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ammonia_PFR_reactor_script_NH3.py
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ammonia_PFR_reactor_script_NH3.py
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###############################################
# Rebrov reactor batch script
# Ting-Chen Lee and Chris Blais
# Northeastern University
# runs through all reactor conditions
###############################################
import numpy as np
import time
import cantera as ct
from matplotlib import pyplot as plt
import csv
import math
import os
import sys
import re
import itertools
import logging
from collections import defaultdict
import git
import json
from rmgpy.molecule import Molecule
from rmgpy.data.base import Database
def save_pictures(git_path="", species_path="", overwrite=False):
"""
Save a folder full of molecule pictures, needed for the pretty dot files.
Saves them in the results directory, in a subfolder "species_pictures".
Unless you set overwrite=True, it'll leave alone files that are
already there.
"""
dictionary_filename = git_path + "/base/chemkin/species_dictionary.txt"
specs = Database().get_species(dictionary_filename, resonance=False)
images_dir = os.path.join(species_path)
os.makedirs(images_dir, exist_ok=True)
for name, species in specs.items():
filepath = os.path.join(images_dir, name + ".png")
if not overwrite and os.path.exists(filepath):
continue
species.molecule[0].draw(filepath)
def prettydot(species_path, dotfilepath, strip_line_labels=False):
"""
Make a prettier version of the dot file (flux diagram)
Assumes the species pictures are stored in a directory
called 'species_pictures' alongside the dot file.
"""
pictures_directory = f"{species_path}/"
if strip_line_labels:
print("stripping edge (line) labels")
reSize = re.compile('size="5,6"\;page="5,6"')
reNode = re.compile(
'(?P<node>s\d+)\ \[\ fontname="Helvetica",\ label="(?P<label>[^"]*)"\]\;'
)
rePicture = re.compile("(?P<smiles>.+?)\((?P<id>\d+)\)\.png")
reLabel = re.compile("(?P<name>.+?)\((?P<id>\d+)\)$")
species_pictures = dict()
for picturefile in os.listdir(pictures_directory):
match = rePicture.match(picturefile)
if match:
species_pictures[match.group("id")] = picturefile
else:
pass
# print(picturefile, "didn't look like a picture")
filepath = dotfilepath
if not open(filepath).readline().startswith("digraph"):
raise ValueError("{0} - not a digraph".format(filepath))
infile = open(filepath)
prettypath = filepath.replace(".dot", "", 1) + "-pretty.dot"
outfile = open(prettypath, "w")
for line in infile:
(line, changed_size) = reSize.subn('size="12,12";page="12,12"', line)
match = reNode.search(line)
if match:
label = match.group("label")
idmatch = reLabel.match(label)
if idmatch:
idnumber = idmatch.group("id")
if idnumber in species_pictures:
line = (
f'%s [ image="{pictures_directory}%s" label="" width="0.5" height="0.5" imagescale=false fixedsize=false color="none" ];\n'
% (match.group("node"), species_pictures[idnumber])
)
# rankdir="LR" to make graph go left>right instead of top>bottom
if strip_line_labels:
line = re.sub('label\s*=\s*"\s*[\d.]+"', 'label=""', line)
# change colours
line = re.sub('color="0.7,\ (.*?),\ 0.9"', r'color="1.0, \1, 0.7*\1"', line)
outfile.write(line)
outfile.close()
infile.close()
print(f"Graph saved to: {prettypath}")
os.system(f'dot {prettypath} -Tpng -o{prettypath.replace(".dot", "", 1) + ".png"} -Gdpi=200')
return prettypath
def show_flux_diagrams(self, suffix="", embed=False):
"""
Shows the flux diagrams in the notebook.
Loads them from disk.
Does not embed them, to keep the .ipynb file small,
unless embed=True. Use embed=True if you might over-write the files,
eg. you want to show flux at different points.
"""
import IPython
for element in "CHON":
for phase_object in (self.gas, self.surf):
phase = phase_object.name
img_file = (
f"reaction_path_{element}_{phase}{'_' if suffix else ''}{suffix}.png"
)
display(IPython.display.HTML(f"<hr><h2>{element} {phase}</h2>"))
if embed:
display(IPython.display.Image(filename=img_file, width=400, embed=True))
else:
display(IPython.display.Image(url=img_file, width=400, embed=False))
# Now do the combined
img_file = f"reaction_path_mass{'_' if suffix else ''}{suffix}.png"
display(IPython.display.HTML(f"<hr><h2>Combined mass</h2>"))
if embed:
display(IPython.display.Image(filename=img_file, width=400, embed=True))
else:
display(IPython.display.Image(url=img_file, width=400, embed=False))
def save_flux_diagrams(*phases, suffix="", timepoint="", species_path=""):
"""
Saves the flux diagrams. The filenames have a suffix if provided,
so you can keep them separate and not over-write.
"""
for element in "CHON":
for phase_object in phases:
phase = phase_object.name
diagram = ct.ReactionPathDiagram(phase_object, element)
diagram.title = f"Reaction path diagram following {element} in {phase}"
diagram.label_threshold = 0.001
dot_file = f"{suffix}/reaction_path_{element}_{phase}_{timepoint}.dot"
img_file = f"{suffix}/reaction_path_{element}_{phase}_{timepoint}.png"
dot_bin_path = (
"/Users/lee.ting/Code/anaconda3/pkgs/graphviz-2.40.1-hefbbd9a_2/bin/dot"
#maybe try "/home/lee.ting/.conda/pkgs/graphviz-2.40.1-h21bd128_2/bin/dot"
)
img_path = os.path.join(os.getcwd(), img_file)
diagram.write_dot(dot_file)
#also make a prettydot file
prettydot(species_path, dot_file, strip_line_labels=False)
# print(diagram.get_data())
print(
f"Wrote graphviz input file to '{os.path.join(os.getcwd(), dot_file)}'."
)
os.system(f"dot {dot_file} -Tpng -o{img_file} -Gdpi=200")
print(f"Wrote graphviz output file to '{img_path}'.")
def run_reactor(
cti_file,
t_array=[598],
surf_t_array=[598], # not used, but will be for different starting temperatures
p_array=[1],
v_array=[2.7155e-8], # 14*7*(140e-4)^2*π/2*0.9=0.027155(cm^3)=2.7155e-8(m^3)
o2_array=[0.88],
nh3_array=[0.066],
rtol=1.0e-11,
atol=1.0e-22,
reactor_type=0,
energy="off",
sensitivity=False,
sensatol=1e-6,
sensrtol=1e-6,
reactime=1e5,
):
# 14 aluminum plates, each of them containing seven semi-cylindrical microchannels of 280 µm width
# and 140 µm depth, 9 mm long, arranged at equal distances of 280 µm
try:
array_i = int(os.getenv("SLURM_ARRAY_TASK_ID"))
except TypeError:
array_i = 0
# get git commit hash and message
rmg_model_path = "../ammonia"
repo = git.Repo(rmg_model_path)
date = time.localtime(repo.head.commit.committed_date)
git_date = f"{date[0]}_{date[1]}_{date[2]}_{date[3]}{date[4]}"
git_sha = str(repo.head.commit)[0:6]
git_msg = str(repo.head.commit.message)[0:50].replace(" ", "_").replace("'", "_").replace("\n", "")
git_file_string = f"{git_date}_{git_sha}_{git_msg}"
# set sensitivity string for file path name
if sensitivity:
sensitivity_str = "on"
else:
sensitivity_str = "off"
# this should probably be outside of function
settings = list(itertools.product(t_array, surf_t_array, p_array, v_array, o2_array, nh3_array))
# constants
pi = math.pi
# set initial temps, pressures, concentrations
temp = settings[array_i][0] # kelvin
temp_str = str(temp)[0]
pressure = settings[array_i][2] * ct.one_atm # Pascals
surf_temp = temp
X_o2 = settings[array_i][4]
x_O2_str = str(X_o2)[0].replace(".", "_")
X_nh3 = (settings[array_i][5])
x_NH3_str = str(X_nh3)[0:30].replace(".", "_")
X_he = 1 - X_o2 - X_nh3
mw_nh3 = 17.0306e-3 # [kg/mol]
mw_o2 = 31.999e-3 # [kg/mol]
mw_he = 4.002602e-3 # [kg/mol]
o2_ratio = X_nh3 / X_o2
# O2/NH3/He: typical is
concentrations_rmg = {"O2(2)": X_o2, "NH3(6)": X_nh3, "He": X_he}
# initialize cantera gas and surface
gas = ct.Solution(cti_file, "gas")
surf = ct.Interface(cti_file, "surface1", [gas])
# initialize temperatures
gas.TPX = temp, pressure, concentrations_rmg
surf.TP = temp, pressure # change this to surf_temp when we want a different starting temperature for the surface
# if a mistake is made with the input,
# cantera will normalize the mole fractions.
# make sure that we are reporting/using
# the normalized values
X_o2 = float(gas["O2(2)"].X)
X_nh3 = float(gas["NH3(6)"].X)
X_he = float(gas["He"].X)
# Use a chain of batch reactors to represent a PFR reactor
number_of_reactors = 1001
rradius = 1.4e-4 #140µm to 0.00014m
rtotal_length = 9e-3 #9mm to 0.009m
rtotal_vol = 49*(rradius**2)*pi*rtotal_length# 49 channels
rlength = rtotal_length/(number_of_reactors-1)
rvol = (rtotal_vol)/number_of_reactors #check porosity
# Catalyst Surface Area
site_density = (surf.site_density*1000) # [mol/m^2] cantera uses kmol/m^2, convert to mol/m^2
#site_density = 2.483e-2 #kmol/m^2 for Pt in RMG
Pt_radius = 1.15e-9 #m, 23Å/2
Pt_mass = 5.43e-4 #g
Pt_density = 2.145e7 #g/m3
Pt_total_vol = Pt_mass/Pt_density
Pt_vol = 4/3*pi*Pt_radius**3
numbers_of_Pt = Pt_total_vol/Pt_vol
cat_area_total = numbers_of_Pt*4*pi*Pt_radius**2
cat_area = cat_area_total/number_of_reactors
# reactor initialization
if reactor_type == 0:
r = ct.Reactor(gas, energy=energy)
reactor_type_str = "Reactor"
elif reactor_type == 1:
r = ct.IdealGasReactor(gas, energy=energy)
reactor_type_str = "IdealGasReactor"
elif reactor_type == 2:
r = ct.ConstPressureReactor(gas, energy=energy)
reactor_type_str = "ConstPressureReactor"
elif reactor_type == 3:
r = ct.IdealGasConstPressureReactor(gas, energy=energy)
reactor_type_str = "IdealGasConstPressureReactor"
# calculate the available catalyst area in a differential reactor
rsurf = ct.ReactorSurface(surf, r, A=cat_area)
r.volume = rvol
surf.coverages = "X(1):1.0"
# flow controllers
one_atm = ct.one_atm
FC_temp = 298.15
volume_flow = settings[array_i][3] # [m^3/s]
molar_flow = volume_flow * one_atm / (8.3145 * FC_temp) # [mol/s]
mass_flow = molar_flow * (X_nh3 * mw_nh3 + X_o2 * mw_o2 + X_he * mw_he) # [kg/s]
mfc = ct.MassFlowController(inlet, r, mdot=mass_flow)
# A PressureController has a baseline mass flow rate matching the 'master'
# MassFlowController, with an additional pressure-dependent term. By explicitly
# including the upstream mass flow rate, the pressure is kept constant without
# needing to use a large value for 'K', which can introduce undesired stiffness.
outlet_mfc = ct.PressureController(r, exhaust, master=mfc, K=0.01)
# initialize reactor network
sim = ct.ReactorNet([r])
sim.set_max_time_step(1e-3)
# set relative and absolute tolerances on the simulation
# Common values for absolute tolerance are 1e-15 to 1e-25. Relative tolerance is usually 1e-4 to 1e-8
sim.rtol = 1.0e-12
sim.atol = 1.0e-22
#################################################
# Run single reactor
#################################################
# round numbers for filepath strings so they're easier to read
# temp_str = '%s' % '%.3g' % tempn
cat_area_str = "%s" % "%.3g" % cat_area
# if it doesn't already exist, g
species_path = (
os.path.dirname(os.path.abspath(__file__))
+ f"/results/NH3_results/{git_file_string}/species_pictures"
)
results_path = (
os.path.dirname(os.path.abspath(__file__))
+ f"/results/NH3_results/{git_file_string}/{reactor_type_str}/energy_{energy}/sensitivity_{sensitivity_str}/{temp}/results"
)
logging.warning(f"Saving results in {results_path}, the file's name is _temp_{temp}_O2_88_NH3_{x_NH3_str}.csv")
flux_path = (
os.path.dirname(os.path.abspath(__file__))
+ f"/results/NH3_results/{git_file_string}/{reactor_type_str}/energy_{energy}/sensitivity_{sensitivity_str}/{temp}/flux_diagrams/{x_O2_str}/{x_NH3_str}"
)
# create species folder for species pictures if it does not already exist
try:
os.makedirs(species_path, exist_ok=True)
save_pictures(git_path=rmg_model_path, species_path=species_path)
except OSError as error:
print(error)
try:
os.makedirs(results_path, exist_ok=True)
except OSError as error:
print(error)
try:
os.makedirs(flux_path, exist_ok=True)
except OSError as error:
print(error)
gas_ROP_str = [i + " ROP [kmol/m^3 s]" for i in gas.species_names]
# surface ROP reports gas and surface ROP. these values are not redundant
gas_surf_ROP_str = [i + " surface ROP [kmol/m^2 s]" for i in gas.species_names]
surf_ROP_str = [i + " ROP [kmol/m^2 s]" for i in surf.species_names]
gasrxn_ROP_str = [i + " ROP [kmol/m^3 s]" for i in gas.reaction_equations()]
surfrxn_ROP_str = [i + " ROP [kmol/m^2 s]" for i in surf.reaction_equations()]
output_filename = (
results_path
+ f"/Spinning_basket_area_{cat_area_str}_energy_{energy}"
+ f"_temp_{temp}_O2_{x_O2_str}_NH3_{x_NH3_str}.csv"
)
outfile = open(output_filename, "w")
writer = csv.writer(outfile)
# Sensitivity atol, rtol, and strings for gas and surface reactions if selected
# slows down script by a lot
if sensitivity:
sim.rtol_sensitivity = sensrtol
sim.atol_sensitivity = sensatol
sens_species = ["NH3(6)", "O2(2)", "N2(4)", "NO(5)", "N2O(7)"] #change THIS to your species, can add "," and other species
# turn on sensitive reactions
for i in range(gas.n_reactions):
r.add_sensitivity_reaction(i)
for i in range(surf.n_reactions):
rsurf.add_sensitivity_reaction(i)
# thermo sensitivities. leave off for now as they can cause solver crashes
# for i in range(gas.n_species):
# r.add_sensitivity_species_enthalpy(i)
# for i in range(surf.n_species):
# rsurf.add_sensitivity_species_enthalpy(i)
for j in sens_species:
gasrxn_sens_str = [
j + " sensitivity to " + i for i in gas.reaction_equations()
]
surfrxn_sens_str = [
j + " sensitivity to " + i for i in surf.reaction_equations()
]
# gastherm_sens_str = [j + " thermo sensitivity to " + i for i in gas.species_names]
# surftherm_sens_str = [j + " thermo sensitivity to " + i for i in surf.species_names]
sens_list = gasrxn_sens_str + surfrxn_sens_str # + gastherm_sens_str
writer.writerow(
[
"Distance (mm)",
"T (K)",
"P (Pa)",
"V (M^3/s)",
"X_nh3 initial",
"X_o2 initial",
"X_he initial",
"(NH3/O2)",
"T (K) final",
"Rtol",
"Atol",
"reactor type",
"energy on?"
]
+ gas.species_names
+ surf.species_names
+ gas_ROP_str
+ gas_surf_ROP_str
+ surf_ROP_str
+ gasrxn_ROP_str
+ surfrxn_ROP_str
+ sens_list
)
else:
writer.writerow(
[
"Distance (mm)",
"T (K)",
"P (Pa)",
"V (M^3/s)",
"X_nh3 initial",
"X_o2 initial",
"X_he initial",
"(NH3/O2)",
"T (K) final",
"Rtol",
"Atol",
"reactor type",
"energy on?"
]
+ gas.species_names
+ surf.species_names
+ gas_ROP_str
+ gas_surf_ROP_str
+ surf_ROP_str
+ gasrxn_ROP_str
+ surfrxn_ROP_str
)
t = 0.0
dt = 0.1
iter_ct = 0
# run the simulation
first_run = True
distance_mm = 0
for n in range(number_of_reactors):
# Set the state of the reservoir to match that of the previous reactor
gas.TDY = TDY = r.thermo.TDY
inlet.syncState()
sim.reinitialize()
previous_coverages = surf.coverages # in case we want to retry
if n > 0: # Add a first row in the CSV with just the feed
try:
sim.advance_to_steady_state()
except ct.CanteraError:
t = sim.time
sim.set_initial_time(0)
gas.TDY = TDY
surf.coverages = previous_coverages
r.syncState()
sim.reinitialize()
new_target_time = 0.01 * t
logging.warning(
f"Couldn't reach {t:.1g} s so going to try {new_target_time:.1g} s"
)
try:
sim.advance(new_target_time)
except ct.CanteraError:
outfile.close()
raise
# save flux diagrams at beginning of run
if first_run == True:
save_flux_diagrams(gas, suffix=flux_path, timepoint="beginning", species_path=species_path)
save_flux_diagrams(surf, suffix=flux_path, timepoint="beginning", species_path=species_path)
first_run = False
if sensitivity:
# get sensitivity for sensitive species i (e.g. methanol) in reaction j
for i in sens_species:
g_nrxn = gas.n_reactions
s_nrxn = surf.n_reactions
# g_nspec = gas.n_species
# s_nspec = surf.n_species
gas_sensitivities = [sim.sensitivity(i, j) for j in range(g_nrxn)]
surf_sensitivities = [
sim.sensitivity(i, j) for j in range(g_nrxn, g_nrxn + s_nrxn)
]
# gas_therm_sensitivities = [sim.sensitivity(i,j)
# for j in range(g_nrxn+s_nrxn,g_nrxn+s_nrxn+g_nspec)]
# surf_therm_sensitivities = [sim.sensitivity(i,j)
# for j in range(g_nrxn+s_nrxn+g_nspec,g_nrxn+s_nrxn+g_nspec+s_nspec)]
sensitivities_all = (
gas_sensitivities
+ surf_sensitivities
# + gas_therm_sensitivities
)
writer.writerow(
[
distance_mm,
temp,
gas.P,
volume_flow,
X_nh3,
X_o2,
X_he,
o2_ratio,
gas.T,
sim.rtol,
sim.atol,
reactor_type_str,
energy,
]
+ list(gas.X)
+ list(surf.X)
+ list(gas.net_production_rates)
+ list(surf.net_production_rates)
+ list(gas.net_rates_of_progress)
+ list(surf.net_rates_of_progress)
+ sensitivities_all,
)
else:
writer.writerow(
[
distance_mm,
temp,
gas.P,
volume_flow,
X_nh3,
X_o2,
X_he,
o2_ratio,
gas.T,
sim.rtol,
sim.atol,
reactor_type_str,
energy,
]
+ list(gas.X)
+ list(surf.X)
+ list(gas.net_production_rates)
+ list(surf.net_production_rates)
+ list(gas.net_rates_of_progress)
+ list(surf.net_rates_of_progress)
)
iter_ct += 1
distance_mm = (n+1) * rlength * 1.0e3 # distance in mm
outfile.close()
# save flux diagrams at the end of the run
save_flux_diagrams(gas, suffix=flux_path, timepoint="end", species_path=species_path)
save_flux_diagrams(surf, suffix=flux_path, timepoint="end", species_path=species_path)
return
#######################################################################
# Input Parameters for combustor
#######################################################################
# filepath for writing files
git_repo = "../ammonia/"
cti_file = git_repo + "base/cantera/chem_annotated.cti"
# Reactor settings arrays for run
#Temps = [498,523,548,573,598,623,648,673,698] #523-673K
Temps = [598]
Pressures = [1] # 1 bar
volume_flows = [5.8333e-8] # [m^3/s]
#3500 Ncm3/min = 3500/e6/60 m3/s = 5.8333e-5
#2000 Ncm3/min = 2000/e6/60 m3/s = 3.3333e-5
# NH3/O2 = 0.068
O2_fraction = [0.88] #O2 partial pressure(atm)
#NH3_fraction = np.linspace(0.01,0.12,30)
#NH3_fraction = [0.01, 0.02, 0.03, 0.04, 0.05, 0.06,0.066, 0.07, 0.08, 0.09, 0.1, 0.11, 0.12] #NH3 partial pressure, 0.01–0.12 atm
NH3_fraction = [0.01,0.015,0.02,0.025,0.03,0.035,0.04,0.045,0.05,0.055,0.06,0.066,0.07,0.075,0.08,0.085,0.09,0.095,0.1,0.105,0.11,0.0115,0.12] #23 values
# reaction time
reactime = 1e5
# sensitivity settings
sensitivity = False
sensatol = 1e-6
sensrtol = 1e-6
run_reactor(
cti_file=cti_file,
t_array=Temps,
reactor_type=1,
v_array=volume_flows,
o2_array=O2_fraction,
nh3_array=NH3_fraction,
energy="off",
sensitivity=sensitivity,
sensatol=sensatol,
sensrtol=sensrtol,
reactime=reactime,
)