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PF louvered-fin geometry

 

 

The procedure: 

 

CHX_Geom_PF_Louvered_Fin(TypeHX$: S_T, a_L, a_T, th_f, b, D_h, theta, beta, A_Fin\A)

 

Provides the geometric data associated with a plate finned - louvered-fin type compact heat exchanger surface.  These data are from Kays and London (1994).

 

Inputs:

The only input is the string identifying the geometry TypeHX$

 3/8-6.06:  'PF_louvered-fin_38_606'

 3/8(a)-6.06: 'PF_louvered-fin_38a_606'

  1/2-6.06: 'PF_louvered-fin_12_606'

  1/2(a)-6.06: 'PF_louvered-fin_12a_606'

  3/8-8.7: 'PF_louvered-fin_38_87'

  3/8(a)-8.7: 'PF_louvered-fin_38a_87'

  3/16-11.1: 'PF_louvered-fin_316_111'

   1/4-11.1: 'PF_louvered-fin_14_111'

  1/4(b)-11.1: 'PF_louvered-fin_14b_111'

  3/8-11.1: 'PF_louvered-fin_38_111'

  3/8(b)-11.1: 'PF_louvered-fin_38b_111'

  1/2-11.1: 'PF_louvered-fin_12_111'

  3/4-11.1: 'PF_louvered-fin_34_111'

  3/4(b)-11.1: 'PF_louvered-fin_34b_111'

 

Outputs:

S_T = transverse fin spacing (m or ft)

a_L = lateral length of a louver (m or ft)

a_T = transverse distance between adjacent louvers (m or ft)

th_f = thickness of fin material (m or ft)

b = plate gap (m or ft)

D_h = hydraulic diameter defined as 4 x minimum flow area x length/heat transfer area (m or ft)

theta = minimum flow area/frontal area for finned surface side only

beta = heat transfer area/volume (m^2/m^3 or ft^2/ft^3) for finned surface side only

A_fin\A = heat transfer area on fins/heat transfer area for finned surface side only

 

Example

$UnitSystem SI Mass J K Pa 

$VarInfo a_L units=m

$VarInfo a_T units=m

$VarInfo beta units=1/m

$VarInfo D_h units=m

$VarInfo S_T units=m

$VarInfo th_f units=m

TypeHX$= 'PF_louvered-fin_38a_87'

CALL CHX_Geom_PF_Louvered_Fin(TypeHX$: S_T, a_L, a_T, th_f, b, D_h, theta, beta, A_Fin\A)

 

{Solution:

S_T = 0.00292 [m]

a_L = 0.009525 [m]

a_T = 0.002032 [m]

th_f = 0.000152 [m]

b = 0.00635 [m]

D_h = 0.00365 [m]

theta = 0.9189 [-]

beta = 1007 [m^2/m^3]

A_Fin/A = 0.705}

 

Related procedures include:

Nondimensional Functions

Coefficient of Heat Transfer

Pressure Drop

 

 

Compact Heat Exchangers