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Código de visual Basic

nestor.fcqPráctica o problema20 de Octubre de 2017

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Option Explicit

Option Base 1

Public Const B2kP As Double = 100

Function tvsat(P) As Double

Dim A0 As Double, A1 As Double, a2 As Double, a3 As Double, a4 As Double, a5 As Double, a6 As Double, a7 As Double, lnp As Double

A0 = -20.69171

A1 = 13.610819

a2 = 7.50043

a3 = -0.37146631

a4 = 0.26070017

a5 = -0.0240092

a6 = 0.0013378831

a7 = -8.9845187E-33

lnp = Log(P * B2kP * a2)

tvsat = A0 + A1 * lnp + a3 * lnp ^ 2 + a4 * lnp ^ 3 + a5 * lnp ^ 4 + a6 * lnp ^ 5 + a7 * lnp ^ 30

tvsat = tvsat + 273.15

End Function

Function Psat(tvsat) As Double

Dim B0 As Double, B1 As Double, b2 As Double, b3 As Double, b4 As Double

B0 = 98.0904

B1 = 21.675595

b2 = -0.017091984

b3 = -6249.2

b4 = 0.000010643944

Psat = B0 * Exp(B1 + b2 * (tvsat) + b3 / (tvsat) + b4 * (tvsat) ^ 2)

Psat = Psat / B2kP

End Function

Function hliq(P) As Double

Dim C0 As Double, C1 As Double, c2 As Double, c3 As Double, c4 As Double, c5 As Double, c6 As Double, c7 As Double, c8 As Double, c9 As Double

C0 = -38196.597

C1 = 8156.7769

c2 = 0.062913098

c3 = 5.9407557E-13

c4 = 1.1973266E-59

c5 = 135722.09

c6 = -170161.83

c7 = 66738.664

c8 = -2246.77

c9 = 402.37285

P = P * B2kP / 98.0904

hliq = C0 + C1 * (P) ^ 0.1 + c2 * (P) ^ 1.5 + c3 * (P) ^ 6 + c4 * (P) ^ 26 + c5 / (P) ^ 0.1 + c6 / (P) ^ 0.15 + c7 / (P) ^ 0.2 + c8 / (P) ^ 0.4 + c9 / (P) ^ 0.5

End Function

Function hvsat(P) As Double

Dim D0 As Double, D1 As Double, d2 As Double, d3 As Double, d4 As Double, d5 As Double, d6 As Double, d7 As Double, d8 As Double, d9 As Double

D0 = 16394.097

D1 = -2326.9083

d2 = -0.12038685

d3 = -1.11011E-13

d4 = -1.2893239E-59

d5 = -46574.48

d6 = 54360.668

d7 = -19508.785

d8 = 368.64023

d9 = -38.23317

P = P * B2kP / 98.0904

hvsat = D0 + D1 * (P) ^ 0.1 + d2 * (P) ^ 1.5 + d3 * (P) ^ 6 + d4 * (P) ^ 26 + d5 / (P) ^ 0.1 + d6 / (P) ^ 0.15 + d7 / (P) ^ 0.2 + d8 / (P) ^ 0.4 + d9 / (P) ^ 0.5

End Function

Public Function DT(Tent) As Double

Dim ValorCelda1 As Double, ValorCelda2 As Double

ValorCelda1 = Worksheets("propiedades").Range("B2").Value                  'Temperatura inicial

ValorCelda2 = Worksheets("propiedades").Range("B4").Value                 'Tv sat

 

DT = ValorCelda1 - ValorCelda2                      'DEFINIR CELDAS

If DT >= 0 Then

DT = DT

ElseIf DT < 0 Then

DT = 0

End If

End Function

Public Function Fact(P) As Double

Dim e() As Variant

Dim f() As Variant

Dim g() As Variant

Dim h() As Variant

Dim Z() As Variant

Dim j() As Variant

Dim K() As Variant

Dim l() As Variant

Dim m() As Variant

Dim n() As Variant

Dim o() As Variant

Dim y As Double

f(1) = 1.3051623:         f(2) = -0.0042356094:     f(3) = 4.755113:          f(4) = 0.0000033460062:       f(5) = -0.0047564201:     f(6) = 0.090788927

g(1) = -0.17902741:       g(2) = -0.0017548594:     g(3) = 1.9129151:         g(4) = 0.0000013486553:       g(5) = -0.0019127371:     g(6) = 0.033372795

h(1) = 0.0070375183:      h(2) = 0.000063713237:    h(3) = -0.067828775:      h(4) = -0.000000048269714:    h(5) = 0.000067821775:    h(6) = -0.0012414538

Z(1) = -0.00016133576:    Z(2) = -0.0000014687338:  Z(3) = 0.0015400988:      Z(4) = 1.1192714E-09:         Z(5) = -0.0000015399384:  Z(6) = 0.00002855647

j(1) = 0.000001828274:    j(2) = 0.000000016671918: j(3) = -0.000016788785:   j(4) = -1.2747094E-11:        j(5) = 0.000000016786967: j(6) = -0.00000032387253

K(1) = -9.2397816E-09:    K(2) = -8.4526863E-11:    K(3) = 0.000000081538461: K(4) = 6.4869756E-14:         K(5) = -8.1529273E-11:    K(6) = 1.6395529E-09

l(1) = 1.6794938E-11:     l(2) = 1.5433165E-13:     l(3) = -1.4013435E-10:    l(4) = -1.1907966E-16:        l(5) = 1.4011765E-13:     l(6) = -2.9868728E-12

m(1) = 0.060726062:       m(2) = 0.00051064489:     m(3) = -0.5476973:        m(4) = -0.00000036934366:     m(5) = 0.0005476369:      m(6) = -0.01035083

n(1) = -0.00056957354:    n(2) = -0.0000047956662:  n(3) = 0.0051488159:      n(4) = 3.4673021E-09:         n(5) = -0.0000051482494:  n(6) = 0.000097125868

o(1) = 0.88778641:        o(2) = 0.0060101547:      o(3) = -6.2985134:        o(4) = -0.0000042275055:      o(5) = 0.0062976297:      o(6) = -0.12744559

P = P / 1.01972

For y = 1 To 6

e(y) = f(y) + g(y) * P + h(y) * (P) ^ 2 + Z(y) * (P) ^ 3 + j(y) * (P) ^ 4 + K(y) * (P) ^ 5 + l(y) * (P) ^ 6 + (m(y) / P) + (n(y) / (P) ^ 2) + o(y) * (P) ^ 0.5

Next y

Fact = e(1) + e(2) * DT + e(3) / DT + e(4) * (DT) ^ 2 + e(5) / (DT) ^ 2 + e(6) * (DT) ^ 0.5

End Function

Function HVapSCAgua(HVapSatAgua) As Double

HVapSCAgua = HvsatAgua + Fact * (DT)                  'Introducir HvsatAgua

End Function

Function SL(P) As Double

Dim AL As Double, BL  As Double, CL  As Double, DL  As Double, EL  As Double, FL  As Double, GL  As Double

AL = -0.000167772

BL = 0.004272688

CL = 0.01048048

DL = 0.05801509

EL = 0.00000009101291

FL = -0.000000000027592

GL = 0.11801

P = P * 14.5038            'Conversion de bar a psia

SL = AL * P + BL / P + CL * (P) ^ 0.5 + DL * Log(P) + EL * (P) ^ 2 + FL * (P) ^ 3 + GL

SL = SL * 4.1868            'KJ/Kg*K

End Function

Function SV(P) As Double

Dim AV As Double, BV  As Double, CV  As Double, DV  As Double, EV  As Double, FV  As Double, GV  As Double

AV = -0.0001476933

BV = 0.0012617946

CV = 0.00344201

DV = -0.08494128

EV = 0.0000000689138

FV = -0.000000000024941

GV = 1.97364

P = P * 14.5038 'Conversion de bar a psia

SV = AV * P + BV / P + CV * (P) ^ 0.5 + DV * Log(P) + EV * (P) ^ 2 + FV * (P) ^ 3 + GV 'Unidadades PSIA/Lb °R

SV = SV * 4.1868    'KJ/Kg*K

End Function

Public Function Tprom(T)

Dim ValorCelda5 As Double

ValorCelda5 = Worksheets("propiedades").Range("B4").Value     'Tsat

Tprom = (T * ValorCelda5) ^ 0.5

End Function

Function SSc()

SSc = SVapSatAgua + (HVapSCAgua - HVapSatAgua) / Tprom

End Function

'tension sup agua

Function Ts(T) As Double

T = 1.8 * (T - 273) + 32   '°F

Ts = 79.5118 - 0.09605 * T

End Function

' conductividad agua

Function K(T)

T = (T - 273)

K = 0.31431 + 0.00047673 * T

K = K * (1.05506 * 3.281)

End Function

'Viscosidad agua

Function v(T)

T = 1.8 * (T - 273) + 32

v = 62.233 / T

End Function

' Densidad agua

Function D(T)

Dim dref As Double

T = 1.8 * (T - 273) + 32

dref = 0.997375 + 0.00012 * T - 0.000001601 * (T) ^ 2 + 0.000000001601 * (T) ^ 3

D = 62.47 * (dref)

D = D * (0.453592 / 28.3168)

...

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