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Mathematical Modeling and Simulation for Production of MTBE

Mathematical Modeling and Simulation for Production of MTBE

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Nomenclature<br />

Symbol Definition Units<br />

A, B,<br />

<strong>and</strong> C<br />

Antoine’s coefficient [−]<br />

A , B ,<br />

<strong>and</strong> C<br />

Ideal vapor enthalpy coefficient [−]<br />

a Activity [−]<br />

a<br />

ij<br />

a ,b , c ,<br />

<strong>and</strong> d<br />

Non-temperature dependent energy parameter<br />

between components i <strong>and</strong> j<br />

VIII<br />

[J/mol]<br />

enthalpy coefficient [−]<br />

bij Temperature dependent energy parameter<br />

between components i <strong>and</strong> j<br />

[J/mol. k]<br />

c Number <strong>of</strong> component [−]<br />

Cp Specific heat <strong>of</strong> a component [kJ/kg. ْ◌ C]<br />

Da Damkohler number ( H rref. /V) [−]<br />

2<br />

Ð Maxwell Stefan diffusivity [mP P/s]<br />

D Distillate flow rate [ mol/hr]<br />

F Feed molar flow rate [mol/hr]<br />

f Fugacity [pa]<br />

h Liquid phase enthalpy [J/mol]<br />

H Vapor phase enthalpy [J/mol]<br />

H molar holdup [ mol/hr]<br />

I Component identification number [-]<br />

J Stage identification number [-]<br />

K thermodynamic equilibrium coefficient<br />

[−]<br />

L 1BMolar flow rate <strong>of</strong> liquid [mol/hr]<br />

m Material balance summation [mol]<br />

Mwi Molecular weight <strong>of</strong> component i [mol/kg]<br />

N Interfacial mass transfer [mol/hr]<br />

Number <strong>of</strong> components <strong>of</strong> a mixture<br />

[−]<br />

NC<br />

n<br />

Pt<br />

Number <strong>of</strong> trays<br />

Total pressure [pa]<br />

[−]

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