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234 lines (200 loc) · 9.21 KB
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# -*- coding: utf-8 -*-
"""
Created on Sun Feb 9 09:36:36 2020
@author: Gavin
"""
# Import modules
import numpy as np
import PFR
import matplotlib.pyplot as plt
from mpl_toolkits.mplot3d import Axes3D
from matplotlib import cm
import pandas as pd
saveDir = "graphs"
mesh_size = 100
# Total channel (reactor) length in m
l_lowerlim = 0.25 # 50
l_upperlim = 5 # 200
# Total flowrate in mL/hr
tot_flowrate = 68100000
# Reactor and channel dimensions in m
# Total channel (reactor) length is specified in the function itself, which is dependent on the specified channel (reactor) length
switchback_len = 50e-3
channel_width = 1200e-6
channel_depth = 1200e-6
addl_len = 10e-3
chip_width = switchback_len+1e-2
chip_thick = channel_depth+2400e-6
# Constants required for determining pumping power
# dynamic viscosity
mu = 0.01985 # Ns/m^2 (from soybean oil @ 60C, from interpolation)
# density
rho = 0.917 # kg/m^3 (from soybean oil)
# local loss (pressure drop) coefficient
KL = 0.2 # for 180 deg bend, flanged
# flow coefficient
Cv = 56.9 # for square channel with laminar flow
# discharge coefficient
Cd = 0.5959
# inlet to microreactors (full pipe diameter in m)
Di = 0.1016
# pump efficiency
eff = 0.75 # approx value from sample pump curve in unit ops
# gravity
g = 9.81 # m/s^2
# Number of individual microreactor units
units_lowerlim = 200000 # 200000
units_upperlim = 2000000 # 2000000
# Reactor volume in μL
V_lowerlim = l_lowerlim*(channel_depth*channel_width)/(1e-9)
V_upperlim = l_upperlim*(channel_depth*channel_width)/(1e-9)
# Flow rate in mL/hr
v0_lowerlim = (tot_flowrate)/(units_lowerlim)
v0_upperlim = (tot_flowrate)/(units_upperlim)
V = np.linspace(V_lowerlim,V_upperlim,mesh_size)
v0 = np.linspace(v0_lowerlim,v0_upperlim,mesh_size)
V, v0 = np.meshgrid(V, v0)
conv = np.empty((len(V),len(v0)))
perc_yield = np.empty((len(V),len(v0)))
DGrelconc = np.empty((len(V),len(v0)))
MGrelconc = np.empty((len(V),len(v0)))
EErelconc = np.empty((len(V),len(v0)))
for m in range(len(V)):
for n in range(len(v0)):
# Input file containing rate constants
in_file1 = "microreactor_constants_basecat"
# Input file containing initial concentration
in_file2 = "feed1"
# Input file containing reactor network scheme w/ reactor volumes
in_file3 = "PFR"
# Read in relevant values from initial concentration input file
with open(in_file2,"r") as f:
lines=np.array(f.readlines())
c0 = []
for i in np.arange(len(lines)):
if lines[i].startswith("cTGE ="):
c0.append(float(lines[i].strip("cTGE =")))
elif lines[i].startswith("cDGE ="):
c0.append(float(lines[i].strip("cDGE =")))
elif lines[i].startswith("cMGE ="):
c0.append(float(lines[i].strip("cMGE =")))
elif lines[i].startswith("cCAT ="):
c0.append(float(lines[i].strip("cCAT =")))
elif lines[i].startswith("cEtOH ="):
c0.append(float(lines[i].strip("cEtOH =")))
elif lines[i].startswith("cEE ="):
c0.append(float(lines[i].strip("cEE =")))
elif lines[i].startswith("cG ="):
c0.append(float(lines[i].strip("cG =")))
elif lines[i].startswith("cTGO ="):
c0.append(float(lines[i].strip("cTGO =")))
elif lines[i].startswith("cDGO ="):
c0.append(float(lines[i].strip("cDGO =")))
elif lines[i].startswith("cMGO ="):
c0.append(float(lines[i].strip("cMGO =")))
conc = PFR.pfr(in_file1,c0,(V[m,n]*1e-6),(v0[m,n]*(1e-3)/3600))
conc = np.vstack(conc)
# Calculate product stream results
conv[m,n] = 100*(c0[7]-conc[:,7][-1])/(c0[7])
perc_yield[m,n] = 100*conc[:,5][-1]/(c0[7]*3)
totconc=0
for i in range(0,len(conc[-1])):
totconc += conc[-1][i]
DGrelconc[m,n] = 100*((conc[:,1][-1]+conc[:,7][-1])/totconc)
MGrelconc[m,n] = 100*((conc[:,2][-1]+conc[:,9][-1])/totconc)
EErelconc[m,n] = 100*(conc[:,5][-1]/(totconc-conc[:,3][-1]-conc[:,4][-1]-conc[:,6][-1]))
# Calculate footprint and pumping power
units = tot_flowrate/v0
channel_len = V*(1e-9)/(channel_depth*channel_width)
num_switchbacks = (channel_len/switchback_len)
chip_len = (num_switchbacks)*(2*channel_width)+addl_len
# Calculate orifice characteristics
beta = ((channel_depth+channel_width)/2)/(Di)
footprint = units*chip_len*chip_width*chip_thick
delta_p_major = (Cv*mu*channel_len*v0*(1e-3)*(1e-3)/3600)/(2*(channel_depth*channel_width)**2)
delta_p_minor = (KL*num_switchbacks*rho*(v0*(1e-3)*(1e-3)/3600)**2)/(2*(channel_depth*channel_width)**2)
#delta_p_orif = (rho/2)*(1-(beta**4))*((v0*(1e-3)*(1e-3)/3600)/(Cd*channel_depth*channel_width))**2
delta_p = delta_p_major + delta_p_minor
pump_power = units*delta_p*((v0*(1e-3)*(1e-3)/3600)/(eff*g))
# Make dataframe with summary of results
labels=["# Microreactor Units","Channel Length (m)",
"Total Flow Rate (mL/hr)","Flowrate thru each Channel (mL/hr)",
"Channel Depth (um)", "Channel Width (um)","% Coversion TG",
"% Yield FAME","DG Rel Conc (mol%)","MG Rel Conc (mol%)",
"FAME Purity (mol%)","Footprint (m^3)","Pumping Power (W)",
"Pressure drop (Pa)"]
data = {"# Microreactor Units": units[m,n],
"Channel Length (m)": channel_len[m,n],
"Total Flow Rate (mL/hr)": tot_flowrate,
"Flowrate thru each Channel (mL/hr)": v0[m,n],
"Channel Depth (um)": channel_depth,
"Channel Width (um)": channel_width,
"% Coversion TG": conv[m,n],
"% Yield FAME": perc_yield[m,n],
"DG Rel Conc (mol%)": DGrelconc[m,n],
"MG Rel Conc (mol%)": MGrelconc[m,n],
"FAME Purity (mol%)": EErelconc[m,n],
"Footprint (m^3)": footprint[m,n],
"Pressure drop (Pa)": delta_p[m,n],
"Pumping Power (W)": pump_power[m,n]}
labels2 = ["cTGE","cDGE","cMGE","cCAT","cEtOH","cEE","cG","cTGO","cDGO","cMGO"]
data2 = {"cTGE": conc[:,0][-1],
"cDGE": conc[:,1][-1],
"cMGE": conc[:,2][-1],
"cCAT": conc[:,3][-1],
"cEtOH": conc[:,4][-1],
"cEE": conc[:,5][-1],
"cG": conc[:,6][-1],
"cTGO": conc[:,7][-1],
"cDGO": conc[:,8][-1],
"cMGO": conc[:,9][-1]}
if m==0 and n==0:
existing_df = pd.DataFrame(columns=labels)
df = existing_df.append(data,ignore_index=True)
existing_df2 = pd.DataFrame(columns=labels2)
df2 = existing_df2.append(data2,ignore_index=True)
else:
df = df.append(data,ignore_index=True)
df2 = df2.append(data2,ignore_index=True)
def plotter(varName,axisName,title,manual_lowerlim=None,manual_upperlim=None,color=None,rotation=None):
# Plot the surface
fig = plt.figure(figsize=(9,7))
ax = fig.gca(projection='3d')
if color:
surf = ax.plot_surface(channel_len, (units*1e-3), varName, cmap=color)
else:
surf = ax.plot_surface(channel_len, (units*1e-3), varName, cmap=cm.viridis)
ax.set_xlim(l_lowerlim,l_upperlim)
ax.set_ylim((units_lowerlim*1e-3),(units_upperlim*1e-3))
if manual_lowerlim and manual_upperlim:
ax.set_zlim(manual_lowerlim,manual_upperlim)
elif manual_lowerlim:
ax.set_zlim(manual_lowerlim,np.amax(varName))
elif manual_upperlim:
ax.set_zlim(np.amin(varName),manual_upperlim)
else:
ax.set_zlim(np.amin(varName),np.amax(varName))
ax.set_zlabel(axisName)
ax.set_ylabel('$10^3$ microreactor units')
ax.set_xlabel('Reactor channel length (m)')
ax.zaxis.label.set_size(13)
ax.yaxis.label.set_size(13)
ax.xaxis.label.set_size(13)
# Add a color bar which maps values to colors.
fig.colorbar(surf, shrink=0.5, aspect=5)
if rotation:
ax.view_init(20,rotation)
else:
ax.view_init(20,225)
plt.savefig("{}/{}.png".format(saveDir,title))
return
plotter(conv, '% Coversion of Triglyceride','conversion',manual_upperlim=100)
plotter(perc_yield, '% Yield of FAME','percentyield')
plotter(DGrelconc, 'Diglyceride Relative Concentration (mol%)','DGrelconc',rotation=135)
plotter(MGrelconc, 'Monoglyceride Relative Concentration (mol%)','MGrelconc',rotation=135)
plotter(EErelconc, 'FAME Purity in Separated Oil Phase (mol%)','EErelconc')
plotter(footprint, 'Footprint ($m^3$)','footprint',color='inferno')
plotter(pump_power, 'Pumping Power (W)','pumppower',color='inferno',rotation=135)
df.to_csv("{}/summary.csv".format(saveDir))
df2.to_csv("{}/conc.csv".format(saveDir))
plt.show()