Page 22 - Separation process principles 2
P. 22

xxvi   Nomenclature


                                        x    mole fraction in liquid phase; mole fraction in   y   vector of mole fractions in vapor phase
                                             any phase; distance; mass fraction in raffinate;   Z   compressibility  factor = PuIRT;  total  mass;
                                             mass  fraction  in  underflow; mass fraction  of   height
                                             particles
                                                                             Zf   froth height on a tray
                                        x    normalized mole fraction = I    ZL   length of liquid flow path across a tray
                                                                                  lattice coordination number in UNIQUAC and
                                        x    vector of mole fractions in liquid phase
                                                                                  UNIFAC equations
                                        x,   fraction of crystals of size smaller than L
                                                                             z    mole fraction in any phase; overall mole frac-
                                        Y    mole or mass ratio; mass ratio of soluble mate-   tion in combinedphases; distance; overall mole
                                             rial  to  solvent  in  overflow;  pressure-drop   fraction  in  feed;  dimensionless  crystal  size;
                                             factor for packed columns defined by  (6-102);   length of liquid flow path across tray
                                             concentration  of  solute  in  solvent;  parameter
                                                                             z    vector of mole fractions in overall mixture
                                             in (9-34)
                                             mole fraction  in vapor  phase;  distance;  mass  Greek Letters
                                        y
                                             fraction  in extract;  mass fraction  in overflow

                  thermal diffusivity, ; relative volatility; surface area per adsorbed molecule

                                             ideal separation factor for a membrane   rnVIL; radiation wavelength
                                             relative  volatility of component i with respect   limiting ionic conductances of cation and anion, re-
                                             to  component  j  for  vapor-liquid  equilibria;   spectively
                                             parameter in NRTL equation
                                                                                  energy of interaction in Wilson equation
                                          energy-balance  parameters  defined  by  (10-23)  to
                                                                                  chemical potential or partial molar Gibbs free
                                             (10-26)
                                                                                  energy; viscosity
                                             relative selectivity of component i with respect
                                                                                  momentum diffusivity (kinematic  viscosity),  ;
                                             to component j for liquid-liquid  equilibria
                                                                                  wave frequency; stoichiometric coefficient
                                             film   flow   ratelunit   width   of   film;
                                                                                  number of functional groups of kind kin mole-
                                             thermodynamic  function  defined  by  (12-37)
                                                                                  cule i in UNIFAC method
                                             residual activity coefficient of functional group
                                                                                  fractional current efficiency; dimensionless dis-
                                             k in UNIFAC equation
                                                                                  tance in adsorption defined by (15-115); dimen-
                                             specific heat ratio; activity coefficient   sionless warped time in (1 1-2)
                                             change (final - initial)             osmotic pressure; product  of  ionic concentra-
                                             solubility  parameter;  film  thickness;  velocity   tions
                                             boundary layer thickness; thickness of the lam-
                                                                                  mass density
                                             inar sublayer in the Prandtl analogy
                                                                                  bulk density
                                             concentration boundary layer thickness
                                                                                  crystal density
                                             Kronecker delta
                                                                                  particle density
                                             exponent parameter in (3-40); fractional poros-
                                             ity; allowable error; tolerance in (10-31)   true (crystalline) solid density
                                             bed porosity (external void fraction)   surface  tension;  interfacial  tension;  Stefan-
                                                                                  Boltzmann constant = 5.671 x  lo-'  w/m2 K4
                                             eddy  diffusivity  for diffusion  (mass  transfer)
                                                                                  interfacial tension
                                             eddy diffusivity for heat transfer
                                                                                  interfacial tension between crystal and solution
                                             eddy diffusivity for momentum transfer
                                                                                  tortuosity; shear stress; dimensionless time  in
                                             particle porosity (internal void fraction)
                                                                                  adsorption defined by  (15-116); retention time
                                             Murphreevapor-phase plateefficiency in(10-73)
                                                                                  of  mother  liquor  in  crystallizer;  convergence
                                             area fraction in UNIQUAC and UNIFAC equa-   criterion in (10-32)
                                             tions; dimensionless concentration change de-
                                                                                  binary interaction parameter in NRTL equation
                                             fined  in  (3-80);  correction factor  in  Edmister
                                             group method; cut equal to permeate flow rate   shear stress at wall
                                             to  feed  flow  rate  for  a  membrane;  contact   v   number of ions per molecule
                                             angle;  fractional  coverage in Langmuir  equa-
                                                                             ,    volume  fraction;  parameter  in  Underwood
                                             tion; solids residence  time in  a dryer; root  of
                                                                                  equations (9-24) and (9-25)
                                             the Underwood equation, (9-28)
                                                                                  local  volume fraction  in the Wilson  equation
                                             average liquid residence time on a tray
                                                                                  probability function in the surface renewal theory
                                             Maxwell-Stefan  mass-transfer coefficient in  a
                                             binary mixture                       pure-species  fugacity  coefficient;  association
                                                                                  factor  in the Wilke-Chang equation;  recovery
                                             binary interaction parameter in Wilson equation
                                                                                  factor in absorption and stripping; volume frac-
                                                                                  lion;  concentration ratio  defined  by  (15-125)
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