import sys
sys.path.append("/Users/jonathanxavier/Developer/sim42")
from ollin.Administrator.AdmOllin import Ollin
from pylab import *
RK = Ollin.AddModel("RK", "RK")
S1 = Ollin.AddCase("S1")
Ollin.Add(["N-BUTANE", "N-PENTANE", "N-HEXANE"], "RK")
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] )
import sys
sys.path.append("/Users/jonathanxavier/Developer/sim42")
from ollin.Administrator.AdmOllin import Ollin
from ollin.Example.UOS import Stream, Valve,Heater,Flash
PR=Ollin.AddModel("PR","PR")
Ollin.Add(["METHANE","ETHANE","PROPANE","ISOBUTANE","N-BUTANE","N-PENTANE","N-HEXANE","N-HEPTANE"],"PR")
Ollin.LoadConst()
S1 = Stream(PR)
S1.X([14520,9070,7260,770,2810,950+1630,1540,3180])
##S1.FracVap(0.9)
S1.T(273.15+40)
S1.P(500)
S1.Mol(455)
V1 = Valve(PR)
V1.DP = 11030
H1 = Heater(PR)
H1.DP = 1
H1.DH = 1
F1 = Flash(PR)
S1.Connect(F1)
##
##V1.Connect(H1)
##H1.Connect(F1)
import sys
sys.path.append("/Users/jonathanxavier/Developer/sim42")
from ollin.Administrator.AdmOllin import Ollin
from pylab import *
RK = Ollin.AddModel("RK", "RK")
S1 = Ollin.AddCase("S1")
Ollin.Add(["ETHANE", "PROPANE", "N-BUTANE", "N-PENTANE", "N-HEXANE"], "RK")
S1.SetX([0.05, 0.15, 0.25, 0.20, 0.35])
S1.T(280)
plot_x = range(50, 270, 5)
plot_y0 = []
plot_y1 = []
plot_y2 = []
plot_y3 = []
plot_y4 = []
plot_y5 = []
for P in plot_x:
S1.P(P)
Ollin.Solve()
yf = S1.Get("yf")
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"))
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
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
from ollin.Administrator.AdmOllin import Ollin
from ollin.Tools.tools import lagrange
from pylab import *
RK=Ollin.AddModel("RK","PR")
S1=Ollin.AddCase("S1")
Ollin.Add(["N-HEPTANE"],"RK")
Ti = range(300,450,10)
S1.SetX([1,])
Ppi=[]
Ppv=[]
for T in Ti:
df=[]
P= []
S1.P(101.325)
S1.T(T)
Ollin.Solve()
Pvi=S1.Get("PreVap")[0]
Ppi.append(Pvi)
fl=S1.Get("fl_i")[0]
fv=S1.Get("fv_i")[0]
P.append(S1.Get("P"))
df.append(fl-fv)
S1.P(Pvi)
Ollin.Solve()
fl=S1.Get("fl_i")[0]
fv=S1.Get("fv_i")[0]
P.append(S1.Get("P"))
df.append(fl-fv)