output files

Execution of the s30.dat.txt benchmark dataset for laminar Reynolds number combined entry flow in a pipe yields a total of four output files.

s30.out.txt

This file is TEXSTAN's primary output file s30.out.txtpdf icon. The contents of this file have been reformatted and presented in the table below. A table of variable definitions is also presented (note: for this output file, kout=8 was used).

variable symbol definition
intg   integration step
x/dh/re (x/Dh)/ReDh (x divided by the hydraulic diameter) divided by the Reynolds number
cf*re cf * Re friction coefficient-Reynolds number product
uclr ucl /um centerline-to-mass-averaged velocity ratio
xplus 2(x/Dh)/(ReDhPr) two times x divided by the hydraulic diameter divided by the Reynolds number-Prandtl number product
nu Nu Nusselt number
th,cl (Tcl-Ts)/(Tm-Ts) ratio of the centerline-to-surface temperature difference to the mass-averaged-to-surface temperature difference
tm/ts Tm /Ts ratio of the mass averaged temperature to the surface temperature
ts Ts surface temperature
qflux qs" surface heat flux

intg x/dh/re cf*re uclr xplus nu th,cl tm/ts ts qflux
TEXSTAN: July 2007
5 .00003 137.95 1.037 .00007 57.858 1.018 .968 3.100E+02 2.160E+02
50 .00025 55.81 1.104 .00071 20.239 1.058 .969 3.100E+02 7.273E+01
100 .00050 43.41 1.144 .00143 14.833 1.084 .970 3.100E+02 5.202E+01
150 .00092 35.35 1.192 .00264 11.365 1.118 .971 3.100E+02 3.864E+01
200 .00206 27.77 1.280 .00589 8.155 1.188 .973 3.100E+02 2.608E+01
250 .00510 22.11 1.429 .01456 5.815 1.335 .976 3.100E+02 1.655E+01
300 .01240 18.63 1.652 .03543 4.441 1.585 .980 3.100E+02 1.028E+01
350 .02392 17.06 1.839 .06835 3.897 1.746 .985 3.100E+02 6.891E+00
400 .04137 16.33 1.947 .11819 3.708 1.794 .990 3.100E+02 4.506E+00
450 .06550 16.07 1.986 .18714 3.665 1.799 .994 3.100E+02 2.688E+00
500 .09050 16.01 1.995 .25857 3.659 1.799 .996 3.100E+02 1.595E+00
519 .10000 16.01 1.996 .28571 3.658 1.798 .997 3.100E+02 1.309E+00

s30.ftn82.txt

The file s30.ftn82.txtpdf icon has been reformatted and presented in the table below, along with a definitions of the output variables.

variable symbol definition
intg   integration step
x/dh (x /Dh) x divided by the hydraulic diameter
htc h heat transfer coefficient
umean um mass-averaged velocity
nu Nu Nusselt number

intg x/dh htc umean nu
TEXSTAN: July 2007
5 2.5000001E-02 2.1989E+01 2.2498E-01 5.7858E+01
20 1.0000000E-01 1.1703E+01 2.2498E-01 3.0792E+01
40 2.0000000E-01 8.5138E+00 2.2498E-01 2.2402E+01
... ... ... ... ...
480 8.0500000E+01 1.3910E+00 2.2498E-01 3.6601E+00
500 9.0500000E+01 1.3906E+00 2.2498E-01 3.6588E+00
519 1.0000000E+02 1.3903E+00 2.2498E-01 3.6583E+00

s30.ftn84.txt

The file s30.ftn84.txtpdf icon has been reformatted and presented in the table below, along with a definitions of the output variables.

variable symbol definition
intg   integration step
x/dh (x /Dh) x divided by the hydraulic diameter
htc h heat transfer coefficient
qflux qs" surface heat flux
tm Tm mass-averaged temperature
ts Ts surface temperature

intg x/dh htc qflux tm ts
TEXSTAN: July 2007
5 2.5000001E-02 2.1989E+01 2.1596E+02 3.0018E+02 3.1000E+02
20 1.0000000E-01 1.1703E+01 1.1298E+02 3.0035E+02 3.1000E+02
40 2.0000000E-01 8.5138E+00 8.0992E+01 3.0049E+02 3.1000E+02
... ... ... ... ... ...
480 8.0500000E+01 1.3910E+00 1.9646E+00 3.0859E+02 3.1000E+02
500 9.0500000E+01 1.3906E+00 1.5951E+00 3.0885E+02 3.1000E+02
519 1.0000000E+02 1.3903E+00 1.3089E+00 3.0906E+02 3.1000E+02

s30.ftn85.txt

The file s30.ftn85.txtpdf icon has been reformatted and presented in the table below, along with a definitions of the output variables.

variable symbol definition
x/dh (x/Dh) x divided by the hydraulic diameter
tauw(I) τs surface shear stress (I-surface)
tauw(E) τs surface shear stress (E-surface)
cf2(I) cf /2 friction coefficient divided by 2 (I-surface)
cf2(E) cf /2 friction coefficient divided by 2 (I-surface)
delp ΔP pressure drop (reference is initial pressure at entrance, po)

x/dh tauw(I) tauw(E) cf2(I) cf2(E) delp
TEXSTAN: July 2007
2.5000001E-02 0.000E+00 4.108E-03 0.000E+00 6.898E-02 2.1805E-03
1.0000000E-01 0.000E+00 2.370E-03 0.000E+00 3.979E-02 4.1316E-03
2.0000000E-01 0.000E+00 1.808E-03 0.000E+00 3.036E-02 5.7891E-03
... ... ... ... ... ...
8.0500000E+01 0.000E+00 4.772E-04 0.000E+00 8.012E-03 1.9179E-01
9.0500000E+01 0.000E+00 4.768E-04 0.000E+00 8.006E-03 2.1090E-01
1.0000000E+02 0.000E+00 4.766E-04 0.000E+00 8.003E-03 2.2903E-01

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