The test from my previous lab notebook entry is still running, here is an updated analysis, it is up to 16 complete cycles now over 72 hours.
Code
import pandas as pd
from tqdm import tqdm, notebook
import numpy as np
import scipy
import plotly.express as px
import plotly.graph_objects as go
import kaleido
from IPython.display import Image
tqdm_disabled = True # True for website, change to False for local work
sampling = True
MIN_POINTS0 = 500
DIFF_LIMIT = 0.1
# electrolyte component masses, in g
MASS_ZnCl2 = 1.40
MASS_NH4Cl = 1.08
MASS_KI = 3.32
MASS_H2O = 8.51
MASS_TriEG = 0.58
total_mass_kg = (MASS_ZnCl2 + MASS_KI + MASS_H2O + MASS_TriEG)/ 1000.
TOTAL_VOLUME = 11 # electrolyte volume in mL, approx, measured by taking as much electrolyte as possible up into a 12 mL syringe
MASS_TO_RESERVOIRS = 14.75 # g of electrolyte actually loaded into system, based on weighing syringe before/after loading reservoirs
# molecular weights in g/mol
density = MASS_TO_RESERVOIRS/ TOTAL_VOLUME
MW_ZnCl2 = 136.315
MW_NH4Cl = 53.49
MW_KI = 166.0028
MW_H2O = 18.01528
MW_TriEG = 150.174
molality_ZnCl2 = MASS_ZnCl2/ MW_ZnCl2/ total_mass_kg
molality_NH4Cl = MASS_NH4Cl/ MW_NH4Cl/ total_mass_kg
molality_KI = MASS_ZnCl2/ MW_KI/ total_mass_kg
molality_TriEG = MASS_TriEG/ MW_TriEG/ total_mass_kg
molality_H2O = MASS_H2O/ MW_H2O/ total_mass_kg
molarity_ZnCl2 = MASS_ZnCl2/ MW_ZnCl2/ TOTAL_VOLUME* 1000.
molarity_NH4Cl = MASS_NH4Cl/ MW_NH4Cl/ TOTAL_VOLUME* 1000.
molarity_KI = MASS_ZnCl2/ MW_KI/ TOTAL_VOLUME* 1000.
molarity_TriEG = MASS_TriEG/ MW_TriEG/ TOTAL_VOLUME* 1000.
molarity_H2O = MASS_H2O/ MW_H2O/ TOTAL_VOLUME* 1000.
filenames = ["../lab-notebook-9/23-03-2026-KPS-5.zip" ]
all_data = []
for f in filenames:
if len (all_data) == 0 :
if "Potentiostat_project" in f:
all_data.append(pd.read_csv(f))
else :
all_data.append(pd.read_csv(f, delimiter= " \t " ))
else :
df0 = pd.read_csv(f, delimiter= " \t " )
df0["Elapsed time(s)" ] += all_data[- 1 ]["Elapsed time(s)" ].iat[- 1 ]
all_data.append(df0)
df = pd.concat(all_data, ignore_index= True )
if not tqdm_disabled:
print ("Electrolyte Composition:" )
print ("Molarities (moles/L solution): {:.2f} M ZnCl~2~, {:.2f} M NH~4~Cl, {:.2f} M KI, {:.2f} M triethylene glycol, {:.2f} M H~2~O \n " .format (molarity_ZnCl2, molarity_NH4Cl, molarity_KI, molarity_TriEG, molarity_H2O))
print ("Molalities (moles/kg solution): {:.2f} m ZnCl~2~, {:.2f} m NH~4~Cl, {:.2f} m KI, {:.2f} m triethylene glycol, {:.2f} m H~2~O \n " .format (molality_ZnCl2, molality_NH4Cl, molality_KI, molality_TriEG, molality_H2O))
print ("Density approx. {:.1f} g/mL \n " .format (density))
print ("Experiment length: {:.1f} hours" .format (all_data[- 1 ]["Elapsed time(s)" ].iat[- 1 ]/ 3600. ))
df["mean_current" ] = df["Current(A)" ].rolling(3 ).mean()
df["prev_current" ] = df["mean_current" ].shift(- 1 )
df["VChange" ] = df["Potential(V)" ].diff().abs ()
df["is_change" ] = (
((df["mean_current" ] > 0 ) & (df["prev_current" ] < 0 ))
| ((df["mean_current" ] < 0 ) & (df["prev_current" ] > 0 ))
).astype(int )
idx_changes = list (df[df["is_change" ] == 1 ].index)
idx_changes.append(len (df) - 1 )
all_curves = []
idx_start = 0
for idx in tqdm(idx_changes, disable= tqdm_disabled):
if len (df.iloc[idx_start:idx, :]) > 50 :
all_curves.append(df.iloc[idx_start:idx, :])
idx_start = idx
results = []
n_curves = np.max ([1 , int (np.floor(len (all_curves) / 2 ))])
for CN in notebook.tnrange(n_curves, disable= tqdm_disabled):
CURVE_N1 = CN * 2
CURVE_N2 = CN * 2 + 1
# Process charge data
if sampling:
N_TERM_POINTS = int (np.min ([MIN_POINTS0, len (all_curves[CURVE_N1]) / 2.0 ]))
MIN_POINTS = int (
np.min ([MIN_POINTS0, len (all_curves[CURVE_N1]) - N_TERM_POINTS * 2 ])
)
df0 = pd.concat(
[
all_curves[CURVE_N1].iloc[:N_TERM_POINTS],
all_curves[CURVE_N1]
.iloc[N_TERM_POINTS:- N_TERM_POINTS]
.sample(n= MIN_POINTS),
all_curves[CURVE_N1].iloc[- N_TERM_POINTS:],
]
).sort_values("Elapsed time(s)" , ascending= True )
df0 = df0[df0["VChange" ] < DIFF_LIMIT]
else :
df0 = all_curves[CURVE_N1].copy()
df0["mAh" ] = np.abs (
scipy.integrate.cumulative_trapezoid(
df0["Current(A)" ], df0["Elapsed time(s)" ], initial= 0
)
* 1000.0
/ 3600.0
)
total_energy0 = scipy.integrate.cumulative_trapezoid(
df0["Current(A)" ].abs () * df0["Potential(V)" ],
df0["Elapsed time(s)" ],
initial= 0.0 ,
)[- 1 ]
# Process discharge data
if sampling:
N_TERM_POINTS = int (np.min ([MIN_POINTS0, len (all_curves[CURVE_N2]) / 2.0 ]))
MIN_POINTS = int (
np.min ([MIN_POINTS0, len (all_curves[CURVE_N2]) - N_TERM_POINTS * 2 ])
)
df1 = pd.concat(
[
all_curves[CURVE_N2].iloc[:N_TERM_POINTS],
all_curves[CURVE_N2]
.iloc[N_TERM_POINTS:- N_TERM_POINTS]
.sample(n= MIN_POINTS),
all_curves[CURVE_N2].iloc[- N_TERM_POINTS:],
]
).sort_values("Elapsed time(s)" , ascending= True )
df1 = df1[df1["VChange" ] < DIFF_LIMIT]
else :
df1 = all_curves[CURVE_N2].copy()
df1["mAh" ] = np.abs (
scipy.integrate.cumulative_trapezoid(
df1["Current(A)" ], df1["Elapsed time(s)" ], initial= 0.0
)
* 1000.0
/ 3600.0
)
total_energy1 = scipy.integrate.cumulative_trapezoid(
df1["Current(A)" ].abs () * df1["Potential(V)" ],
df1["Elapsed time(s)" ],
initial= 0.0 ,
)[- 1 ]
CE = 100.0 * (df1["mAh" ].iloc[- 1 ] / df0["mAh" ].iloc[- 1 ])
EE = 100.0 * (total_energy1 / total_energy0)
VE = 100.0 * EE / CE
results.append(
{
"Number" : CN + 1 ,
"CE" : CE,
"VE" : VE,
"EE" : EE,
"Charge_potential" : df0["Potential(V)" ].mean(),
"Discharge_potential" : df1["Potential(V)" ].mean(),
"Charge_stored" : df1["mAh" ].iloc[- 1 ] / TOTAL_VOLUME,
"Energy_density_discharge" : total_energy1 / TOTAL_VOLUME / 3600.0 * 1000 ,
}
)
# Save the modified DataFrames back to the all_curves list
all_curves[CURVE_N1] = df0
all_curves[CURVE_N2] = df1
results_df = pd.DataFrame(results)
# results_df = results_df[:10] # lab notebook #9 was written only after first 10 cycles
if not tqdm_disabled:
print (results_df)
print ("" )
print (results_df.mean())
# Plot charge/discharge curves
fig1 = go.Figure()
for CN in range (n_curves):
CURVE_N1 = CN * 2
CURVE_N2 = CN * 2 + 1
fig1.add_trace(
go.Scatter(
x= all_curves[CURVE_N1]["mAh" ] / TOTAL_VOLUME,
y= all_curves[CURVE_N1]["Potential(V)" ],
mode= "lines" ,
name= f"Charge { CN+ 1 } " ,
line= dict (color= "blue" , dash= "solid" ),
)
)
fig1.add_trace(
go.Scatter(
x= all_curves[CURVE_N2]["mAh" ] / TOTAL_VOLUME,
y= all_curves[CURVE_N2]["Potential(V)" ],
mode= "lines" ,
name= f"Discharge { CN+ 1 } " ,
line= dict (color= "grey" , dash= "solid" ),
)
)
fig1.update_layout(
title= "Charge and Discharge Curves" ,
xaxis_title= "Capacity (Ah/L)" ,
yaxis_title= "Potential (V)" ,
)
fig1.show()
Code
# Plot efficiency
fig2 = px.scatter(
results_df,
x= "Number" ,
y= ["VE" , "CE" , "EE" ],
labels= {"value" : "Efficiency (%)" , "variable" : "Metric" },
title= "Efficiency by Cycle" ,
)
fig2.update_traces(mode= "markers" )
fig2.update_layout(\
yaxis= dict (range = [- 10 , 100 ])
)
fig2.show()
# Plot potential
# fig3 = px.scatter(results_df, x="Number", y=["Charge_potential", "Discharge_potential"],
# labels={"value": "Potential (V)", "variable": "Metric", "Number": "Cycle Number"},
# title="Mean Potential by Cycle")
# fig3.show()
Code
# Plot discharge charge capacity
# fig4 = px.scatter(results_df, x="Number", y="Charge_stored",
# labels={"Charge_stored": "Discharge Capacity (Ah/L)", "Number": "Cycle Number"},
# title="Discharge Capacity by Cycle")
# fig4.show()
# Plot discharge energy capacity
fig5 = px.scatter(
results_df,
x= "Number" ,
y= "Energy_density_discharge" ,
labels= {
"Energy_density_discharge" : "Energy Density on Discharge (Wh/L)" ,
"Number" : "Cycle Number" ,
},
)
fig5.show()
Okay, Figure 3 is interesting. There appears to be some periodic behavior of increasing capacity and then a sharp drop, like a wave. I think this is due to fluid transfer between the reservoirs.
To explain—flow batteries, especially those with porous separators, have problems with volume imbalance due to differing osmotic and mechanical pressures, water transfer, basically all the different transport phenomena going on at the same time through a porous membrane with two electrolytes with different intrinsic properties (when charged, at least).
If you have a symmetric system, like this, you can remedy this just by transferring the electrolyte from one reservoir back to the other. I did this a lot during my PhD. I even built a system to do it automatically by controlling pump speeds with a PID controller hooked to a camera that monitored reservoir levels, and wrote a paper on it [1 ] . That paper contains more background on the issue.
That approach relied on clear reservoirs though so we can’t use it here. It was also an active control system, and a passive one would be better.
To solve this simply, I have designed the reservoirs with a sort of spillover between them, so that they are connected. Here is a transparent FreeCAD view showing the internal connection.
So, what I think is happening, is that volume imbalance builds up, then electrolyte flows between one reservoir to the other. This discharges the cell somewhat, resulting in a loss of capacity, but it keeps the imbalance limited. The process then repeats itself it seems.
I could try to validate this visually, but likely will wait until a larger system makes this easier to observe. For now it’s interesting to see in the data.
Code
table_df = (
results_df.describe().loc[["mean" , "std" ]]
.round (decimals= 1 )
.drop(columns= ["Number" , "Charge_potential" , "Discharge_potential" ])
.rename(
columns= {
"CE" : "Coulombic Efficiency (%)" ,
"EE" : "Energy Efficiency (%)" ,
"VE" : "Voltaic Efficiency (%)" ,
"Charge_stored" : "Discharge Capacity (Ah/L)" ,
"Energy_density_discharge" : "Energy Density (Wh/L)" ,
}
)
)
# Bar chart of efficiencies with error bars
eff_cols = ["Coulombic Efficiency (%)" , "Voltaic Efficiency (%)" , "Energy Efficiency (%)" ]
eff_labels = ["Coulombic" , "Voltaic" , "Energy" ]
means = table_df.loc["mean" , eff_cols].values
stds = table_df.loc["std" , eff_cols].values
Code
fig6 = go.Figure()
fig6.add_trace(go.Bar(
x= eff_labels,
y= means,
error_y= dict (type = "data" , array= stds, visible= True ),
name= "Efficiency" ,
marker_color= ["#1f77b4" , "#ff7f0e" , "#2ca02c" ]
))
fig6.update_layout(
yaxis_title= "Efficiency (%)" ,
yaxis= dict (range = [0 , 100 ])
)
fig6.show()
Code
cap_cols = ["Discharge Capacity (Ah/L)" ]
cap_labels = ["Discharge Capacity" ]
cap_means = table_df.loc["mean" , cap_cols].values
cap_stds = table_df.loc["std" , cap_cols].values
fig7 = go.Figure()
fig7.add_trace(go.Bar(
x= cap_labels,
y= cap_means,
error_y= dict (type = "data" , array= cap_stds, visible= True ),
name= "Capacity" ,
marker_color= "#1f77b4"
))
fig7.update_layout(
yaxis_title= "Discharge Capacity (Ah/L)"
)
fig7.show()
Code
ed_cols = ["Energy Density (Wh/L)" ]
ed_labels = ["Energy Density" ]
ed_means = table_df.loc["mean" , ed_cols].values
ed_stds = table_df.loc["std" , ed_cols].values
fig8 = go.Figure()
fig8.add_trace(go.Bar(
x= ed_labels,
y= ed_means,
error_y= dict (type = "data" , array= ed_stds, visible= True ),
name= "Energy Density" ,
marker_color= "#2ca02c"
))
fig8.update_layout(
yaxis_title= "Discharge Energy Density (Wh/L)"
)
fig8.show()
Gonna let this cell cycle over the weekend, fingers crossed!
References
[1]
K.P. Smith, C.W. Monroe, Image-based mechanical balancing of reservoir volumes during benchtop flow battery operation, Frontiers in Chemical Engineering 3 (2021). https://doi.org/
10.3389/fceng.2021.748865 .
Citation BibTeX citation:
@online{smith2026,
author = {Smith, Kirk Pollard},
title = {Managing Electrolyte Volume Imbalance in Flow Battery Testing
/ {Lab} {Notebook} {Entry} \#10},
date = {2026-03-27},
url = {https://dualpower.supply/posts/lab-notebook-10/},
langid = {en}
}
For attribution, please cite this work as: