NASA i zalecany sposób ładowania akumulatorków Ni-Cd oraz Ni-Mh: Link Szczegółową analizę i czytelny PDF umieściłem w w załączniku. Polska strona: Link Od siebie dodam, że metodę zalecaną przez NASA, od wielu lat stosuję we własnych ładowarkach akumulatorków Ni-Mh.
INVESTIGATION OF THE RESPONSE OF NIMH CELLS TO BURP CHARGING
the Faculty of the Department of Chemical Engineering
University of Houston
In Partial Fulfillment of the Degree
Doctor of Philosophy
in Chemical Engineering
Eric C. Darcy
INVESTIGATION OF THE RESPONSE OF NIMH CELLS TO BURP CHARGING
Eric C. Darcy
Chairman of the Committee
Kishore Mohanty, Professor
Demetre J. Economou, Professor
Richard Willson, Professor
Allan J. Jacobson, Professor,
Scott S. Perry, Assistant Professor,
Richard Pollard, Scientist and Technical Leader,
The Dow Chemical Company
Charles Dalton, Associate Dean,
Cullen College of Engineering
James T. Richardson, Professor and Chairman,
The advice and support of a number teachers, supervisors, colleagues, friends, and family made
this work possible for which I wish to express enormous gratitude.
Dr. R. Pollard's guidance, insightful advice, and unwavering support as my research advisor has
been invaluable. Dr. K. Mohanty also deserves thanks for volunteering to be my advisor at the end in
place of Dr. Pollard. Also instrumental are my supervisors during the work, T. Davies, B. Wittschen,
and W. Brasher. They made possible the resources to work on this endeavor and had the necessary
patience while some of my "real" NASA work was delayed.
Bill Tipton provided me with what seem to be an endless supply of KOH solutions along very
useful laboratory experimental advice. Glenn Morgan's assistance during the SEM and EDS work
deserves recognition. The detailed electrical design of the battery cycler would not have been possible
without S. Hossain and B. Hughes must be commended for his persistence to keep it free of hardware
I want thank my co-workers, B. Bragg, E. Kluksdahl, D. Allison, and S. Lazaroff for their
encouragement and for stepping-in to take on some of my NASA always growing projects, which
allowed me to dedicate more time to this work. Also deserving thanks are my mountain climbing
buddies D. Schneider, D. Young, and T. Barrera, who along with my Dad, provided the necessary
nagging reminders that I needed to stay on course, by perpetually asking me, "How is that thesis going?
The final compilation of this work would not have been possible without the selfless help of my inlaws, Paul and Rosetta. They are fantastic grand-parents, particularly to our 2 year old daughter, and
they stood in for me while I was away for many nights and week-ends compiling this dissertation.
Finally, I must thank my wife, Cheryl, for her incredible patience, tremendous love, and her
understanding support through some difficult times along the journey of this work. A better friend, I
could not have.
INVESTIGATION OF THE RESPONSE OF NIMH CELLS TO BURP CHARGING
the Faculty of the Department of Chemical Engineering
University of Houston
In Partial Fulfillment of the Degree
Doctor of Philosophy
in Chemical Engineering
Eric C. Darcy
Performance cycling and calorimetric analysis of nickel metal hydride cells have revealed that reverse
pulse ("burp") charging improves performance over other charging techniques. Burp charging
periodically applies a short-duration, high-rate discharge pulse followed by a short rest during an
otherwise galvanostatic charge. Results show improved charge input and output, lower heat generation
during charge, lower charge overvoltage, and no loss of cycle life. Several hypotheses for the
responsible phenomena were examined. In-situ video-microscopic analysis of the cell and its nickel
electrode during charge revealed the significance of the gas evolution reactions. In-situ gas generation
rate measurements made manometrically during charge determined that the burp pulse sequence results
in less gas generation than galvanostatic charging. Evidence is presented that the "burp" pulse sequence
electrochemically consumes gas bubbles generated during charge at the positive and negative electrodes,
respectively. Removing bubbles increases the effective electrode surface area, results in a lower charge
overvoltage, and reduces cell pressure.
TABLE OF CONTENTS
1.0 Introduction (Chapter 1)
1.1 Statement of the Problem..........................................................................
1.3 Background and Review of Previous Work.....................................................
2.0 Description of Experiment (Chapter 2)
2.1 Performance Cycling...............................................................................
2.2 Cell Calorimetry....................................................................................
2.3 Destructive Physical Analysis.....................................................................
3.0 Results and Discussion (Chapter 3)
3.1 Performance Cycling..............................................................................
3.2 Cell Calorimetry....................................................................................
3.3 Destructive Physical Analysis.....................................................................
3.6 Summary and Conclusions (Chapter 4)...............................................................
A. Design, Specifications, and Operation of Battery Cycling Experiment.....................
B. Design, Specifications and Operation of Cell Calorimetry Experiment....................
C. Set-up and Procedure for Destructive Physical Analysis......................................
D. Set-up and Procedure for Video-Microscopy...................................................
E. Set-up and Procedure for Manometry............................................................
LIST OF FIGURES
Typical reverse pulse (burp) current waveform.
Simple galvanostatic charging effects on cycle life.
Smart versus simple galvanostatic charging. Comparison of discharge output versus cycle life.
Burp charging versus smart galvanostatic charging. Comparison of discharge output versus cycle
Calorimetric comparison of galvanostatic and pause charging. Charge heat and voltage
comparison versus time.
Calorimetric comparison of the three charge waveforms. Charge heat and overvoltage versus
Comparison of the charge overvoltage and gas generation of three charge methods (burp, pause,
and galvano) versus runtime with the same nickel metal hydride cell. Initiation of 2nd
charge/discharge cycle for each method was at a runtime of 0 minutes. Gas generation volume
indicated by centimeters of water displaced in a manometer. Current levels; Burp at 2.000A,
Pause at 1.974A, Galvano at 1.915A.
Comparison of the end of charge with exaggerated pause and burp waveforms versus runtime
with the same nickel metal hydride cell. Initiation of the charge was at a runtime of 0 minutes.
Voltage and gas evolution curves versus runtime during a charge rest period followed by cell
discharge into a 0.5 ohm load.
Comparison of voltage and gas levels in a flooded and nominal cell during galvanostatic charge
at 1.915A, rest, and resistive discharge at 0.5 ohm.
Cell gas and voltage level during charging of a flooded NiMH cell. Comparison of galvanostatic,
pause, and burp charge methods.
Automated 10 Station Battery Cycler with adjacent calorimeter. Power supplies are
adjacent to Charger Assembly Racks. Batteries are positioned in 3 layer holder placed on top of
Close-up of a charger assembly rack partially retreated from its slot to show its charger
controller IC on printer circuit board in front of small fan.
Cross section of cell calorimetry experiment.
Schematic of the in-situ video-microscopic experiment. Charge/discharge cycler and electrical
connections not shown for clarity.
Configuration of nominal cell with manometer. Glass spheres taking up extra volume in cylinder
containing cell are not shown for clarity. Cell had small hole drilled into its negative end.
LIST OF FIGURES (Cont.)
Configuration of flooded cell with manometer. Cell had small holes drilled into its negative and
LIST OF TABLES
Description of waveforms compared during video-microscopic experiments.
Nickel electrode surface area and pore volume comparison.
Comparison particle size distribution of metal hydride electrodes with each charge technique.
Industrial jargon for a short-duration, high-rate discharge pulse during charge
The discharge or charge current, in amperes, expressed as multiple of the rated capacity
Destructive Physical Analysis
Energy Dispersion Spectroscopy
General Purpose Instrument Bus
Johnson Space Center
Light emitting diode
National Aeronautics and Space Administration
Nickel metal hydride
Negative to positive electrode active mass ratio
Open circuit voltage
Random access memory
Scanning Electron Microscopy
Talker Listener Device
Virtual Instrument, LabVIEW(R) subroutine
CHAPTER 1: INTRODUCTION
1.1 Statement of the Problem
Over the last 20 or more years, numerous alternatives to galvanostatic (constant current) battery
charging have been tried in a more or less trial and error approach to minimize charge time and/or maximize
battery discharge performance of rechargeable batteries without sacrificing their cycle life. One particular
periodic method, called "burp" charging, uses a very short reverse (discharge) pulse followed by a short
pause in an otherwise galvanostatic charge regime . This method, also called reflex charge, has been
reported to improve the performance and life of commercial nickel cadmium (NiCd) batteries [2, 3]. In
addition, results of my cycling tests demonstrate the improved performance and cycle life of sealed
commercial nickel metal hydride (NiMH) batteries when using burp charging. These results are detailed in
Chapter 3 herein.
The problem is that, to my knowledge, there is no clear, supported explanation of the phenomena
responsible for how and why cells (particularly, sealed NiMH cells) benefit from this alternative waveform.
The proliferation of consumer, industrial, military, and aerospace applications for rechargeable
batteries have resulted in a world wide battery industry with annual sales exceeding $20 billion and growing
every year at a rapid rate thanks to advances in consumer electronics, lower power requirements, and the
increasing demand for portable electronic products . Future battery sales will escalate by many factors if
and when electric vehicles become a more prominent alternative to current internal combustion vehicles.
The great majority of NiCd, NiH2, and NiMH cells are designed with the positive nickel electrode
being active material limited because excess negative electrode active material is needed to recombine the
inevitable oxygen gas produced during charging and overcharging. Typical N:P (negative to positive active
material) ratios range from 1.25 to 1.95 for typical NiCd and NiMH cell designs [5, 6]. Keeping the cell gas
pressure within levels that do not require thick cell casing and/or relief valve operation is critical. If excess
pressure is vented, water and/or reactants are lost. This alters the relative states of the charge of the
electrodes, leads to higher internal resistance, and eventually degrades cycle life. The amount of excess
negative electrode active material designed into a cell is related to the expected rates of oxygen generation
at the nickel electrode during charging. The negative hydride electrode mass makes up about 50% of typical
current commercial cell designs . Thus, any charge method which reliably reduces that oxygen
generation rate allows a reduction in the N:P ratio and make feasible higher capacity and higher energy
density cell designs.
Consequently, any charge method which improves battery performance and life can have a very
significant impact on current and future battery designs. This is particularly true with aerospace battery
applications where batteries with higher gravimetric and volumetric energy densities and longer cycle life
are always aggressively sought.
Furthermore, today's commercial burp chargers, available in an integrated circuit, apply the
current waveform consistently at about 1 Hz throughout the charge sequence. A typical burp charge current
waveform is shown in Figure 1. The 5 millisecond discharge pulse current level is typically set at
-2.5 times the charge current level. Including its 29 millisecond current pause, one cost of the burp
waveform is that it effectively charges at a rate 5% slower than a galvanostatic waveform set at the same
charge current. Understanding the phenomena responsible for the benefits of this sequence will guide
improvements. For example, would a variable frequency burp charging waveform which increases
frequency with increasing state of charge (hence, with increasing oxygen gas generation rate) be more
effective? What role does the 24 millisecond pause after the "burp" play in producing the observed effect?
Which is more beneficial, the pause or the burp?
Charge current, A
Waveform period = 1.076 s
5 ms discharge burp
Fig. 1. Typical reverse pulse (burp) current waveform.
1.3 Review of Previous Work
With the Ni-Cd, Ni-H2, and Ni-MH cells, at the positive electrode, nickel hydroxide (Ni(OH)2) is
the discharged active material and is oxydized to nickel oxyhydroxide (NiOOH) to become the charged
active material during charge by the following electrochemical half-reaction;
Ni(OH)2 + OH ? NiOOH + H2O + e .
Competing with this reaction, is the undesirable oxygen gas evolution half-reaction,
4OH ? O2? + 2H2O + 4e .
The degree of absence of reaction 2 largely determines the charge efficiency. It is generally
observed that charge efficiency increases with decreasing temperature and vice-versa. This is because the
oxygen evolution potential varies more with temperature than does the potential for reaction 1 . Cell
manufacturers put additives such as lithium and cadmium in the nickel electrode to raise this oxygen
overpotential or reduce the nickel oxidation potential to obtain decent charge efficiency at higher
temperatures . Generally, at the beginning of charge, reaction 1 is highly preferred over reaction 2, but,
as the state of charge increases with the charge overpotential applied, the oxygen evolution reaction
becomes more significant. If charging is continued after nearly all the nickel hydroxide has been oxidized,
then reaction 2 will be a prominent overcharge reaction and large amount of bubbling can be expected at the
For the NiMH cell, the electrochemical half-reaction on the metal hydride electrode during charge
M + H2O + e ? MH + OH .
As mentioned before, sealed-cell designers typically put in more negative active material (MH)
than positive active material to keep hydrogen pressures lower and help recombine the oxygen gas
generated during overcharge by the following chemical reaction [4, 9],
4MH + O2? ? 4M + 2H2O.
This requires oxygen gas transport from the positive electrode, through the separator, and to the
negative electrode. The combination of reactions 2, 3, and 4 results (at least on paper) in no electrochemical
or chemical change in the cell. Ideally, reaction 4 is sufficiently facile to prevent the build up of oxygen gas
and prevent the negative hydride electrode from being fully charged which would result in the build up of
hydrogen gas via,
2H2O + 2e
H2? + 2OH ,
which generates hydrogen gas by water electrolysis during charge. However, if reaction 2 produces oxygen
gas at a faster rate than reaction 4 can consume it, then cell pressure builds up. This can lead to cell
venting, leading to permanent cell failure.
Reaction 5 is an undesirable electrochemical alternative to reaction 3. It was recently determined
that reaction 5 is not only a significant overcharge reaction but can be prevalent during charging at high
rates due to diffusion limitations of adsorbed atomic hydrogen into the bulk of certain metal hydrides 
via the following mechanism;
2Hads + 2OH
2Hads + 2M
2H2O + 2e
In other words, if reaction 7 is not fast enough to prevent accumulation of the necessary adsorbed
atomic hydrogen on the metal hydride surface, these atomic hydrogens will prefer to form hydrogen gas to
achieve reaction 5 via the reaction 6 followed by reaction 8 [11, 12, 13, 14];
In summary, the goal of any good charger is to maximize the charge acceptance of a battery while
minimizing the heat and pressure build up in cells. In other words, minimize reaction 2 and 5 by monitoring
cell parameters for the proper indication of the onset of overcharge. Unfortunately, cell pressure is not a
parameter that can be practically monitored in cost conscious batteries. Furthermore, in multiple cell
batteries monitoring the pressure of only one cell is risky due to inevitable cell-to-cell temperature
variations, and alternatively monitoring that of all cells is inherently complex.
Since their inception, a large majority of commercial NiCd and NiMH batteries have been and are
charged galvanostatically. The only differences in the various galvanostatic charge methods lie with the
termination algorithm used. Voltage, voltage slope, temperature, and temperature slope termination
algorithms are the most common algorithms in commercial chargers today .
Many charge waveforms and termination algorithms have been and are still being tried today in the
pursuit of the optimum charge method. The burp charge waveform was first patented in the late 1960s ,
licensed in 1990 into a commercial integrated circuit, P/N ICS1700, and later redesigned with a soft start
condition and improved termination algorithms to become the ICS1702 . It has achieved commercial
success and is a preferred method for NASA's space battery applications using commercial NiCd and
NiMH cells, without an accepted understanding of the phenomena involved. To date, several possible
explanations have been offered to explain why burp charging improves NiCd and NiMH battery
performance over other charge techniques. None to date has been offered with what I consider convincing
Nevertheless, here are three such hypotheses;
1) Burp charging prevent/retards porosity and granular morphology changes in the porous electrodes with
continual cycling. The reverse pulses prevent formation of large crystals of charged active material .
Larger crystals cause porosity to increase or decrease. Greater porosity can cause detachment of active
material from the electrode. The reduction of active material participating in the electrochemical
reaction can increase charge overvoltage. Similarly, a loss of porosity (densification) can impede ion
transport leading to increases in charge overvoltage. Particularly for the metal hydride electrode,
particle size changes have been found experimentally [17, 18, 19, 20] and theoretically  to have
large effects on the electrode's electrochemical properties and their cycle life [22, 23].
2) Burp charging dislodges oxygen bubbles produced on and masking the active nickel electrode surface.
Theoretically, it has been shown that displacing masking bubbles augments the effective surface area of
the electrode and produces a corresponding reduction in charge overvoltage . Lowering the
overvoltage reduces charge heat generation and the tendency for oxygen evolution.
3) Burp charging depolarizes the electrode surface by pulling ions away from the electrode surfaces and
which ionically agitates the inner Helmholtz plane  as a result of a double layer capacitance effect.
This agitation facilitates gas diffusion .
This thesis is organized in the following manner; Chapter 2 contains the experimental techniques
used to demonstrate and understand the performance differences between burp charging and other methods.
Chapter 3 contains a discussion of the results of each experimental technique. Chapter 4 summarizes the
findings and conclusions of the work.
CHAPTER 2: EXPERIMENTAL
2.1 Performance Cycling
Commercial NiMH 4/3A cells from Sanyo rated at 2400 mAh (P/N HR-4/3AU) were selected for
this focused comparison of charge methods because my earlier tests demonstrated their consistent cycling
performance relative to competing cell designs. This cell design consists of a foam positive nickel electrode,
an AB5 mischmetal hydride negative electrode, and polypropylene separator. Cells were assembled into 4
cells-in-series packs and cycled 400 times at a C-rate for both the charge and discharge phases. In all cases,
the discharge was terminated 1.0V/cell which is considered as 100% depth-of-discharge. Four different
charge techniques were evaluated.
Galvanostatic to a maximum temperature (45 °C)
b) Galvanostatic to a negative voltage slope or a temperature slope (Galvanostatic)
Burp waveform to a voltage inflection point, or a temperature slope (Burp)
d) Pause waveform is the burp waveform with the discharge pulse replaced by a rest. (Pause)
The control of the burp waveform and termination was achieved using an integrated circuit (IC)
named the ICS1702 QuickSaver(R) . This IC achieved the short discharge pulse by momentarily
switching the battery to a calibrated resistor sized to provide about -5A. The pause waveform was achieved
by removing this discharge resistor to make the current equal to zero. The galvanostatic waveform was
controlled by an IC named bq2003 made by Benchmarq which relies on a negative voltage slope or in a rise
in temperature for its termination algorithms. The charger circuits monitored battery temperature with
negative thermal coefficient thermistors.
Up to ten battery packs were cycled while in a thermal chamber set at 25 °C. The control of the
cycling of each of 10 battery packs was done independently. I developed a computer program to automate
the cycling of all the packs. The cycling was operated without interruption for 400 cycles over a six week
period. With a C-rate charge and a C-rate discharge and only 5 minute rests in-between transitions, about 10
cycles a day were achieved. Battery voltage, current, and temperature were recorded at about 0.1 Hz
throughout the cycling. Voltage and current were measured to ? 1 mV and ? 1 mA resolution while
temperature was measured to ? 0.1 °C.
More detailed descriptions of the test articles, test set-up, equipment used, and test conditions of
the performance cycling experiments are in Appendix A.
2.2 Cell Calorimetry
Calorimetry was employed to quantitatively determine cell thermal response differences between
the various charge methods. After achieving 400 cycles, one of the 4 cells from each pack was separated
from the pack in order to place it in the chamber of a Hart Scientific heat conduction calorimeter. Once in
place, the cell was reconnected in series with its original pack. One battery pack at a time was cycled with
the same charge method as before. In addition to the battery parameters monitored as before, the cell
voltage and heat from the cell in the calorimeter were recorded as well. The calorimeter chamber was
controlled to 23 °C and maintained within a ? 0.01 °C. Cell voltage and heat were measured to ? 1 mV and
? 0.1 mW, respectively.
The thermal time constant of this calorimeter is about 6 minutes. Thus, to isolate the heat
measurements from charging and discharging phases, a two hour rest period followed the charge and a 30
minute rest followed the discharge. This permitted the heat measurement to return to equilibrium before
starting the next phase and enhanced the accuracy of area under the curve calculations (i.e. thermal energy).
Thirty cycles were performed this way on each battery pack before repeating with the next pack and charge
method. Each pack was charged with the same waveform and termination algorithm used to accumulate its
previous 400 cycles.
More detailed descriptions of the test articles, test set-up, equipment used, and test conditions of
the calorimetric experiments are in Appendix B.
2.3 Destructive Physical Analysis
To investigate the first hypothesis concerning changes in electrode morphology, cycled cells were
disassembled in an argon filled glove box to extract active material samples from both electrodes. The
samples were examined with Scanning Electron Microscopy (SEM) and Energy Dispersion Spectroscopy
(EDS) to visually and elementally compare the surfaces, respectively. Additional analysis included the
surface area and pore size distribution of the positive electrode samples and the particle size distribution of
the negative electrodes. Samples from cells with 400 burp, pause, and galvanostatic cycles were compared
to cells charged once galvanostatically.
More detailed descriptions of the cell disassembly method, of the electrode sample preparation,
and of the analysis instrumentation are in Appendix C.
Video-microscopy was used to qualitatively observe changes in cell gasing activity while under the
various charging methods. The electrode coil was extracted from its cell can and placed in a transparent
beaker. A 6.4 M potassium hydroxide (KOH) solution was used to immersed a 1/4 of the coil. That lower
portion of the electrode coil had a portion of its outer separator layers and outer hydride electrode cut away
to view the nickel electrode with a video-microscope. This was achieved by uncoiling the coil to scissor cut
an aperture. Coil compression was regained with Tefzel(R) tie-wraps. The beaker used was made of
transparent polymethylpentene which resists attack from alkaline solutions. Electrical leads were fed
through a customized rubber stopper to enable cycling the cell while sealed.
The video-microscope (model PV-10 manufactured by Olympus) and lens system used provided a
variable zoom capability from 10X to 70X magnification. The system was connected to a television monitor
with a videocassette recorder.
The cell was cycled with each of the three charge techniques (galvanostatic, pause, and burp) while
bubble formation on the submerged portion of the coil was observed and recorded. Particular focus was
placed on the nickel electrode surface. The current waveforms were controlled and generated by an
arbitrary waveform generator. Table 1 describes the waveforms compared. The one second period was
extended to 5 seconds to allow more time between pulses to assess a possible cause and effect relationship
between the current step change and oxygen bubble formation/dislodgment.
Table 1. Description of waveforms compared during video-microscopic experiments.
Galvanostatic Constant current of 2A
2A interrupted with a 25 ms rest
2A interrupted with a 125 ms rest
2A interrupted with -5A, 5 ms pulses followed by a
20 ms rest
2A interrupted with -5A, 25 ms pulses followed by a
100 ms rest
A beeper was connected to a voltage comparator to sound an audible beep during each occurrence
of a reverse pulse or relaxation period in the current waveform. This sound was recorded by a microphone
onto the VCR tape to allow one to determine if a correlation exists between bubble formation (or
dislodgment) and current pulse or relaxation. Only qualitative observations were made with this test
More detailed descriptions of the test articles, test set-up, equipment used, and test conditions of
the video-microscopy experiments are in Appendix D.
Manometry was used to quantitatively measure cell gassing rates and quantities as a result of
various charge methods. Pressure variations during cell cycling were measured and recorded with a water
filled manometer. A small hole was drilled in the center of the bottom of the can of a commercial cell from
Sanyo which had been charged and discharged 10 times. The cell was placed in a 50 ml graduated cylinder
and sealed with a rubber stopper. Tubing connected the cylinder to the input end of the manometer. Cell
electrical leads were fed through the rubber stopper to enable cycling the cell. The same electrical set-up
used in the video-microscope experiment was used for this experiment.
The U-tube of the manometer was filled with distilled water. A vertical displacement of up to 20
cm of water could be accommodated and changes could be measured to within ? 0.025 cm. A rate of gas
evolution was calculated by measuring water displacement as fast as every 30 seconds. The manometer was
calibrated by introducing a known quantity of nitrogen gas with a syringe into the rubber stopper of the cell.
One ml of gas produced a 4.1 cm displacement of water or conversely, 1 cm displacement results from a
0.244 ml of gas generation.
The cell was charged and discharge twice with each of three charge waveforms; galvanostatic,
burp, and pause. The comparison was performed on 3 consecutive days. The first cycle was performed to
stabilize the cell. The second cycle was performed immediately after the 1st and is deemed more valid for
comparison. To equalize the charge input rates of each method, the galvanostatic portion of each charge
sequence was set at slightly different levels. For example, to match the charge rate input of the burp charge
at 2A, the galvanostatic and pause charge rate were set at 1.915A and 1.974A, respectively. At these rates,
each charge technique achieved the same net charge input per period. In each case, the cell was discharged
to 1.000V using a 0.5 ohm resistor and the charge was terminated when cell voltage reached 1.550V.
A second set of comparison tests was conducted to exaggerate possible differences between charge
methods. In this case, all three conditions began charging galvanostatically for the first 55 minutes of
charge. Thereafter, every minute included a 6 second OCV rest for the exaggerated pause waveform while
the exaggerate burp waveform coupled a 1 second 5A discharge pulse with a 5 second OCV rest every
minute. The charge current levels for the three waveforms were as follows: galvanostatic (1.915A), pause
(1.965A) and burp (1.985A).
A third set of comparison tests was conducted with the cell flooded in 6.4M KOH solution. The
objective was to minimize solid-gas recombination reactions 4 and 6 to better measure the electrochemical
gasing products from reactions 2 and 5. As in the two previous manometric tests described, the cell coil was
not disturbed, only a small venting hole was drilled into each end of the cell casing. The cell was flooded
with electrolyte for over a week before cycling to ensured complete electrolyte immersion of the cell coil.
More details on the test article configurations are in Appendix E.
CHAPTER 3: RESULTS AND DISCUSSIONS
3.1 Performance Cycling
Repeated galvanostatic charging NiMH cells to a end temperature of 45°C can hurt cycle life very
significantly as shown in Figure 2. Here, a 2.4 Ah cell was charged at C-rate until a set temperature at the
cell skin is achieved. After 200 cycles, the C-rate discharge capacity performance of the cell severely
degrades. Note that maximum discharge capacity output during the first 200 cycles is about 97%.
% of Nameplate Capacity
C-rate discharge output
of Sanyo 4/3AU NiMH cell.
C-rate galvanostatic charge
until cell temperature
reaches 45 deg C.
End of Charge Temperature, deg C
Fig. 2. Simple galvanostatic charging effects on cycle life.
Using the same galvanostatic waveform with a more sophisticated termination algorithm yields a very
different result. The charge was terminated when a negative voltage slope or a certain rise in cell
temperature were detected. The results in Figure 3 show a more prolonged break-in period before achieving
maximum discharge capacity of 99% of nameplate capacity (2.4 Ah) within 250 cycles and remaining
steady to 400 cycles. The end of charge cell temperatures were kept between 30 and 35°C through most of
From these results, one can conclude that the "smart" termination algorithms limited the amount of
overcharge heat generated every cycle. The cycle life improvement comes at a cost in the output during the
early cycles. The break-in period is prolonged.
When the C-rate burp charging waveform of Figure 1 is used, the C-rate discharge output is
improved without any detriment to cycle life as is shown in Figure 4. Discharge outputs of 102% were
achieved. In addition, the break-in number of cycles to reach outputs of 97% was reduced from 160 to 90
cycles. As with the "smart" galvanostatic method, cell temperatures at the end of charge as measured on the
cell skin were maintained below 35 °C. Therefore, the burp method produced a greater sustained discharge
output without increasing cell temperature or compromising cycle life.
Ah output with " smart " galvanostatic charge
% of Nameplate Capacity
Break-in period prolonged
End of Charge Temperature, deg C
Temperature at end of " smart "
Ah output with galvanostatic charge to 45 deg C
Fig. 3. Smart versus simple galvanostatic charging. Comparison of discharge output versus cycle life.
Ah output with Burp charging
End of burp charge temperature
% of Nameplate Capacity
Ah output with " smart " galvanostatic
End of charge temperature, deg C
Fig. 4. Burp charging versus smart galvanostatic charging. Comparison of discharge output versus
3.2 Cell Calorimetry
These cycling results from the previous section provoked questions as to why and how the
performance is improved by the burp current waveform versus the constant current waveform. Do the two
methods produce different charge efficiencies, charge overvoltage, and/or charge heat generation rates?
What effect does the short discharge pulse have relative to the effect of the following 24 ms rest? Which is
more important in improving discharge output and shortening break-in period?
Insights can be obtained from the calorimetric experiments of an individual cell charged
galvanostatically and per the waveform in Figure 1 without the discharge pulse. The latter waveform is
referred to herein as the pause waveform. From the Figure 5 results, one can see that the charge overvoltage
of the two methods overlay on each other except at the beginning and at the end of charge. A closer look at
the beginning shows that initially the voltage and heat rise are retarded with the pause waveform. Since the
charge portion of the pause waveform was kept at the same current level (2.3A), the Ah charge input per
period for the pause waveform versus the galvanostatic waveform is 3% lower. However, the charge heat is
reduced throughout the bulk of the charge by more than 3%, except at the end of charge. Therefore, the
reduced charge heat generation by virtue of the pause method can not be attributed solely to its 3% lower
charge input per period.
Heat and voltage profiles
from galvanostatic vs
pulse charging of Sanyo
4/3AU cell. Cycle 425
at C-rate at 23 deg C.
Fig. 5. Calorimetric comparison of galvanostatic and pause charging. Charge heat and voltage
comparison versus time.
The peak voltage and heat levels are similar, but the pause peaks occur about a 1 minute later.
Most significantly, the charge heat rate in W is reduced throughout the charge with the pause waveform.
The area under the heat curve, in J, is about 8% lower than with the galvanostatic waveform. This is
unexpected because the charge overvoltages were so similar, and the temperature rise (Tfinal - Tinitial) in the
cells during charge remained unchanged.
Adding the 5 ms discharge pulse, to obtain the burp waveform, reduces the charge input per period
another 1.25% further. It reduces the heat generation rate and the charge overvoltage as shown in Figure 6.
Lowering the cell heat generation allowed a greater charge input (in Ah) prior to termination by the same
algorithms as the pause technique. Specifically, a 5% greater charge input was allowed, resulting in a 5%
greater discharge output during calorimetric cycling. The most noticeable reason for the greater charge
input is the delayed rise in charge overvoltage particularly near the end of charge. The charge heat rate is
6% lower than for the pause waveform at the midpoint of the charge. The temperature rise in the cell was
lowered by 1°C, despite the larger charge input in Ah. At the same relative states-of-charge, a difference of
nearly 50 millivolts occurred in the charge overvoltage near the end of charge. Therefore, the burp pulse is
responsible for lowering the charge overvoltage and heat allowing a greater charge input (resulting in
greater discharge output) than can be achieved by the pause method.
Sanyo 4/3AU cell
Fig. 6. Calorimetric comparison of the three charge waveforms. Charge heat and overvoltage versus
3.3 Destructive Physical Analysis
SEM and EDS revealed these differences between fully charged electrode samples and those
charged after 400 cycled times;
The average metal hydride grain size decreased noticeably with all cycling methods.
b) EDS revealed a mischmetal hydride surface composed of La, Ce, Nd, Pr, Ni, Co, Al, Mn, Zn, with
traces of Dy and Sm. More Mn was noticeable on the surface of the 400 cycled hydrides than the once
The once charged nickel electrode surface had a pasted appearance while all the cycled surfaces
appeared much more fibrous.
d) In all the above analyses, differences between the cycling methods were not discernable.
The results of surface area and pore volume analysis of the positive electrodes are shown in Table
2. Surface area decreases and pore volume slightly increases with cycling when comparing the once-charged
electrodes to ones cycled 400 times at 100% DOD. Within a 80% confidence interval on the average of the
measurements, the burp method does not stand out significantly better than the galvanostatic method to
prevent loss of pore volume with cycling. In contrast, the BET surface area difference between the
galvanostatic and either the burp or pause method is significant. The transient (burp and pause) methods
cause a loss in electrode surface area which indicates that the particle, crystal, or grain size has increased
with these methods. This data on cells cycled at 100% DOD is contrary to the hypothesis that burp charging
prevents formation of large crystals which reduce surface area. It has been reported that cycling NiMH and
NiCd cells with repeated partial discharges, followed by moderate overcharge causes a voltage depression
sometimes referred to as a memory effect . The cause of this effect has been linked to a phase
conversion of the nickel charged active material from ?-NiOOH to ?-NiOOH with a concomitant increase in
particle size . In cell cycling studies specifically aimed at examining this phenomena, the burp
waveform and its termination algorithm were found to mitigate this voltage depression effect .
Therefore, since the work herein did not examine this effect, no validation or contradiction is offered.
Finally, the pore volumes of the control, burp, and galvanostatic electrodes are all within the 80%
confidence interval. Only the pore volume increase of the pause method stands out as significant. No
explanation is offered for this at this time.
Table 2. Nickel electrode surface area and pore volume comparison
Control (charged once)
BET surface area, m2/g
Pore volume with dia & lt; 200 nm,
The results of particle size distribution of the hydride electrode samples are shown in Table 3.
Median and mean are given with a standard deviation along with the range of minimum and maximum
particle size. These wide distributions have standard deviations too large to make any conclusions other
than the once-cycled hydride has slightly larger grain sizes than all the hydrides cycled 400 times.
Table 3. Metal hydride particle size distribution comparison
Control (1 charge) 42
Standard dev. (um)
2.0 - 229
2.6 - 229
2.6 - 175
2.3 - 200
Therefore, all these data, obtained on sealed NiMH cells cycled at 100% Depth-of-Discharge
(DOD) do not support an electrode morphology mechanism as proposed in hypothesis #1 to explain the
burp charge phenomena as found with vented NiCd cells . This suggests that sealing the cell may have a
prominent role. Cell pressure effects will be investigated in later sections.
Could double-layer capacitance effects be responsible for the differences in overvoltage observed
between the charge methods? A closer look at the transient voltage response during the current interruption
of the pause with an oscilloscope reveals a 0.16 V drop per cell requiring 20 us to fully develop as a result
of interrupting a 2 A charge. Therefore, the capacitance effect of the double-layer decays at a much faster
rate than the duration of the pause or burp event of these transient charge methods. These results are
consistent with previous findings for porous electrodes . This means the period of the burp and pause
methods would have be shorten to ~20 us to potentially benefit from the double-layer capacitance effect.
Thus, double-layer capacitance is not found to be the direct mechanism for the overvoltage effects
observed as in hypothesis #3. However, can the effect facilitate gas diffusion? Since the double layer is very
thin (~ 1x10-9 m) and adjacent to the electrode surface, its agitation impact on gas bubbles is restricted to
that thin surface region and can possibly impact the bubble's surface tension. Since this region is smaller
than the average pore size (~30x10-9 m) of the nickel electrode and much smaller than the average particle
size (~35x10-6 m) of the metal hydride electrode through which the gas bubbles must diffuse, and the effect
decays so quickly, it is not regarded as a prominent factor.
Video observations at 70X magnification were focused on a portion of the current collector of the
nickel electrode which was submerged in electrolyte because that is where the oxygen bubbles are
generated. During charge, these revealed a very significant amount of bubble generation whose rate
increased with state of charge. During the first 30 minutes of charging at 2 A, very little bubbling activity is
noticeable. Thereafter, the bubbling becomes more pervasive. After 45 minutes, some larger bubbles are
noticeable as they rise much faster to the surface of the electrolyte level which was set at one quarter up the
cell coil. Once 55 minutes into the charge, the largest bubbles appeared and flaking of electrode material
was observed. These were accompanied with a steady stream of the small bubbles.
No cause and effect relationship between the occurrence of a pause or burp in current and the
release of bubbles could be established. The flow of bubbles is too steady and pervasive throughout the
observed electrode. Even when the period of the pause and burp waveform was expanded by a factor of
five, no qualitative differences could be discerned with the 5 second period. No video-microscopic evidence
was found supporting hypothesis #2 that reverse pulse of burp charging dislodges oxygen bubbles masking
the positive nickel electrode surface.
Even after the charging was terminated, the flow of bubbles continued steadily, albeit without
increasing. It takes over 1 minute after termination of charge to notice a decrease in bubble flow. Even after
resting for one hour, a very small flow of very small bubbles is still observable. However, within one minute
of starting a C-rate discharge, one can visually detect that the flow of bubbles has slowed even at the high
magnification levels. The response delay to current changes can be attributed to the tortuous bubble path
present in these porous electrodes.
Clearly from these observations, the gas evolution reactions play a significant role during charge.
The role apparently increases non-linearly with increasing state-of-charge. Furthermore, the onset of
discharge also produces a gas consuming effect which is visually detectable. This provides an insight that
gas consumption may be also occurring during the burp pulse during charge. An alternative experimental
method is required to quantify the gas evolution amount and rate with the various charge methods.
In the manometric set-up, the cell was least disturbed from its commercial configuration. The
electrode coil was still under its designed compression level inside its cell can and with its original
electrolyte quantity and composition. The only cell level changes versus the calorimetric experiments were
that its pressure at 0% state-of-charge was zeroed to ambient pressure before beginning the nearly C-rate
charge and that gases generated had a bigger volume to expand into, which maintained cell pressures at
lower levels. Therefore, the chemical and electrochemical equilibriums were not the same.
From Fig. 7, one can see that the gas evolution curves show an exponential increase near the end of
charge as was qualitatively discerned from the video-microscopy observations. The shape of the
galvanostatic gas curve is similar to that recently determined by others experimentally [11, 32] and
predicted theoretically . At this current rate, significant gas evolution occurs with all methods well
before reaching full charge and the majority of constituent is hydrogen, not oxygen [11, 32]. Therefore, the
effects the various waveforms have on the hydride electrode and its reactions can not be dismissed
compared to the effects on the nickel electrode in contributing to the cell pressure.
The galvanostatic charge method resulted in significantly more gas generation near the end of
charge than either the burp or pause method. Fifty minutes into the charge, the gas generation rate of the
galvanostatic method diverts from the other two methods. At the time the galvanostatic method had reached
the cut-off voltage of 1.550V (73.5 minutes into the C/1.2 charge), the galvanostatic method had generated
twice the gas volume as the other two methods while receiving equivalent charge inputs in
galvano gas level
burp gas level
pause gas level
Cell Voltage, V
Fig. 7. Comparison of the charge overvoltage and gas generation of three charge methods (burp,
pause, and galvano) versus runtime with the same nickel metal hydride cell. Initiation of 2nd
charge/discharge cycle for each method was at a runtime of 0 minutes. Gas generation volume
indicated by centimeters of water displaced in a manometer. Current levels; Burp at 2.000A, Pause at
1.974A, Galvano at 1.915A.
ampere hours. In contrast, very little difference exists between the pause and burp gas curves. One can infer
from this result, that interrupting the galvanostatic charge is more important than also including a discharge
The charge overvoltage values from the curves are quantitatively about 10 mV higher at
comparable states of charge to the values from curves shown in Figs 5 and 6. An ohmic losses error analysis
of the calorimetric and manometric test cells determined that, for both cases, of the overvoltage difference is
strickly due to a combination of not being able to run at the same test current (2.0A vs. 2.3A) and not being
able to place voltage sense leads directly on the cell terminals. Details of this analysis are in Appendix E.
Nevertheless, the charge overvoltage curve of the galvanostatic method also followed a similar pattern
relative to the overvoltage of the other methods. From the onset of the charge, the galvanostatic overvoltage
curve is higher than the other two. This causes the galvanostatic charge to reach the cut-off voltage about
1.75 minutes sooner than the other two techniques. This was also observed upon analysis of the results of
the performance and calorimetric cycling experiments. Thus, interrupting the galvanostatic waveform with
rest or with rest and burps, lowers the charge overvoltage.
However, it is surprising to not see any significant overvoltage or gas evolution differences
between the burp and pause methods in Figure 7. The differences in the charge overvoltage curves between
burp and pause in Figure 6 were not replicated in Figure 7. A main difference between the manometric and
the calorimetric cells is that the operating pressure of the cell was much lower for the manometric test
because a hole had been drilled into it to connect it to the manometer. The inert volume of the manometric
cell is estimated at over 100 times that inside the undisturbed cell used during the calorimetric test.
Therefore, the partial pressure of hydrogen and oxygen is correspondingly less for the manometric cell.
Why the reduced partial pressure mitigates the charge voltage and gas evolution differences between the
burp and pause waveforms is unknown.
A smaller difference is the charge current level. The calorimetric tests used the same 2.3A charge
current for each method. Burp charging at 2.30A is equivalent to pause charging at 2.27A at an equivalent
charge input per period. However, this small current change can only account for less than 1 mV of
difference based on a 22 mohm cell internal resistance estimated from voltage fluctuations during step
changes in current  in a method similar to that used previously . In contrast, the burp and pause
waveforms diverged by 10 mV at the mid-charge point in Figure 6. Therefore, the slight variation in charge
current level do not invalidate the results.
The goal of the exaggerated waveform test was to determine if lengthening the period of the
waveforms would produce a more discernible difference in the overcharge and gas evolution results. The
waveforms were all galvanostatic until 55 minutes into the charge. Up to that point, the overvoltages of all
three curves varied by no more that 4 millivolts and manometer levels were within 0.3 cm of each other.
Thereafter, the overvoltage curves separated slightly while the gas curves diverged more significantly. In
Fig. 8, the overvoltage data of the transient methods are displayed without smoothing the data for clarity
with a moving average box car algorithm as is done in all other figures. Note that with data recorded
roughly every 2 seconds, voltages at different stages of the waveforms are recorded yielding what maybe
misinterpreted as measurement noise.
At the end of charge, the order of decreasing overvoltage was galvanostatic, pause, and burp as
was found in the calorimetric cycling. Similarly, after 65 minutes into the charge, the order of decreasing
rate of gas evolution was galvanostatic & gt; pause & gt; burp. This experiment helped distinguish the advantage of
the burp over the pause method.
In this test, the burp overvoltage took the longest to get to the cut-off voltage of 1.550V. The onset
of the exaggerated pause causes a temporary reduction in overvoltage relative to the galvanostatic method.
However, this effect is not long lasting as the two methods reach the cut-off voltage at the same time.
Nevertheless, the pause method does retard gas generation relative to the galvanostatic method. The pause
method temporarily reduces the overvoltage while the full second discharge pulses of the exaggerated burp
method produced a more lasting overvoltage reduction. The burp method is best at retarding gas generation.
Figs. 7 and 8 demonstrate a correlation between higher overvoltage and higher gas generation.
The pause waveforms of Figs. 7 and 8 are nearly identical. This indicates that a five fold extension
the relaxation time step (from 30 to 150 milliseconds) does not lower the gas generation rate. Therefore,
lengthening the pause time does not produce any benefit. In contrast, a comparison of the burp waveforms,
indicates that lengthening the discharge pulse of the burp method from 5 to 25 milliseconds does reduce or
retard the gas generation rate.
Furthermore, saving the pause and burp steps towards the end of the charge as in Fig. 8 appears to
be just as effective as having them throughout the charge process as in Fig. 7. This suggests that an
improved charge could be attained by making the frequency and the length of the burp and relaxation steps
increase as a function of increasing state-of-charge. Additionally, this is more evidence that a gas related
phenomena is more likely responsible than a changing electrode morphology phenomena as proposed in
hypothesis #1. It is difficult to understand how a morphological phenomena could have a similar variation
Fig. 8. Comparison of the end of charge with exaggerated pause and burp waveforms versus runtime
with the same nickel metal hydride cell. Initiation of the charge was at a runtime of 0 minutes.
Figure 9 shows a typical gas curve during the very end of charge and throughout charge rest and
discharge. Thirty seconds after the end of charge, gas evolution peaks and non-linearly decreases thereafter.
The decrease during the charge rest is due to the chemical reactions of oxygen and hydrogen gas
+ 2H2 ?
oxygen recombining with surface hydride (reaction 4), and hydrogen hydriding at the negative electrode via,
2M + H2 ?
Note that at the onset of discharge, the rate of gas consumption (slope of the gas curve) becomes noticeably
more negative indicating an increase in gas consumption. This was also observed during the video-
microscopic experiment. Flow of small gas bubbles from the nickel electrode nearly disappear after the
onset of discharge.
45 minute rest period
Cell voltage, V
slope change at
onset of discharge
Discharge runtime, minutes
Fig. 9. Voltage and gas evolution curves versus runtime during a charge rest period followed by cell
discharge into a 0.5 ohm load.
These observations support the mechanism that during the discharge pulse of the burp waveform,
oxygen bubbles are not dislodged but rather consumed at the positive electrode surface. During this burp
pulse, two competing electrochemical options exists; one is the reverse of the half-reaction 1, the other, the
reverse of half-reaction 2. Envisioning a charged pore surface of the positive electrode with a masking
oxygen bubble, which of these two mechanisms will the bubble prefer? One can rationalize that the gas
bubble will impede water transport to the NiOOH surface (impeding the reverse of reaction 1) and cause the
water to prefer reacting with the masking oxygen bubble (reverse of reaction 2).
At the hydride surface, during the burp pulse, the choices are the reverse of reactions 3 or 5. As
was reported previously [10, 11, 14], the reverse of reaction 3 involves diffusion of adsorbed atomic
hydrogen from the bulk of the hydride metal structure. This is slower than the reverse of reaction 5 which is
a surface reaction. Therefore, a high rate pulse of discharge current (burp) should favor reversing reaction 5
over reversing reaction 3 on the metal hydride surface, which lowers cell pressure by consuming gas. Thus,
evidence suggests that gas bubble consumption occurs electrochemically at both electrodes during the rapid
discharge pulse of the burp charge method.
The chemical recombination mechanism of reaction 9 requires the transport of the oxygen from the
positive to the negative and is very exothermic (-136 kcal/mole of O2) . If it is prominent, it
significantly raises the operating temperature of the cell. Raising the temperature of the metal hydride drives
more hydrogen out to recombine with electrochemically evolved oxygen. Via this chemical process, the
temperature of a fully charged or overcharged cell could continue warming even while it rests on open
circuit after charging has stopped. This has been observed while leak testing a competing commercial cell
design after placing large groups of closely packed cells in a 50 °C oven immediately after charging the cell
at C/10 for 16 hours. Such cells are typically at 32-40 °C as a result of the overcharge. Once open-circuited
and placed in the oven, they were found to overshoot the oven set-point . These observations provide
some supporting evidence for occurrence of this chemical recombination mechanism at higher temperatures.
Using the following assumptions derived from my calorimetric data, DPA data, and an
extrapolation from literature data : 4 atm partial pressure of oxygen after the C/10 charging, 2 cc of
void volume in the cell, 0.20 cal/g-°C, 52 g/cell, 40 °C cell temperature, and the ideal gas law, a cell
adiabatic temperature rise of 4 °C is predicted as a result of gaseous recombination. Higher temperatures
drive more hydrogen out of the hydride and will cause oxygen bubbles trapped in the positive electrode
(leftover from the slow overcharge) to expand, which favors their escape. In turn, more reactants will
increase the rate of recombination making possible a vicious cycle when closely packed cells can not reject
In the absence of discharge pulses ("burp") during the charge, cell pressure is maintained by the
chemical recombination processes (reactions 4 and 9) and rehydriding of hydrogen gas at the negative
electrode (reaction 10). Adding discharge pulses, adds additional electrochemical mechanisms to consume
the oxygen and hydrogen evolved via the reverse of reactions 2 and 5. Removing bubbles from an electrode
surface increases its effective area and reduces its local current density. As a result, the overvoltage is
slightly reduced which allows a slightly greater charge runtime. In turn, a lower charge overvoltage results
in lower cell heat generation which in a virtuous cycle will reduce oxygen and hydrogen evolution.
In the flooded cell experiment, both electrodes are immersed in liquid electrolyte. The purpose of
this experiment was to gain insight on the relative importance of the chemical gas recombination path
versus the electrochemical gas consumption path. Since the chemical path requires oxygen transport from
the positive to the negative electrode, flooding should make that transport less facile and cause a greater
accumulation of gas bubbles near the electrode surfaces.
With the flooded charge process, the lack of solid-gas interfaces impedes the solid-gas reactions
(4, 9, and 10) all of which consume gas. As a result after 40 minutes of charging, gas generation rates and
amounts are higher as shown in Fig. 10, which compares the nominal (or electrolyte starved) cell data from
Fig. 7 to that of a flooded cell during galvanostatic charging. Several features of the flooded cell gas curve
are noteworthy. The measured gas level actually decreases very slightly during the early stages of charge
and then rapidly begin to rise at a lower state of charge (~ 50% vs 80% SOC calculated on a 2.4 Ah
coulombic basis) than for the starved cell. Note that at the beginning of charge, the charge overvoltage of
the flooded cell is significantly lower than the starved cell. This is attributed to the increased ionic
conductivity resulting from a completely wetted path between electrodes. The increased slope of the charge
overvoltage of the flooded versus the starved cell may reflect the loss of that increased conductivity by the
emerging transport difficulties associated with the accumulation of surface gases. Coincidentally, once the
charge overvoltage of the flooded cell surpasses that of the starved cell (after 30 minutes or at 42% SOC),
its gas generation rate rises dramatically. These results confirm the prominent role that the availability of
exposed solid electrode surface has on cell pressure by promoting solid-gas interface reactions which
The charge of the flooded cell was terminated after 52 minutes of charge to prevent gas levels from
exceeding the measurement capacity of the manometer after charge is terminated. Note how rounded the gas
curve is after charge is terminated. Peak gas generation lags 20 minutes behind and the gas level increases
by 2.5 cm (versus a 30 second lag and an increase of only 1 cm for the starved cell) after charge is
terminated. In comparison, once charge is terminated on a starved cell, gas levels lower quickly. This
difference reflects the slow nature of gas transport from the pores of the immersed electrodes.
Further evidence of the slowed chemical recombination processes is how much slower gases are
consumed during the charge rest and discharge periods. Additionally, as with the starved cell, the onset of
discharge slightly accelerates gas consumption. This is more evidence that gases are consumed during the
discharge pulse of the burp waveform.
Cell Voltage, V
Flooded gas level
Fig. 10. Comparison of voltage and gas levels in a flooded and nominal cell during galvanostatic
charge at 1.915A, rest, and resistive discharge at 0.5 ohm.
The flooded cell experiment also permitted measuring a net cell coil expansion of 0.38 cm3 which
occurs during charge and is manifested by a rise in the immersing KOH level. A net expansion occurs
because the expansion of the metal hydride is greater than the contraction of the nickel electrode (where the
uncharged species is less dense than charged species [4, 38]). This expansion leaves more room for gas
storage and maybe the reason the gas level on the manometer initially decreases after the onset of charge.
This effect is small and is soon overwhelmed by the gas generation rate.
Figure 11 shows the voltage and gas levels of all three charge methods applied to the flooded cell.
In comparing the gas levels after 50 minutes, the order of increasing gas generation is burp & lt; galvanostatic
& lt; pause (4.80 cm & lt; 6.65 cm & lt; 7.30 cm). The difference between the burp and galvanostatic method, 1.85
cm is much less than the factor of two difference seen for the starved cell before its end of charge point (see
Fig. 7). Furthermore, the voltage traces are not discernibly different with each method. Unfortunately, the
flooded cell charging process had to be terminated sooner, possibly before differences may have developed.
Nevertheless, the burp method produced the lowest gas curve. A repeat of this test produced very
reproducible results. The advantage that pause charging had over galvanostatic charging with the starved
cell is not manifested in the gas curves the flooded cell of Fig. 11. This indicates that pause method needs
exposed electrode surfaces and facile gas transport to manage cell gas generation better than the
galvanostatic method. The short relaxation step of the pause method is not enough to allow diffusion of
oxygen bubbles away from the nickel electrode surfaces. Therefore, flooding the cell served to elucidate
differences between these dynamic charge methods by slowing gas transport, limiting solid-gas interfaces,
and impeding its reactions.
Once the gas consuming chemical reactions are suppressed by the transport limitations of oxygen
in the flooded condition, the electrochemical gas consumption surface discharge reactions (reverse of
reactions 2 and 5) produce an accumulative effect significant enough to quantitatively measure
manometrically. This is more evidence supporting a gas consumption mechanism during the discharge pulse
rather than a dislodgment mechanism. If the discharge pulse of the burp method was dislodging gas from
the electrode surfaces as in hypothesis #2, the diffusion limitations of the gas in the flooded environment
would cause an accumulation of gas near the electrode surface, further impede ionic flow, and raise
overvoltage. This was not observed during charge in the video-microscopic or manometric experiments.
Cell Voltage, V
Fig. 11. Cell gas and voltage level during charging of a flooded NiMH cell. Comparison of
galvanostatic, pause, and burp charge methods.
What cell and charger design improvements does the results of this work suggest?
As far as the cell is concerned, electrolyte quantity is critical. Too little results in higher ionic
impedance. Too much impedes the cells gas management processes. Maintaining a sufficient amount of
exposed hydride to support the gas management processes is critical. Reducing the gas transport path by
reducing the electrode and/or separator thickness and increasing their area would improve the gas
management process. The higher surface area cell could then support higher current rates without a
concomitant cell pressure increase. Furthermore, this work indicates that the gas consuming hydride
electrode plays an important role in influencing cell pressure and charge overvoltage by virtue that it
contains most of the solid-gas interfaces. One should find ways to improve the surface rehydriding kinetics
of the hydride to maintain lower hydrogen partial pressures. Additionally, if the inner surface of the can
could be coated with a recombination catalyst as exists in aerospace Ni/H2 cells , cell pressures could be
As far as charger design suggestions, this works indicates that a benefit could be gained from
increasing the frequency of the discharge pulses with increasing state of charge. The results of the starved
cell with nominal and exaggerated waveforms (Figs. 7 and 8) indicate that not much is gained from the burp
pulses during the first half of the charge process and some benefit can be obtained from introducing them as
late as after 76% SOC, when they are more beneficial. Similarly, it may be beneficial to increase the
duration of the discharge pulse with increasing state of charge. Lastly, the exaggerated waveform
experiment indicates that lengthening the duration discharge pulse is beneficial while that of the pause step
CHAPTER 4: SUMMARY AND CONCLUSIONS
In summary, the cycling performance tests on commercial sealed NiMH cells demonstrated that
burp (reverse pulse) charging improves cycling capacity without degrading cycle life over pause and
galvanostatic methods. In-situ calorimetric tests concluded that burp charging lowers charge overvoltage
and heat generation when compared to the other methods. Destructive physical analysis of both electrodes
by SEM and EDS revealed no significant differences in active materials cycled 400 times by either
techniques. Same conclusion on the particle size analysis of the metal hydride electrodes. Pore volume
analysis of the nickel electrode revealed that burp charging maintains pore volume only very slightly better
than galvanostatic charging.
In-situ video-microscopy qualitatively revealed the significance of gas-generating side reactions
during charge. Focusing on the positive nickel electrode, bubble generation was observed to have a nonlinear relationship with increasing state-of-charge. Even with a 70X magnification and an exaggerated pause
and burp waveform with a period extended by a factor of five, no cause and effect relationship between the
occurrence of a pause step or a burp pulse in current and the release of bubbles could be visually
established. However, after a 1 hour charge rest, a very small flow of bubbles are still observable on the
positive electrode surface. Within one minute of the onset of C-rate discharge, a reduction in the flow of
bubbles is visually detectable. This indicates that the onset of discharge consumes gas.
Manometric gas analysis of cells during cycling allowed for a quantitative comparison of the
amount and rate of gas generation or consumption with the various cycling methods. With a normal cell,
with little free electrolyte, the burp and pause charge methods generated significantly less gas than the
galvanostatic method. With the cell in a flooded state, all the methods produced more gas at earlier states of
charge because of less facile gas transport and the lack of exposed hydride to catalyze gas consumption
reactions. In flooded cells, pause charging loses its advantage over the galvanostatic method. In the flooded
condition, burp charging stands alone with lowest gas generation rate. Gas recombination paths that were
facilitated by the pause method in the starved cell are impeded by the slow transport of gases to the hydride
electrode in the flooded condition. Burp charging is the only one of the three methods capable of consuming
electrode surface gas by reversing the gas generation electrochemical reactions during the discharge "burp"
pulse. Hence, the "burp" label implying a dislodgment of gas is a misnomer and the method is more
accurately labeled as "reverse pulse" charging.
As a result of this work, specific cell and charger design recommendations were made. A particular
important cell design suggestion, is to maximize the amount of exposed solid surfaces that are catalytic to
oxygen and hydrogen recombination. An important charger suggestion would be to increase the frequency
and duration of the discharge pulses during charge as a function of increasing state-of-charge.
Conclusion 1: In sealed NiMH cells, it has been demonstrated that during charge undesirable gas
generating side reactions and heat increase with increasing charge overvoltage. Charge methods which
lower overvoltage maintain lower cell pressures and temperatures. Transient current charge methods such as
reverse pulse charging have this advantage over galvanostatic charging with NiMH cells.
Conclusion 2: The video-microscopic and manometric analysis of the cell gas generation and
consumption rates support that the reverse pulse or discharge pulse of "burp" charging causes a
consumption not a dislodgment of surface gas bubbles via a reversal of the electrochemical gas evolution
half-reactions at both electrodes.
F. Benjamin, SMPTE Journal, 86, 204 (1977).
F. Benjamin, The Reflex Principle of Charging Nickel-Cadmium and Other Batteries, Gardena:
Christie Electric Corp., 1972, pg. 3-11.
O.C. Wagner and D.D. Williams, Proc. of the 26th Power Sources Conf., Cherry Hill, NJ, (1974),
D. Linden, in Handbook of Batteries, McGraw-Hill, NY, 1995, section 6.2
G.S. Nagarajan and J.W. Van Zee, Journal of Power Sources, 70, 173 (1998).
Y. Sone, H. Kusawake, K. Koga, and S. Kuwajima, "Status of Nickel Metal Hydride Cell
Development", 1997 NASA Aerospace Battery Workshop, p. 161.
A.H. Zimmerman, in Hydrogen and Metal Hydride Batteries, P.D. Bennett and T. Sakai, Editors,
PV 94-27, p. 268, The Electrochemical Society Proceeding Series, Pennington, NJ (1994).
A.H. Zimmerman, Power Sources 12, T. Keily and B.W. Baxter eds., Taylor and Francis Ltd.,
Basingstoke, England, 1988, p. 235.
T. Fuller and J. Newman, Modern Aspects of Electrochemistry, Number 27, R. White, editor, p.
359, Plenum Press, NY, 1995.
C. Iwakura, M. Matsuoka, and T. Kohno, J. Electrochem. Soc., 141, 2306 (1994).
M. Ikoma, S. Yuasa, K. Yuasa, S. Kaida, I. Matsumoto, and C. Iwakura, Journal of Alloys and
Compounds, 267, 252 (1998).
Q.M. Yang, M. Ciureanu, D.H. Ryan, and J.O. Strom-Olsen, J. Electrochem. Soc., 141, 2108
Q.M. Yang, M. Ciureanu, D.H. Ryan, and J.O. Strom-Olsen, J. Electrochem. Soc., 141, 2113
P.H.L. Notten and P. Hokkeling, J. Electrochem. Soc., 138, 1877 (1991).
B. Kerridge, Electronic Design News, 13 May 1993, pg. 100.
C. B. Falcon, U.S. Pat. 5,600,226, (1997).
Z. Zhaoling and S. Dongsheng, ,J. of Alloys and Compounds, 270, L7 (1998).
T. Ikeya, K. Kumai, and T. Iwahori, J. Electrochem. Soc., 140, 3082 (1993).
T. Sakai, A. Uchiyama, H. Miyamura, N. Kuriyama, and H. Ishikawi, J. Electrochem. Soc., 140,
A. Zuttel, F. Meli, and L. Schlapbach, J. of Alloys and Compounds, 221, 207 (1995).
M. Viitanen, J. Electrochem. Soc., 140, 936 (1993).
F. Meli and L. Schlapbach, J. of Less Common Metals, 172-174, 1257 (1991).
A. Zuttel, F. Meli, and L. Schlapbach, J. of Alloys and Compounds, 200, 157 (1993).
J. Dukovic and C.W. Tobias, J. Electrochem. Soc., 134, 331 (1987).
F. Williamson, "Battery Management System - Optimized Electrokinetics Control in Galvanic,
Electrolytic, and Storage Operating Modes", 1997 NASA Aerospace Battery Workshop, p. 29.
M. Mankikar, Electronic Engineering Times, CMP Publications, Manhasset, NY, (25 July 1994).
QuickSaver(R) is a registered trademark of Galaxy Power, Inc., Valley Forge, PA.
K. Takeno, K. Ikeda, N. Shiojima, H. Hasebe, and Y. Sato, Abstract of 31st Battery Symposium,
Japan, p. 157 (1990).
Y. Sato, K. Ito, T. Arakawa, and K.Kobayakawa, J. Electrochem. Soc., 143, L225 (1996).
D. Whitmer, Galaxy Power, Inc., 1998, private communication.
C. Lagergren, G. Lindbergh, and D. Simonsson, J. Electrochem. Soc., 142, 787 (1995).
D. Kim, H. Lee, K. Jang, and J. Lee, J. Electrochem. Soc., 145, 3387 (1998).
W.B. Gu, C.Y. Wang, and B.Y. Liaw, J. Electrochem. Soc., 145, 3418 (1998).
B. Strangways, "28V CRV Cell Test, Performed for NASA-JSC", SRI report #78J, Jan 1998.
R. Pollard and J. Newman, J. Electrochem. Soc., 128, 491 (1981).
R. N. Smith and C. Pierce, "Solving General Chemistry Problems", WH Freeman and Co. CA,
1980, p. 227.
B. Strangways, Symmetry Resources, Inc., 1998, private communication.
Handbook of Chemistry and Physics, CRC, Cleveland, OH, (1966).
6.0 APPENDIX A
Design, Specifications, and Operation of the Performance Cycling Experiment
An Automated Battery Cycler capable of independently controlling the cycling of 10 batteries was
designed and assembled at the National Aeronautics and Space Administration's Johnson Space Center
(NASA-JSC), per my specifications. A photo of the rack mounted cycler and its adjacent battery chamber is
depicted in Figure A1. The cycler consist of 10 power supplies and 10 charger assembly racks. The cycler is
designed to test rechargeable batteries and automated commercial charging circuits. During the charge state,
the power supplies feed the chargers which charges the batteries. During the discharge state, the batteries
are discharged directly through those same power bipolar supplies. The current limits of each of the 10
battery stations are 20 V and 10 A and are dictated by the bipolar power supplies used. The brain of the
cycler is a Macintosh computer which talks to a power controller which switches batteries from state to state
(charge, discharge, and off) and a Kepco Talker/Listener Device (TLD) to control the power supplies. The
batteries are secured onto a holder which fits into a thermal chamber. Custom software routines were
generated in LabVIEW to acquire the data, control the cycler based on this data, and decide whether to
store the data. This appendix in details describes the design, specification, and operation of the cycler for
the benefit of this thesis and any further users of the cycler.
Data Acquisition Units
The cycler has two Fluke Hydra Data Acquisition Units, P/N 2620A, each with 20 data channel
scanning capability along with 8 digital output channels. Each unit is controlled via a RS-232 computer
link. The pair allows for the acquisition of battery voltage, current, and temperature for 10 batteries. No
external signal conditioning is necessary. Refer to the Hydra User Manual for more specifications. In the
current configuration, one Hydra (Port 0) scans voltages and currents and puts out a 7 digital bit signal for
relay switching to the Relay Controller. The other Hydra (Port 1) scans temperatures and puts out a single
digital bit signal to the Wathdog Timer in the Relay Controller.
The Relay Controller was designed and built at NASA-JSC to contain all the relay drivers. It is
located at the top of the rack. It uses the digital output signals from one Hydra and opens/closes charge and
discharge relays for each battery station. The seven digital bit signal uses bits 0 through 3 to specify the
station, bit 4 to specify charge or discharge, bit 5 to specify on or off, and bit 6 to enable and disable the
signal. Bit 7 is displayed on the front panel but not used. The digital bit signal can be manually controlled
from the front panel by flipping each bit in the manual position. The Relay Controller has individual light
emitting diode (LED) indicators to indicate which charge and discharge relays are open/close. The Relay
Controller also houses the Watchdog Timer which is a safety device to monitor the alertness of the
computer. The timer will open all relays if the computer does not send it a simple digital signal at least once
every 60 seconds. On the front panel, the timer can be turned on or bypassed. LED indicators show when
the timer is receiving its periodic signal from the computer and whether it has timed out or not.
Charger Assembly Racks
The Charger Assembly Racks as shown in Fig. A2 were design and built at NASA-JSC and each
contains a charger circuit board, charge and discharge relays, and a current shunt. These racks are designed
to be slipped into any of the 10 stations. The front panel allows one to manually set the relays to charge or
discharge and to set the charge rate to high or low. The LED indicators show what state the chargers are in.
Each rack has a fuse located it back panel for overcurrent protection.
Fig. A1. Automated 10 Station Battery Cycler with adjacent calorimeter. Power supplies are
adjacent to Charger Assembly Racks. Batteries are positioned in 3 layer holder placed on top of
GPIB Talker-Listener Device
The Kepco TLD 488 converts digital General Purpose Interface Bus (GPIB) signals from the
computer to analog signals for communication with the power supplies. The TLD does this via A/D cards,
TL-488-4B. Each can talk to four power supplies. The TLD contains three such cards. At the power supply
end, an interface card, -PCA X-3 processes the analog signal.
Each station has its dedicated Kepco BOP 20-10M power supply. This is a bipolar four quadrant
supply capable of constant current or constant voltage control to 20 volts and 10 Amps. A green indicator
light labeled " Remote " is on when the supply is under TLD control, otherwise it can be operated from its
front panel. Refer to the Kepco BOP 20-10M Manual for details.
A Macintosh IIci computer with 20 MBytes of Random Access Memory (RAM) and an 1 GByte
harddisk is used to run the software controlling the Stand. It is equipped with two internal cards. One from
National Instruments, NB-GPIB, for GPIB communications and the other from Applied Engineering,
Quadralink, which provides four additional RS-232 ports. For data transfer, an ethernet link is available on
the computer to link it to any other computer.
The controlling, data acquisition, and data logging software is written as virtual instruments (VI) in
LabVIEW(R) 2.2.1. The main VI is called " Battery Cycler. " It controls battery cycling and performs the
necessary data acquisition. The data recording is done by a VI called " Batt Hist. " It stores all the channels
of data into a binary format which is ideally suited from analysis using Igor. Battery Cycler and Batt Hist
operated concurrently. The watchdog timer is supplied with its necessary pulses by the VI " Watchdog "
which is a subVI to Battery Cycler.
All charge methods were set at the same current, 2.3A. The simple galvanostatic charge method
terminating when the battery reached 45°C, using a thermocouple placed on the battery, was achieved
without any commercial charger circuit. The "smart" galvanostatic charge method was achieved with the
Benchmarq bq2003 integrated circuit (IC) controller which terminated upon a seeing a negative voltage
slope or reaching a certain positive temperature slope. The "burp" method was achieved with the ICS1702
controller from Galaxy Power, Inc. This chip provided the reverse pulse charge waveform shown in Figure
1 and terminated after seeing a voltage infection. The reverse pulse or discharge "burp" was achieved when
with IC switched the battery to a resistor, sized to produce the desired discharge current. The "pause"
method was achieved with the same IC controller except that the discharge pulse resistor was removed from
the circuit. This resulted in a 29 ms OCV rest during every period of the waveform. One shortcoming with
all these controllers is that they provide no means of detecting which of the multiple termination algorithms
was responsible for terminating charge.
The Sanyo HR-4/3AU NiMH cell rated at 2400 mAh was used extensively for this work.
Previously comparisons of competing commercial cells shown that at the time this design yielded the best
C-rate capacity coupled with the most consistent cycling results. The batteries consisted of four cells in
series which were mounted on a 3 layer cylindrical holder. The edge plates of the holder provided a
conductive path to the walls of the cylindrical chamber of the calorimeter. These plates have many large
holes to allow the necessary wire paths and allow air circulation through each level. One thermocouple and
one thermistor were taped on each 4-cell battery.
The batteries are maintained in isothermal environment by resting the 3 layer holder in the
cylindrical chamber of the S77XX Heat Conduction Calorimeter, manufactured by Hart Scientific, Inc. The
cylindrical chamber was immersed in a controlled water bath. Above the calorimeter chamber, an air
circulation bath also help maintain at consistent thermal environment for the batteries during the cycling.
The water and air baths of the calorimeter were set at 23°C temperature of the experiment described herein.
Both baths have to capability to be set at any temperature between 0 and 80 °C.
The chargers assembly racks were mounted into their respective rack slots (see Fig. A2.) after
having its charging parameters set. Each is connected to by four quick-disconnects; one to a power supply,
one to a battery with thermistor, one to a Hydra for current measurement, and the last to the relay controller.
This allows one to easily remove and reinstall a charger for modifications. Whenever these charging trays
are removed from the rack, one should verify that its fuse is still operational and replace as necessary.
Fig. A2. Close-up of a charger assembly rack partially retreated from its slot to show its charger
controller IC on printer circuit board in front of small fan.
The batteries to be tested are secured into a designated slot on the three tier holder. Then, the
appropriate power leads are soldered to each battery tab. Sense leads and thermistors must be tied directly
to each battery. Leaving the air bath of the calorimeter, the thermistor leads and power leads are bundled
together. Similarly, the sense leads and the thermocouple leads are bundled together leading to a break-out
board behind the calorimeter. Once the voltage sense leads and thermocouple leads are connected, data
connections can be verified on the front panel of the Hydras. The Hydra on port 0 should be configured for
channels 1 through 10 to read voltages. Channels 11 through 20 should be configured with a multiplicative
factor of 100 to read currents in amperes. Channels 1 through 10 on the Hydra on port 1 should be
configured for T type thermocouples. Once this was done, no further signal conditioning was needed.
Starting the battery cycling process should begin first by opening the data logging VI called " Batt
Hist " . Before executing it, a number of parameters must be set or verified on its front panel. Number of
channels should be set to 40 to record ten state times, voltages, currents, and temperatures. Samples per
channel set the length of each logging file. The first such file is labeled by the user and automatically
suffixed with a " 00 " . When the sample per channel limit is reach by any channel, subsequent data is logged
into a new file with the suffix " 01 " and so on. A 3000 samples per channel setting will result in roughly a 1
MByte datafile. The " Save Every " parameter determines how often data is evaluated for storage. Fifteen is
the fastest setting.
In the " Chan # " cluster array several parameters are set for each channel. The " Deadband " and
" Fencepost " features tell HIST to log a channel value whenever that value is not within the deadband of the
previous value or whenever the fencepost time has elapsed. Also in the cluster, each channel must be titled
and given units. Refer to the HIST manual for more details.
The " Plot " option displays a real time plot of a selected channel from the beginning of the current
file contents. This particular region of this plot can be expanded by defining appropriate beginning and end
times. Turning off this plotting options relieves the computer to handle other tasks more efficiently.
Executing VI Batt Hist.
First, turn on each battery station which you want cycled. Select a discharge current in Amps
(positive) and the number of cycles desired for each battery. The state of and the number of cycles
completed by each battery are displayed. Next, set up the Battery Cycler VI by setting the parameters in
Cluster titled " Key parameters of Battery Station " . The duration of trickle charge and the rest periods after
discharge and trickle charge are user selectable for each battery station. The Discharge phase of a battery is
terminated when its voltage dips below the user selected " discharge cut-off voltage " . The Charge phase is
nominally terminated by the charger's internal logic circuitry. However, if a battery voltage or temperature
exceeds the user selected " charge voltage limit " or battery temperature limit, Battery Cycler will terminate
the charge and switch on to Trickle Charge. The onset of the Trickle Charge phase of a battery is initiated
once the battery current is detected to be lower than the user selected " trickle current threshold " .
If one prefers to trickle charge at a selected constant rate rather than the rate set by the charger,
then, setting the " Trickle w/ Kepco " switch to " yes " and setting the corresponding current in the " trickle
charge current " array will do just that. If some of the charging assemblies require constant current input
rather than constant voltage, these must be identified in the " charge input " switch. Constant current is
denoted " CC " while constant voltage, the default setting, is " CV " .
If one prefers to bypass the chargers in the tray and use the Kepco power supply directly, then,
setting the charge time to zero will skip through the charge phase and go to trickle charge. Kepco trickle
charge can be set to any current up to 20 A. The same voltage and temperature limits exist for this " trickle "
phase as with the normal charge phase. One should be careful in properly defining the time limit for this
" trickle charge " phase.
Finally, one can decide whether to set-up filenames for cycle logging station highlights and for a
restart folder. A dialog box will prompt you for these filenames. " No " to the " set-up files? " will cause the
previous files to be used. The filenames and any error messages are displayed on the front panel.
Upon executing Battery Cycler, the connected batteries will be cycled. The state of charge of each can be
seen on the front panel of Battery Cycler. All the batteries will start in the Charge Rest state and show a " -1 "
cycle count which is zeroed once Discharge begins. The data of each can be seen on the front panel of
When a battery station is turned off either by the user or by the Battery Cycler VI, it can be
restarted in two simple steps. First, turn on the particular station control of the Battery Cycler. Then,
execute the Station Restart VI after having selected the appropriate restarting conditions of that VI. It is
suggested to rename the cyclelog file if a new battery is substituted in the battery station.
The detailed data from the stand is stored by Batt Hist in binary files and the cycle highlights of
each battery station is stored by Battery Cycler in individual text files. The binary files come in pairs
suffixed " .data " and " .ptrs " which can readily be loaded by Igor, a graphical data analysis software. Igor
uses an XOP macro called " LoadHIST Channel " to do this. Refer to the Igor User Manual for more details
and instructions. The final values of state time, voltage, current, and temperature of each battery state
(discharge, discharge rest, charge, trickle charge, and charge rest) is recorded along with its cycle number
and charge termination reason into a cyclelog file for each battery station. The user is prompted to name
that file upon execution of Battery Cycler. The values for each cycle are continually appended to the
cyclelog file along with a time and date stamp as they occur.
Battery Cycler VI Operation
The Battery Cycler VI is composed of a two step sequence consisting of initializing instruments
and files followed by a While Loop containing the main activities of Battery Cycler. This While Loop is
perform until all battery stations are turned off either by the user or by the program. The While Loop has a
three step sequence which consists of (1) triggering a scan of all data channels and updating global variables
and displays, (2) performing the main For Loop that evaluates what to do with the data, and (3) displaying
key parameters and triggering the watchdog timer.
The main For Loop steps through each battery station and extract that channel's time stamp,
voltage, current, and temperature from the latest scanned data, filters it for glitches, and loads it into a
global variable called " Final Data " . This same global variable is used in many other VIs and demonstrates
one of the most powerful features of LabVIEW for passing information from one process to another. Global
variables as 10 element arrays are used extensively in all VIs for the stand. For example, " Battery Station
On/Off " keeps track of which stations are on. If a station is off, the main For Loop only updates the " Time
Zero " global array and uses the " Power Controller " VI to open all that channel's relays. If the station is on,
then if there is not a glitch in the data (values out of range), the " Cycle State " VI is called to decide if the
battery should continue in that state, be switched to the following state, or turned off.
Cycle State is the most complex of the subVIs in Battery Cycler because it uses the most input
parameters. It uses the data from the global variable array " Final Data " and compares it to defined control
parameters for deciding whether to call upon " New State " to switch state. The " Discharge " state is
terminated only when the battery voltage dips below the discharge cut-off voltage control parameter. The
following " Discharge Rest " state is terminated when the state time exceeds the discharge rest time control
array parameter and when the battery temperature is below the temperature limit control parameter. The
following " Charge " state is terminated when either of the following occurs; (1) charge current is below a
trickle threshold control parameter which indicates trickle charging is occurring, (2) battery voltage exceeds
battery voltage limit control parameter, or (3) battery temperature exceeds the control parameter limit. The
following " Trickle Charge " state is terminated when either of the following occurs; (1) state time exceeds
trickle charge time control array parameter, (2) battery voltage exceeds battery voltage limit control
parameter, or (3) battery temperature exceeds the control parameter limit. The following " Charge Rest "
state is terminated when the state time exceeds the charge rest time control array parameter and when the
battery temperature is below the temperature limit control parameter. Upon termination of charge rest, the
cycle count for that battery is incremented and compared to the cycles required control array parameter. If
cycles completed exceeds cycles required, then Power Controller is called to turn off that station. If not,
then New State is called. In both cases, the cycle highlights stored in a global variable array called " Cycle
Endpoints " are stored to a file by the VI " Cycle Log " .
New State uses the Power Controller VI to switch relays from on state to the following state. For
every state switch, Power Controller is called to turn off the current state followed by turning on the new
state. A couple complexities merit mention. Nominally, the chargers require an input of constant 11 volts.
Certain chargers require a constant current input which is accomplished by telling the Power Controller to
" discharge " the battery with a charging current through the discharge loop. The discharge relay indicators
will be on but the battery will be charging. This simplifies the software and serves as reminder that this
charger operates with a constant current input. User controlled constant rate trickle charging is also handled
the same way though the discharge loop.
Batt Hist VI Operation
The VI " HIST " was purchased from Gary W. Johnson, Inc., in Livermore, CA, and modified into
" Batt Hist " to fit the stand's purposes. The major modifications include using the global variable " Final
Data " as the source of data and logging data into sequentially suffixed files. The 40 channel data of Final
Data is put into format compatible with HIST by the VI " Final Data 1D "
The Watchdog VI simply tells one of the Hydra Data Acquisition Units to periodically send a
digital I/O pulse to the Watchdog Timer circuitry in the Relay controller. If the VI fails to do so within a
300 seconds span, the timer will trip open all relays and not accept any new commands without being reset.
The VI " Station Restart " allows one to begin or resume cycling a battery after it has been turned
off. One selects the station index to restart, what state its should start in, and what filename should log the
highlights of its cycling. Prior to executing Station Restart, make sure that the boolean station on/off control
on the front panel of " Battery Cycler is on. The key feature here is that Battery Cycler never has to be
interrupted during this process. Therefore, the cycling of the other batteries is uninterrupted while making
modifications to one or more batteries.
" Ni-MH Battery Test Stand Schematic Drawings " by S. Hossain and B. Hughes, LMES, Jan 94.
Hydra, 2625A Data Logger and 2620A Data Acquisition Unit, Users Manual, Fluke, Inc.
Interactive Digital Programmer, Model TLD-488-16, Operator's Manual, Kepco, Inc.
Bipolar Operational Power Supplies Model 20-10M Instruction Manual, Kepco, Inc.
Benchmarq Charger Evaluation Board, product literature, Benchmarq, Inc.
Integrated Circuits Systems 1702 QuickSaver Evaluation Board,
User Guide to the S77XX Heat Conduction Calorimeter, TTA-OP-O-54
LabVIEW 2 User Manual, National Instruments, Inc.
HIST, Historical Trending Package for LabVIEW, User's Manual, Gary W. Johnson, Inc.
Design, Specifications, and Operation of the Cell Calorimetry Experiment
A heat conduction calorimeter, model # 5023, and custom 4/3A cell holder from Hart Scientific
were used in this experiment as shown in Figure B1. The cylindrical calorimeter chamber is capable of
accommodating cells as large as DD size. To provide proper heat conduction using a 4/3A cell, the cell is
stripped of its insulating sleeve and inserted into the holder. The fit is very snug to maximize thermal
contact. Heat from the cell is conducted to the cylindrical wall of the calorimeter chamber which contains
The calorimeter operates on the Seebeck or thermocouple effect. As heat is conducted through the
thermoelectric device, a voltage is produced which is proportional to the temperature difference across the
thermoelectric device. The water side of the thermoelectric sensor is maintained a constant temperature by
virtue of the continuously-circulating, temperature-controlled water bath. As the temperature of the test
article side of the thermoelectric sensors fluctuates, the proportional voltage signal recorded is a measure of
the heat flow through the sensors.
The water bath maintains the water temperature within ? 0.01 °C. The sensitivity of the heat
measurement is 100 uW. The measurements are calibrated by replacing the cell in the holder with a resistor
simulating the heat generation levels of the cell. With precise knowledge of the electrical power input into
the calibrating resistor, a calibration factor is obtained for the experimental conditions that converts the
voltage reading of the thermoelectric sensors into a heat value. By calibrating with similar current levels and
external heat disturbances, most sources of error are canceled out. Accuracy of the calibration measurement
was within ? 0.5 mW.
For this experiment, one of the 4 cells from the battery packs which were cycled 400 times was placed in
the holder. The other 3 cells where place on the outside top of the calorimeter and connected in series to the
cell inside the calorimeter. Together electrically, the 4 cell pack was cycled 25 times with one of the stations
of the cycler described in Appendix A. Voltage sense leads connected very close to the cell tabs inside the
cell holder were provided for an accurate voltage measurement. The sense and power leads were built into
the holder stand-offs.
Fig. B1. Cross section of cell calorimetry experiment.
Set-Up and Procedure for Destructive Physical Analysis (DPA)
All cells were disassembled in a fully charged state inside an argon filled glove box, manufactured
by Vacuum/Atmospheres Company. Prior to each cell disassembly, the glove box was purged with argon
until a purity of & gt; 99% was confirmed by gas sample analysis by gas chromatography. Humidity of the glove
box was maintained between 20% and 40% and measured by a hygrometer to prevent cells from drying out
during disassembly. The purpose of the inert environment was to prevent oxidation of active material and
due to the pyrophoric nature of some metal hydrides.
While inside the glove box, cells were stripped of their insulation and tabs. A miniature lathe manufactured
by Sherline (P/N 60428) was used to make a circumferential cut just below the crimp seal of the cell. The
positive tab was cut to separate the top of the cell from the rest of the cell assembly. The sharp metal
cutters, a small cut in the can was made next to where the outer electrode ends two layers of separator
overlap each other. With needle-nose pliers, the cell can was peal away until electrode coil was released.
The negative tab, which consists of a metal ring which is welded to the edges of the negative current
collector, was pealed away to free the electrode coil. At this point, the separator overlap which is glued to
the inner separator layer is maintaining coil compression. Using a sharp blade, the separator glue joint was
undone which permitted uncoiling the jelly-roll electrode coil. The cell's dual separator design meant that
each electrode was wrapped in separator.
Once each electrode and separator were separated, each was rinsed three times in de-ionized water
to remove as much KOH deposits as possible. After a one hour drying time, coupons of each electrode and
separator were obtain, double bagged, and removed from the glove box.
The coupons for the SEM and EDS analyses were prepared by cutting 1 cm square coupon of each
electrode material with its current collector. I designed a custom coupon holder to keep the coupon sealed
from the ambient environment until a vacuum had been achieved. Then, a gear mechanisms on the holder
allowed it to be remotely opened for viewing by the SEM. Special attention was paid to not disturb the
surface of the specimen coupons. For the surface area and pore size distribution analysis of the positive
electrodes and the particle size analysis of the negative electrodes, specimens were obtained by gently
scrapping the active material off their respective current collectors.
For the surface area and pore size analysis was performed with a Coulter SA 3100 surface area and
pore size analyzer manufactured by Coulter Corporation. All specimens were out-gassed at 70 °C for 60
minutes prior to measuring the BET surface area using helium.
For the particle size analysis of the negative hydride, all specimens were prepared in a test tube to
with 2 ml of water with a drop de-agglomerizer added. The specimen solutions with the insoluble active
material were treated to the same 2 minute ultrasonic treatment. The analysis was performed with a Horiba
LA-910 laser scattering particle size distribution analyzer manufactured by Horiba Instruments Inc. Each
specimen was further agitated for 5 minutes and circulated for 7 minutes in the instrument prior to the
Set-up and Procedure for Video-Microscopy
For the in-situ video-microscope experiment, the cell coil was uncoil only enough to allow a small
1 cm square corner cut of the outer hydride electrode and the adjacent separator layers to expose the
positive nickel electrode. The coil compression was regain with tie-wraps as shown in Fig. D1. The coil
was double bagged and removed from the glove box.
Sturdy nickel strips 1 mm thick were spot welded to the tabs of the coil. The strips were fed
through to a customized rubber stopper made for a 1 L polymethylpentene beaker. The beaker material was
chosen for its tolerance to KOH attack and for its transparency. A 6.4 M solution of KOH was prepared and
spared for 2 hours with nitrogen gas to remove dissolved oxygen to prevent formation of carbonates. After
the solution was pour into the beaker to a level that immersed the exposed nickel electrode window of the
coil, the head space of the beaker was purged with nitrogen gas and sealed. All the above steps were
performed in one day to preclude long exposure of the cell and electrolyte to the ambient environment.
A video microscope system consisted of a video-microscope, Model PV10 CB, with a 10 to 70X
magnification lens, Model OVM-70X, and a high intensity light source, Model PV10-PS, all manufactured
by Olympus Corp. The lens was secured in place with a stand adjacent to the outside of the beaker wall
directly facing the area of interest of the electrode coil. The video output of the video-microscope was fed
to a VCR/TV system.
The desired current waveform was achieved by programming a Macintosh computer equipped with
a analog output card. This voltage signal was amplified by the Preston amplifier and fed to the current
control input of a bipolar power supply/amplifier, Model BOP-20-10M, manufactured by Kepco
Instruments, Inc. With the power supply in the current control mode, the voltage signal input into the power
supply produced the desired current waveform. This waveform was verified to be accurate within ? 1 mA
with a calibrated digital oscilloscope. Voltage and current data were measured and acquired with a Hydra
Data Acquisition Unit from Fluke, P/N 2620A. A LabVIEW VI was generated to control waveform and
record the voltage, current, and time data.
An audio signal was provided to the VCR to signal the occurrence of discharge pulse or relaxation
pause in the charge waveform. This signal was short beep made possible by connecting a buzzer to a
voltage comparator which triggered the beep every time the voltage signal from the computer was & lt; zero
volts. This beep was amplified by microphone and the resulting audio signal was fed to the VCR audio
The cell was discharged by connecting it to a 0.5 ohm resistor to 1.0V. After waiting 5 minutes, a
residual discharge at 1 ohm to 1.0V followed. The cell was allowed to rest & gt; 15 minutes prior to the charge
cycle according to the current waveforms described in Table 1. The nearly C-rate charge was terminated
after & lt; 70 minutes or earlier depending on the vigorous nature of the bubbling activity.
Fig. D1. Schematic of the in-situ video-microscopic experiment. Charge/discharge cycler and
electrical connections not shown for clarity.
Set-up and Procedure for Manometry
For the manometric experiments, complete fresh cells were used that were equipped with
solderable tabs. The cells were cycled at room temperature at C/2 rate 10 times to ensure their capacity
performance was nominal. A very small hole was drilled into the middle of the negative end of the first cell.
The cell tabs were soldered to wires which were soldered to nickel strips fed through a rubber stopper. The
cell/stopper assembly was sealed in a graduated cylinder filled with glass spheres used to consume volume.
The polypropylene tubing network connected the cell to a manometric gauge, Model E-00905, from ColeParmer Instrument Co. The gauge is designed to be used with 15 ml of mercury and has a readable level
range of 20 cm. De-ionized water was used instead to provide more pressure sensitivity.
The manometer was calibrated by introducing known volumes of nitrogen gas with a syringe
through the rubber stopper. For example, insertion of 1 ml of gas, produced a 4.1 cm displacement in the
The cycling control of the cell was performed with same set-up as in the video-microscopic
experiment. Charger was terminated when cell voltage reached 1.550V. Voltage sense leads were connected
to the nickel strips outside the rubber stopper. This introduced an extra 11.6 mohm of resistance that would
have been avoided if the sense lead could have been on the cell terminals. In comparison to the test cell for
the calorimetric experiment, the analogous resistance was measured at 4.5 mohm. This explains why the
overvoltage of the manometric experiments were about 10 mV higher while running at 2.0 A than the
overvoltage of the calorimetric experiments running at 2.3A.
The set-up for the flooded cell experiment varied slightly. A small hole was drilled into the centers
of both ends of the cells. The cell positive was placed on top to allow flooding the cell with 6.4 M KOH
without immersing the positive lid of the cell. The KOH solution was prepared as in appendix D. The head
space of the cell and manometer were purged with nitrogen before the cell rested for & gt; 1 week to ensure
complete flooding. More electrolyte was introduced and a subsequent purge followed to the first
charge/discharge cycle. Cell was allowed to rest for 2 more days, before the experiment started. For every
charge method, two charge/discharge cycles were performed and the second cycle was used for comparison.
This prevented variations due to various lengths of storage stand time. The rest time between the first and
second cycle was kept consistent at one hour and was not enough time to have cell pressures return to the
starting ambient pressure. Therefore, cell pressure was equalized to ambient pressure before the start of the
second charge/discharge cycle to re-zero the manometer.
Fig. E1. Configuration of nominal cell with manometer. Glass spheres taking up extra volume in
cylinder containing cell are not shown for clarity. Cell had small hole drilled into its negative end.
Fig. E2. Configuration of flooded cell with manometer. Cell had small holes drilled into its negative
and positive ends.