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Charging method lifepo4 280AH EVE (float or not.)

I have 32 cells of 3.2v LF280ah Eve batteries and just about to install them and would like to know charging parameters for Bulk, Absorption, and Float. According to paperwork i see bulk should be 14.6v (3.65v x 4) running a 12v setup. Any help would be appreciated.

Michael
This simple question can have a really complicated answer. :)
@Ampster's simple answer is pretty good though.
 
I am using this for my catamaran house bank. So I have 2640 watts of solar with two solar chargers, cerbo, touch 50, Quattro 12v/5000w/120amp inverter/charger x 2 run in parallel to give me 10k watts of inverter power to run a/c - water heater - water maker - washing machine etc…We live on it full time.
 
In that case you can use some Float to keep the cells topped up from Solar so you go into the evening with a full pack. A good Float setting would be 3.32 to 3.34 per cell to keep them at resting voltage duing the day. Depending on your charge controller a low current cutoff for Absorb could accomplish the same result. Float and Absorb are variations of Constant Voltage settings.
 
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So your saying to float at bulk/absorption at 14.0v and float to 13.4v? I know I had drop in lithium’s (Battleborn) before and bulk/absorption were 14.6v and float was 13.8v; wondering if these batteries would be similar in the voltage/percentage?
367DBC42-7AFF-4E64-AE60-17670F58CC6F.jpeg
 
if you're using victron charge controllers, use the victron lithium charge profile for best allround performance
 
Sorry this turned out to be so long.

There are two things that happen at high state of charge that are detrimental to LFP longevity.

First is negative side graphite anode swells about 11% due to all the lithium ions packed in between the graphite lattice when fully charged. It is called intercalation. This puts stress pressure on the protective SEI layer between graphite anode and electrolyte. SEI (Solid Electrolyte Interface) is a very thin grown protective layer to repell electrons from entering electrolyte which will degrade electrolyte. For normal cell operation, only lithium ions should flow in electrolyte. Lithum ions create electrons transfer in the positive (LiFePO4) and negative (Graphite) electrodes which are then passed to the battery terminals. I will come back to this so remember cell current output demand requires lithium ion flow within cell. The more current demanded, the greater the internal ion flow must be.

SEI normally gets some small cracks everytime a cell is charged. It is regrown on subsequent charging but this regrowth consumes a little bit of available lithium which reduces cell capacity a little bit for every full recharge. The SEI regrowth repair process also thickens up the SEI layer which increases cell impedance to flow of lithium ions. Over time, SEI continued growth from recharge cycles is the primary aging process in all lithium ion cells. It locks up lithum, reducing cell capacity, and increases cell impedance over time.

Second is the higher cell voltage. The greater the cell voltage, the more the barrier is reduced for electrons to jump the repulsive barrier at the graphite-electrolyte interface and enter the electrolyte. This causes decomposition of electrolyte which is the second most significant aging process for all lithium ion cells. Higher temp also accelerates this so maintaining high state of charge in a warm environment results in faster aging.

When you overcharge a cell with higher then 3.65v you encourage electrons to enter electrolyte. Above about 4.3v the rate of electron entering electrolyte really increases. When electrolyte decomposes it outgasses (mostly carbon dioxide) which causes cell to bloat. Second more damaging is other electrolyte decomposition compounds gum up electrode to electrolyte interfaces reducing lithium ion migration paths through the cell increasing cell impedance.

----extra info ----
Charging is not just about cell terminal voltage. It also depends on what the bulk charge current is. Back to ion flow. Whether it is charging or discharging, some overpotential (terminal voltage drop for discharge and terminal voltage rise for charging) is required to create a lithium Ion from a lithium atom and move it along through the electrode material, across the electrolyte, and into other electrode. Some of this overpotential is used to break loose the electron to create the ion and some is used to push the ion along.

There is also some pure cell metal conductor IR loss, which is mostly what you are measuring when doing a 1 KHz AC cell impedance measurement with a YR1035 battery impedance meter. This measurement also has some contribution for ion migration movement. It only contributes 5%-50% of actual terminal voltage discharge drop or charging rise depending on amount of cell current demanded.

This overpotential drives the creation and movement of lithium ions. The movement of lithium ions is proportional to demanded cell current. The more the demanded cell current the more overpotential required to create and move the ions.

The relation between cell current and overpotential voltage is proportional to the log of the demanded current. This holds up to the point where the electrodes (anode and cathode material) start to become starved for ions to move due to thickness of electrode material. The onset of ion starvation is dependent on electrode thickness for a given cell design. 'Blue' cells are designed with thick electrodes to give good AH capacity. Their downside is peak current capability which starts to enter electrode starvation at about 0.5 CA of demanded current. Current demand must be met so overpotential must get greater to drive the restricted electrode starved ion movement.

When you charge at higher currents there is more overpotential terminal voltage rise to move greater volume of ions so the 'internal' cell is effectively seeing a lower voltage. This is why terminal voltage is not the complete story of determining when a cell is fully charged. This higher overpotential at higher current also means more internal cell losses and more internal heating.

This is same process for discharging.

3.43v is the magic 'neutral' full charge voltage for a LFP cell. Any voltage above 3.45v with near zero charge current flow is a fully charged cell. The overpotential requires a minium of 10-20 mV above (charging) or below (discharging) the rested cell voltage to create any small cell current. This is why just passively paralleling cells will not fully balance them. The higher SOC cell will end up being about 10 mV higher while the lower SOC cell will end up being about 10 mV lower once they are separated and reach their equilibrium rested open circuit voltage. This net 20 mV rested OCV difference can still have a 30-40% difference in SOC between cells.

Other important item is overpotential shift has a time delay after a demand current is changed. It typically takes 1-3 minutes to equilized but this time increases below 20% state of charge. It also has variance in time above 90% state of charge but there is another factor in that region explained in next paragraph.. Overpotential versus current demand is dependent on temperature. Overpotential versus demanded current starts to really get worse below about 10 degs C. At -20 degs C it is terribly high resulting in a very restricted maximum current capability from cell and terminal voltage collapse effecting ability to pull out AH's of cell capacity.

So why does a cell taken off a full saturated charge at 3.65v not drop to 3.45v. This is caused by a surface charge build up mostly in graphite anode. As cell approaches full charge and charging current drops off, the required overpotential drops. At a constant 3.65v, overpotential is traded for surface capacitance charging. For LFP, this surface charge energy is only about 0.01% of cell's rated AH capacity (28 mA/H for 280AH cell) but can take several days to bleed itself off without any external help. A 1-3 ohm power resistor can bleed off the surface charge in a minute or two. Like discharging an electrolytic capacitor it takes a little time for electrons to diffuse out of the effective dielectric. You should have close to 3.45v once surface charge is bled off.

Now for the uncomfortable revelation, matching AH's and cell impedance does not totally ensure matched cells. Overvoltage at a given current (and temp) must also be matched. It becomes more important if you subject cells to high discharge or charge currents. Packed together prismatic cells at high discharge current results in center core cells having less ability to dissipate heat. Since overpotential is temperature dependent, there will be overpotential mismatch on the bundled prismatic cells. There is a reason Tesla and Battleborn use cylindrical spaced cells.

LFP Over-potential Chart.png
 
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if you're using victron charge controllers, use the victron lithium charge profile for best allround performance
Yes using all victron products for this setup. Victron solar chargers, inverter/chargers, Rec BMS, cerbo, touch 50, orion dc/dc (for charging house bank to starter battery), wake speed (charging alternators to house bank), 2640 watts of solar, 2240ah of Eve lithium batteries.

@RCinFLA thanks for the lengthy explanation I do appreciate it, I just really want to know what I should set my chargers too for B/A/F settings. I loved reading what you wrote. What I understand that 3.43v should be the float which is 13.72v, and bulk should be? According to others some say 14v, others says 14.2v, wondering your thoughts?
 
What I understand that 3.43v should be the float which is 13.72v, and bulk should be? According to others some say 14v, others says 14.2v, wondering your thoughts?
I float mine at 3.35v per cell which is around 85% state of charge. This is common for a UPS application using LFP batteries. I don't really need to maintain a full charge.

But you also have to think about BMS balancing. Many BMS's don't balance until a cell rises above 3.4v and with small amount of balancing dump current, to get any balancing time you have take absorb up to 3.50-3.55v per cell. If you don't achieve some level of dump on all cells you might have a cell that just keeps getting lower and lower in state of charge relative to other cells.

For just a single string of 280 AH cells you need to provide a minimum of 100 mA/day for balancing or 700 mA/hrs per week..
For a 200 mA balancing dump that is half hour per day or 3.5 hrs per week minimum.

Half hour per day does not sound like much but it means you must hold full absorb charging for at least a half hour per day or 3.5 hours per week to keep up with balancing. If you discharge and recharge at higher CA levels, or batteries kept in warmer environment, the balancing requirement is greater. If your charger is absorb current taper level terminated you may not stay in absorb long enough to get the required balancing time.

Bottomline, if your BMS trips off for cell overvoltage you are not getting enough balancing in.
 
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You have to terminate charging at an appropriate current.
I think that was what @RCinFLA FLA was implying when he said that for proper balancing you may need to be in Contant Voltage mode (Absorb) for an hour. The way most charging algorithms do that is with a setting for time or current.
 
Okay i just found an good article and now i get it a bit more.

How good is the victron blue smart? if i just buy that if i want to charge it slowly and leave it unatended for a few days and then just disconnected the battery. it should be alright then. just because i dont always trust timers. if it jams it keeps charging and then 1800bucks of batteries is wasted,
instead of 130bucks for an victron

Looking at the charging method from an CTEK charger (lifepo4) it just keeps it at 90%-95% 24/7 so that wouldnt be good at all.
I have used the blue smart to charge my SOK batteries. It works perfectly, and puts my mind at ease that I do not have to constantly monitor it.

 
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