from ollin.Administrator.AdmOllin import Ollin
from numpy.oldnumeric import array
RK = Ollin.AddModel("PR", "PR", "ANTOINE")
Ollin.Add([
"METHANOL", "HYDROGEN", "CARBON MONOXIDE", "CARBON DIOXIDE", "WATER",
"METHANE"
], "PR")
S1 = Ollin.AddCase("S1") #Alimentacion al compresor
S1.SetX([0, 69, 21, 7, 0, 3])
S1.T(25 + 273.15)
S1.P(101.325 * 1)
Ollin.Solve("S1") #Caculamos S1
Ollin.Resumen("S1")
##print S1.Get("H")
S2 = Ollin.AddCase("S2") #salida del compresor
S2.SetX(S1.Get("x"))
S2.H(S1.Get("H")) #Considerando que es adiabatico dQ=0
S2.P(101.325 * 20)
Ollin.Solve("S2") #Caculamos S2
Ollin.Resumen("S2")
#Salida del calentador
S3 = Ollin.AddCase("S3") #Alimentacion al ractor
S3.SetX(S2.Get("x"))
S3.T(400 + 273.15)
S3.P(S2.Get("P"))
Ollin.Solve("S3")
#La reaccion se realiza en fase gas adiabaticamente dQ=0
S1.SetX([1, 1, 1])
S1.T(322)
plot_x = range(10, 1000, 10)
plot_y0 = []
plot_y1 = []
plot_y2 = []
plot_y3 = []
plot_y4 = []
##plot_y5 = []
Pr = []
print plot_x
for P in plot_x:
S1.P(P)
Ollin.Solve()
yf = S1.Get("Ki")
plot_y0.append(yf[0])
plot_y1.append(yf[1])
plot_y2.append(yf[2])
## plot_y3.append( yf[3] )
## plot_y4.append( yf[4] )
## plot_y5.append( S1.Get("FracVap") )
Pr.append(P)
## print adm.TheObj["Str"].Prop["FracVap"],adm.TheObj["Str"].Prop["T"]
##print "PC",S1.Get("PC")
##print Pr
plot(Pr, plot_y0)
plot(Pr, plot_y1)
from ollin.Administrator.AdmOllin import Ollin
from numpy.oldnumeric import array,power,pi
PR=Ollin.AddModel("PR","PR")
Ollin.Add(["HYDROGEN","METHANE","BENZENE","TOLUENE","DIPHENYL",],"PR")
S1=Ollin.AddCase("S1")#Alimentacion al compresor
S1.SetX([0.366021,0.548913,0.062618,0.021503,0.000945])
S1.T(38+273.15)
##S1.FracVap(0.9)
S1.P(3206.062)
Ollin.Solve("S1")#Caculamos S1
Ollin.Resumen("S1")
L = (1-S1.Get("FracVap"))*1919.605
Gv = (L*S1.Get("MolWt_l"))/( S1.Get("LiqDen")*60 )
Vr = Gv*5
Lon = power((256*Vr/pi),0.333333)
Dia = Lon/4
print "Longuitud", Lon
print "Diametro",Dia