# -*- coding: utf-8 -*-
"""
A script to evaluate mixtures, in order to find some with vapor pressures
in some limits at given temperatures, together with the temperature glide.
The results are stored as figure, as csv and in a json-file(Input); all in the
given directory.
The csv output file structure is as follows:
* number of calculation
* the four mole fractions, species names are in the title
* index l: the properties for saturated vapor at the given low temperature
* index sup: the poperties at superheating at pressure p_l for a prescribed superheating
* index h: the properties for saturated vapor at the given high temperature
* index is: the properties for the isentropic state (sup ->p_h) at the given low temperature
* index is80: the properties for the isentropic effic. of 80 % (sup ->p_h) at the given low temperature
* index dew: the properties for the saturated liquid at p_h
* index mid: the properties at the mean enthalpy between q=0 and q=1 at p_h
* index thr: the properties for the isenthalpic throtteling from saturated liquid to p_l
* index hplT: the properties at T_l and p_h
* index thrlow: the properties for the isenthalpic throtteling from hplt ->p_l
* index bol: the properties for saturated liquid at the low pressure p_l
* p_ratio: the pressure ratio
* T_glide_h: the temperature glide at high pressure
* dv/v'': (ca.) the mean change in volume along throtteling relative to the specific volume of the vapor, this is a measure of how much work is 'lost' along throtteling
* dv/v''-b: similar volume ratio after subcooling to thrlow, answer the question: will subcooling reduce losses (strongly)?
* COP_is: What is the predicted COP for isentropic compression (losses along throtteling are seen here)
For each indexed state : T,p,h,v,s,q,u in SI units(mass base) are listed.
part of carbatpy
Created on Thu Oct 19 14:11:14 2023
@author: atakan
"""
import os
import json
import itertools
import matplotlib.pyplot as plt
import seaborn as sbn
import pandas as pd
import numpy as np
import carbatpy as cb
[docs]def mixture_search(fluids_all, temp_both, p_both, res_dir, d_temp_superheating=5,
resolution=21, temp_limit=False, **kwargs):
"""
Mixtures are evaluated/screened to find mixtures with a given temperature
glide in a certain pressure range. For all possible mixture compositions
first the saturated vapor pressure at the given low temperature and composition
is evaluated, if it is in the allowed regime, the saturated vapor pressure
(p_h) of the mixture at the high temperature is evaluated.
If this is below the allowed high
pressure, the saturated liquid temperature at this p_h is evaluated and the
temperature difference is taken as temperature glide. The pressure ratio is
plotted as a function of temperature glide.
The plot, the states (as csv-file) and the input parameters (as .json-file)
are stored.
in the csv-File first the mole fractions are given followed by the
properties of the low temperature sat.vapor, after superheating,
for thehigh temperature sat. vapor, the isentropic state after compression,
high pressure sat.liquid, low pressuer isenthalpic (throtteling) state to
the high pressure sat. liquid, and the low pressure saturated liquis state.
For each of them: T,p,h,v,s,q,u in SI units(mass base)
Parameters
----------
fluids_all : list of strings
up to 4 fluid names of the mixture, as defined in the fluid model
(REFPROP).
temp_both : List of two floats
the minimum (at low pressure) and the maximum (at high pressure)
saturated vapor temperature (both dew points) in K.
p_both : List of two floats
allowed min and max pressure in Pa.
res_dir : string
Directory name, where the results are stored.
d_temp_superheating : float. optional
super heating temperature in K. The default is 5.
resolution : integer, optional
inverse is the interval for the mole fraction screening (21 means every
0.05 a value is calculated). The default is 21.
temp_limit : Boolean, optional
selects only values, where the temperature of the saturated liquid at
high pressure is above temp_both[0]. The default is False.
kwargs : dict
is not implemented yet, but can be used later to select another fluid
model, instead of REFPROP.
Returns
-------
None.
"""
# dir_name = r"C:\Users\atakan\sciebo\results\optimal_hp_fluid"
eff_isentropic = 0.8 # isentropic efficiency, compressor
all_results = {}
exception_messages = []
all_results["warn"] = 0
if len(kwargs) > 0:
print(f"These arguments are not implemented yet{kwargs}")
all_results["warn"] = 1
dir_name = res_dir
plt.style.use('seaborn-v0_8-poster') # 'seaborn-v0_8-poster')
# fluids_all = ["Ethane", "Propane", "Pentane", "CO2"]
fluid_mixture = "*".join(fluids_all)
# fluid_mixture = "Dimethylether * Butane * Pentane * Hexane" # "Propane * Butane * Pentane * Hexane"
names = ["x_" + s for s in fluids_all]
fn_end = "".join([s[:3] for s in fluids_all])
fname = cb.helpers.file_copy.copy_script_add_date(
fn_end, __file__, dir_name)
# fname = date + fn_end
comp = [.5, 0., 0.5, 0.0] # , 0.0]
flm = cb.fprop.FluidModel(fluid_mixture)
my_fluid = cb.fprop.Fluid(flm, comp)
temp_low, temp_high = temp_both
p_low, p_high = p_both
x_i_range = np.linspace(0, 1, resolution)
results = []
sound_speeds = []
lin_t_deviations_all =[]
n_species = len(fluids_all)
variables_dict = {"File_name": fname,
"Dir_name": dir_name,
"Fluid": fluid_mixture,
"T_low": temp_low,
"T_high": temp_high,
"d_temp_superheating": d_temp_superheating,
"p_low": p_low,
"p_high": p_high,
"eta_is80": eff_isentropic,
"what": "T_sat_l, T_sat_h, T_super, T_is,T_is80, T_throt,Tsat_l_high"
}
# Dateipfad, in dem die JSON-Datei gespeichert wird
json_file_path = fname+"_variablen.json"
# Speichern des Dictionaries in einer JSON-Datei
with open(json_file_path, 'w', encoding="utf-8") as json_file:
json.dump(variables_dict, json_file)
print(f"Variablen wurden in '{json_file_path}' gespeichert.")
mole_fractions = np.zeros((n_species))
for positions in itertools.product(range(len(x_i_range)), repeat=n_species-1):
# positions ist ein Tupel, das die ausgewählten Positionen enthält
actual_x = np.array([x_i_range[i] for i in positions])
if actual_x.sum() <= 1:
mole_fractions[:3] = actual_x
mole_fractions[n_species-1] = 1 - actual_x.sum()
my_fluid.set_composition(mole_fractions)
try:
state_low = my_fluid.set_state(
[temp_low - d_temp_superheating, 1.], "TQ") # find low pressure
state_sup = my_fluid.set_state([state_low[1], temp_low],
"PT", cb.fprop._TRANS_STRING) # super heated state at low pressure
s_speed = state_sup[-1] # needed for the machines
state_sup = state_sup[:7]
if (state_low[1] > p_low) and (state_low[1] < p_high):
state_low_boil = my_fluid.set_state([state_low[1], 0],
"PQ") # saturated liquid at low pressure
state_high = my_fluid.set_state(
[temp_high, 1.], "TQ") # find high pressure, sat. vapor
if (state_high[1] < p_high and state_high[1] > p_low):
state_is = my_fluid.set_state(
[state_high[1], state_sup[4]], "PS") # isentropic compression
work_is = state_is[2] - state_sup[2]
work_80 = work_is / eff_isentropic
# state after compression with eff_isentropic
state_is80 = my_fluid.set_state(
[state_high[1], state_sup[2] + work_80], "PH")
# saturated liquid at high pressure
state_dew = my_fluid.set_state(
[state_high[1], 0], "PQ")
# check the deviation from linearity at high p
state_average = (state_high + state_dew) / 2
state_mid = my_fluid.set_state(
[state_high[1], state_average[2]], "PH")
lin_temp_deviation = (state_mid[0] - state_average[0])
if temp_limit and state_dew[0] > temp_low:
state_throttle = my_fluid.set_state([state_dew[2],
state_low[1]], "HP") # throtteling the liquid to low pressure
state_high_p_low__temp = my_fluid.set_state(
[state_high[1], temp_low], "PT") # high pressure cooled to low_t
state_throttle_low = my_fluid.set_state([state_high_p_low__temp[2],
state_low[1]], "HP")
results.append(np.array([*mole_fractions, *state_low,
*state_sup,
*state_high,
*state_is,
*state_is80,
*state_dew,
*state_mid,
*state_throttle,
*state_high_p_low__temp,
*state_throttle_low,
*state_low_boil]))
sound_speeds.append(s_speed)
lin_t_deviations_all.append(lin_temp_deviation)
except Exception as ex_message:
exception_messages.append(ex_message)
property_names = cb.fprop._fl_properties_names[:7]
results = np.array(results)
names = [*names, *[n+"_l" for n in property_names],
*[n+"_sup" for n in property_names],
*[n+"_h" for n in property_names],
*[n+"_is" for n in property_names],
*[n+"_is80" for n in property_names],
*[n+"_dew" for n in property_names],
*[n+"_mid" for n in property_names],
*[n+"_thr" for n in property_names],
*[n+"_hplt" for n in property_names],
*[n+"_thrlow" for n in property_names],
*[n+"_bol" for n in property_names]
]
dframe = pd.DataFrame(data=results, columns=names)
dframe.to_csv(fname+".csv")
add_data={}
add_data["speed_of_sound_sup"] = sound_speeds
add_data["p_difference"] = dframe["Pressure_h"] - dframe["Pressure_l"]
add_data["p_ratio"] = dframe["Pressure_h"] / dframe["Pressure_l"]
add_data["T_glide_h"] = dframe["Temperature_h"] - dframe["Temperature_dew"]
add_data["delta_T_mid"] = lin_t_deviations_all
add_data["dv_v''"] = 1 - (dframe[property_names[3]+"_thr"]
+ dframe[property_names[3]+"_dew"]) / \
(dframe[property_names[3]+"_is"] + dframe[property_names[3]+"_sup"])
if temp_limit:
add_data["dv_v''"] = 1 - (dframe[property_names[3]+"_thr"]
+ dframe[property_names[3]+"_dew"]) / \
(dframe[property_names[3]+"_is"] +
dframe[property_names[3]+"_sup"])
add_data["dv_v''_b"] = 1 - (dframe[property_names[3]+"_thrlow"] # does it help to subcool?
+ dframe[property_names[3]+"_hplt"]) / \
(dframe[property_names[3]+"_is"] + \
dframe[property_names[3]+"_sup"])
add_data["COP_is"] = (dframe[property_names[2]+"_is"]
- dframe[property_names[2]+"_dew"]) /\
((dframe[property_names[2]+"_is"]-dframe[property_names[2]+"_sup"]))
add_data["COP_is80"] = (dframe[property_names[2]+"_is80"]
- dframe[property_names[2]+"_dew"]) /\
((dframe[property_names[2]+"_is80"] -
dframe[property_names[2]+"_sup"]))
add_data = pd.DataFrame.from_dict(add_data)
all_data= pd.concat([dframe, add_data], axis=1)
all_data.to_csv(fname+".csv")
# Plot
figure, axes = plt.subplots(
figsize=(10, 10), layout="constrained", nrows=1, ncols=1)
fff = sbn.scatterplot(x="T_glide_h", y="p_ratio",
hue=names[0], size=names[1],
style=names[2], data=all_data.round(3), ax=axes)
sbn.move_legend(fff, "upper left", bbox_to_anchor=(1, 1))
axes.set_title(f"Mixture: {fluids_all}")
figure.savefig(fname+".png")
all_results["exception_messages"] = exception_messages
all_results["results_DataFrame"] = all_data
return all_results
[docs]def eval_is_eff_roskosch(data, file_out):
"""
Evalutes the data in the combined dataFrame with the initial fluid screening
and the output of the Roskosch compressor model (h_aus, s_aus, h_e) for
exactly the states
calculated along the screening. The column names are quite special and
one has to know that the Roskosch model calculates in kJ, while carbatpy
uses SI units (J). With the output enthalpy of the Roskosch model, the
**COP_comp** is calculated. Using the enthalpies and entropies along the
isobaric heat ransfer, mean temperatures are calculated.Here are again two
cases
.. line-block::
a) for throttling at quality=0
b) throttling after subcooling to T_low (names: *_lowT*).
With these mean
temperatures, the COPs for two reversible cases are calculated: for the
isentropic efficieciecy of 80% *COP_rev80* and for the Roskosch 'real'
case *COP_rev_r*. Finally, the (pseudo-)real COP is compared to the
reversible COP, giving a second law efficiency *eff_sec_law_r* for the
Roskosch efficiencies and *eff_sec_law_80* for the fixed 80% efficiency,
which include the
compressor and the throttling, but **no heat transfer**!
The Roskosch piston compressor model is described here:
http://dx.doi.org/10.1016/j.ijrefrig.2017.08.011
Is part of carbatpy.
Parameters
----------
data : pandas.dataFrame
as calculated by combining the fluid screening dataFrame with the
ouput of the Roskosch model (as dataFrame).
file_out : string
name of the file (incl. directory) where the resulting dataFrame shall
be stored.
Returns
-------
data : pandas.dataFrame
input expanded by the results.
"""
# mean low T, first with throttling at x=0, then with subcooling to T_low
# index name for the latter _lowT
new_data ={}
new_data["T_mean_low"] = (data['spec_Enthalpy_sup'] - data['spec_Enthalpy_thr']
) / (data['spec_Entropy_sup'] - data['spec_Entropy_thr'])
new_data["T_mean_low_lowT"] = (data['spec_Enthalpy_sup'] - data['spec_Enthalpy_thrlow']
) / (data['spec_Entropy_sup'] - data['spec_Entropy_thrlow'])
try: # if the Roskosch-model data are in the dataFrame
new_data["COP_comp"] = (data["h_aus"] * 1000 - data['spec_Enthalpy_dew']) /\
((data["h_aus"] - data["h_e"]) * 1000)
new_data["T_mean_high_is_r"] = (
data['h_aus'] * 1000 - data['spec_Enthalpy_dew'])/(data['s_aus'] - data['spec_Entropy_dew'])
new_data["COP_rev_r"] = data["T_mean_high_is_r"] / (data["T_mean_high_is_r"]
- new_data["T_mean_low"])
new_data["COP_rev_r_lowT"] = data["T_mean_high_is_r"] / (data["T_mean_high_is_r"]
- new_data["T_mean_low_lowT"])
new_data["eff_sec_law_r"] = data["COP_comp"] / data["COP_rev_r"]
new_data["eff_sec_law_r_lowT"] = data["COP_comp"] / data["COP_rev_r_lowT"]
except:
pass
# values for isentropic efficiency of 80% and throttling at a quality of 0
new_data["T_mean_high_is80"] = (data['spec_Enthalpy_is80'] - data['spec_Enthalpy_dew']) \
/ (data['spec_Entropy_is80'] - data['spec_Entropy_dew'])
new_data["COP_rev80"] = new_data["T_mean_high_is80"] / (new_data["T_mean_high_is80"]
- new_data["T_mean_low"])
new_data["eff_sec_law_80"] = data["COP_is80"] / new_data["COP_rev80"]
# values for isentropic efficiency of 80% and throttling at the low T and high p
new_data["T_mean_high_is80_lowT"] = (data['spec_Enthalpy_is80'] - data['spec_Enthalpy_hplt']) \
/ (data['spec_Entropy_is80'] - data['spec_Entropy_hplt'])
new_data["COP_rev80_lowT"] = new_data["T_mean_high_is80"] / (new_data["T_mean_high_is80"]
- new_data["T_mean_low_lowT"])
new_data["eff_sec_law_80_lowT"] = data["COP_is80"] / new_data["COP_rev80_lowT"]
new_data = pd.DataFrame.from_dict(new_data)
all_data= pd.concat([data, new_data], axis=1)
all_data.to_csv(file_out)
return all_data
[docs]def get_fluid(data):
"""
find the fluids used in the screening
Parameters
----------
data : pandas.dataFrame
dataFrame from fluid screening with mole fractions. In the column names
the names of the fluids are found.
Returns
-------
fluids : list of strings
names of the fluids.
fluid_col : list of strings
List with the column names (includes a sarting"x_".
fluid_str : string
Fluid composition string as accepted by RefProp.
"""
fluids = []
fluid_col = []
col_names = data.columns
for name in col_names:
if name.find("x_") > -1:
if name not in fluid_col: # no doubles
fluids.append(name[2:])
fluid_col.append(name)
fluid_str = "*".join(fluids)
return fluids, fluid_col, fluid_str
[docs]def combine(filenames, filename_out="automatic"):
"""
Combine two data frames out of two or more files with same number of lines
and fitting to each other. Can be used, when after fluid screening
machine efficienceies, costs,
etc. are calculated as post-processing. Can help in evaluation and
plotting.
Parameters
----------
filenames : list of strings
all filenames (incl. directories), to be read.
filename_out : string, optional
Where to store the result. The default is "automatic". Then the first
filename isxpanded vy "-combined".
Raises
------
ValueError
If tgere is a problem with the files.
Returns
-------
combined : pandas.dataFrame
the combined dataFrame.
"""
all_frames = []
if filename_out == "automatic":
fname_new = filenames[0].split(".")
filename_out = fname_new[0]+"-combined0." + fname_new[1]
try:
for which in filenames:
all_frames.append(pd.read_csv(which))
except Exception as excep:
text = f"{which} vs. {os.getcwd()}, {excep}"
raise ValueError(text) from excep
combined = pd.concat(all_frames, axis=1)
combined.to_csv(filename_out)
return combined
[docs]def data_plot(filename, what, filename_out="automatic", fig_title=""):
"""
Plotting a dataframe from a file using a dictionary with the keys
being the plotted parameters "x", "y", "hue" etc. and storing it to
a file.
Parameters
----------
filename : string
csv-file with the data-frame to be imported.
what : dictionary
keys "y","x","hue", "style", size etc. values must be some column names. .
filename_out : string, optional
where to store the plot, including directory. The default is "automatic".
fig_title : string, optional
Title of the figure to be plotted, default is "".
Returns
-------
bool
success?
"""
try:
dframe = pd.read_csv(filename)
set(what).issubset(set(dframe.columns))
except Exception as excep:
print(f"{what} not in columns!\n{excep}")
return False
# Plot
figure, axes = plt.subplots(
figsize=(10, 10), layout="constrained", nrows=1, ncols=1)
fff = sbn.scatterplot(x=what["x"], y=what["y"],
hue=what["hue"], size=what["size"],
style=what["style"], data=dframe.round(3), ax=axes)
sbn.move_legend(fff, "upper left", bbox_to_anchor=(1, 1))
axes.set_title(fig_title)
if filename_out == "automatic":
filename_out = filename.split(".")[0] + "-plot2.png"
figure.savefig(filename_out)
return True
[docs]def plot_cycle(filename, dataset):
try:
dframe = pd.read_csv(filename)
except Exception as excep:
print(f"Problem: {excep}")
return False
[docs]def get_cycle_points(data, index):
indices =range(7)
sup_names = [ "_l" ,
"_sup" ,
"_h" ,
"_is" ,
"_is80" ,
"_dew" ,
"_mid" ,
"_thr" ,
"_hplt" ,
"_thrlow" ,
"_bol"
]
n_points = len(sup_names)
points =np.zeros((len(indices),n_points))
for outer, variable in enumerate(indices):
property_name = cb.fprop._fl_properties_names[variable]
names = [property_name + sup for sup in sup_names]
points[outer,:] = data.loc[index, names]
return points
if __name__ == "__main__":
[docs] FLUIDS_ACTUAL = ["Propane", "Ethane", "Pentane",
"Butane"] # ["DME", "Ethane", "Butane","CO2"]
TEMP_LOW = 285.00
TEMP_HIGH = 363.00
PRESSURE_LOW = 10E4
PRESSURE_HIGH = 22E5
DIRECTORY_NAME = cb._RESULTS_DIR + r"\optimal_hp_fluid\fluid_select_restricted"
TEMPERATURE_LIMIT = True
warn = mixture_search(FLUIDS_ACTUAL, [TEMP_LOW, TEMP_HIGH],
[PRESSURE_LOW, PRESSURE_HIGH],
DIRECTORY_NAME, resolution=21,
temp_limit=TEMPERATURE_LIMIT)
#####################################################
directory = cb._CARBATPY_BASE_DIR
directory += "\\tests\\test_files\\"
filename1 = directory + r"test_data_ProEthPenBut\2024-02-06-16-51-ProEthPenBut.csv"
filename2 = directory + \
r"test_data_ProEthPenBut\2024-02-06-16-51-ProEthPenBut-compressor-Roskosch.csv"
combined_data = cb.utils.property_eval_mixture.combine([filename1,
filename2],
filename_out="automatic")
##############################################
what_act = {"x": 'spec_Volume_sup', "y": 'COP_is80', "hue": 'T_glide_h',
"size": 'p_ratio', 'style': 'Temperature_hplt'}
SUCCESS = data_plot(filename1, what_act)
############################################
fluids_act, fluid_col_act, fluid_str_act = get_fluid(combined_data)
#########################################
evaluated_data = eval_is_eff_roskosch(combined_data,
directory+'evaluated.csv')