreviations

\({c}\) :

Instantaneous mass concentration of species \(i\), kg m−3

Molar concentration of species \(i\) in Sect. 1.4.2, mol s−3

\({c}_{\text{t}}\) :

Total molar concentration of component i per m3, mol m−3

C :

Time average concentration, kg m−3

C + :

Dimensionless concentration

c′:

Fluctuating concentration, kg m−3

\(\overline{{{c}^{\prime 2} }}\) :

Variance of fluctuating concentration, kg2 m−6

D :

Molecular diffusivity, m2 s−1

D e :

Effective mass diffusivity, m2 s−1

D t :

Isotropic turbulent mass diffusivity, m2 s−1

\({\mathbf{D}}_{\text{t}}\) :

Anisotropic turbulent mass diffusivity, m2 s−1

g :

Gravity acceleration, m s−2

[I]:

Identity matrix, dimensionless

J w :

Mass flux at wall surface, kg m−2 s−1

k :

Fluctuating kinetic energy, m2 s−2

Mass transfer coefficient, m s−1

[k]:

Matrix of mass transfer coefficients, m s−1

l :

Characteristic length, m

p′:

Fluctuating pressure, kg m−1 s−2

P :

Time average pressure, kg m−1 s−2

Pe:

Peclet number

r c :

Ratio of fluctuating velocity dissipation time and fluctuating concentration dissipation time

S :

Source term

Sc :

Schmidt number

Sc t :

Turbulent Schmidt number

t :

Time, s

\(T^{\prime}\) :

Fluctuating temperature, K

\(\overline{{T^{\prime 2} }}\) :

Variance of fluctuating temperature, K2

T :

Time average temperature, K

u :

Instantaneous velocity of species i, m s−1

u′:

Fluctuating velocity, m s−1

u τ :

Frictional velocity, m s−1

u + :

Dimensionless velocity, m s−1

U, V, W :

Time average velocity in three directions, m s−1

y + :

Dimensionless distance, m

α t :

Turbulent thermal diffusivity, m−1 s−1

δ :

Thickness of fluid film, m

ε :

Dissipation rate of turbulent kinetic energy, m2 s−3

ε c′ :

Dissipation rate of concentration variance, kg2 m−6 s−1

ε t :

Dissipation rate of temperature variance, K2 s−1

μ :

Viscosity, kg m−1 s−1

μ t :

Turbulent viscosity, kg m−1 s−1

\(\nu_{\text{e}}\) :

Effective turbulent diffusivity, m2 s−1

ρ :

Density, kg m−3

τ μ , τ c , τ m :

Characteristic time scale, s

τ w :

Near wall stress, kg m−1 s−2

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Authors and Affiliations

  1. School of Chemical Engineering and Technology, Tianjin University, Tianjin, People’s Republic of China

    Kuo-Tsung Yu & Xigang Yuan

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  1. Kuo-Tsung Yu
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Correspondence to Kuo-Tsung Yu .

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Yu, KT., Yuan, X. (2017). Basic Models of Computational Mass Transfer. In: Introduction to Computational Mass Transfer. Heat and Mass Transfer. Springer, Singapore. https://doi.org/10.1007/978-981-10-2498-6_1

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  • DOI: https://doi.org/10.1007/978-981-10-2498-6_1

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  • Online ISBN: 978-981-10-2498-6

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