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  • Thin sleeves to insulate screws (no more tape)

    General Discussion
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    sepiS
    @doho that's a great idea, I'll give it a try!
  • Updates on development kit, large-format cell, roadmap

    Blogs
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  • Fe-Mn

    Electrolyte Development
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    Charging to 6Ah/L at 30mA/cm2 and discharging at 5mA/cm2. At most we only get 2-3 Ah/L of available capacity, same as if we charged to 4Ah/L. [image: 1758211363268-f3e1b8fc-98a1-4c8b-b305-b4d4a5bedee6-image.png]
  • Only Fe system

    Electrolyte Development
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    This test showed some deterioration on cycling: [image: 1758097795042-c586de1d-8d24-4884-bd7a-a00afb789080-image.png] I took out the catholyte and anolyte when charged (you can see the anolyte (left) and catholyte (right) in the pictures below). There isn't any hydroxide precipitation in either one. However there are some pieces of detached Fe metal on the anolyte, which I think are what causes the slight loss in capacity and increases in ohmic resistance as a function of time. [image: 1758097834649-5ee56443-1754-4f62-9a96-83d6194304ca-image-resized.png]
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  • 3D printed barbed connector

    General Discussion ting 3dprint
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    sepiS
    My pumps didn't have them, only the ones built into the pump. I saw that on some of your pictures, you have additional fittings between the different elements, I guess to make it easier to connect and disconnect the cell. In the end, it might make more sense to just shrink the barbs on the flowframe and/or tank a bit so the tubing comes off mor easily.
  • New Certified Open Source Hardware!

    Blogs
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    sepiS
    Congratulations, that's great to hear!
  • Alternative Electrolytes

    Electrolyte Development
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    sepiS
    @danielfp248 huh, that makes a lot of sense.
  • Separator material

    General Discussion
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    sepiS
    @danielfp248 ah, that makes sense as a last resort measure but would it not be nice to not lose charge? Well it all depends on how easiy it is to counteract by setting a different flow for the different electrolytes.
  • Theoretical Practical tank size limit

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    @Vorg We will slowly get there but no, right now we don't have any kWh capacity battery. As I mentioned, it will be several years before we get there. The fun is to walk this path and make everything open source on the way.
  • MyStat PCBs for free

    General Discussion
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    @sepi Hi, if you do the selling of the tube, I would order 2 (two) meters.
  • RFB University

    General Discussion
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    sepiS
    @danielfp248 sorry, my question was not well formulated. I meant a potential between the electrolytes inside the cell independently the possibility of measuring them using an electrode. Or to formulate it differently, if you cut through the cell (lile you cut a sandwich) and plotted the electrical potential between the electrodes, how would it look like?
  • Blog: czahl's build

    General Discussion
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    @czahl I am a huge fan of trying this, especially for the larger format where setups are likely to be more permanent. As kirk mentioned we have never actually tried it, so please let us know if you do!
  • Yeah… That went well.

    Blogs redflow solar victron
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  • Towards a working system

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    Q
    @muntasirms Absolutely! A bunch of other great documentation on here, wanted to try to my part. I have a colleague who uses HIPS exclusively in strong alkaline systems. Significantly easier to print than PP from my limited experience. It's not pure polystyrene (which is great for alkaline), but the additive(s) don't seem to affect their tolerance too much. I'll keep you posted on compatibility as I test these systems! Not sure how long the parts will last yet.
  • Adopting the Contributor Covenant

    Announcements
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    C
    @kirk In general this is exactly the way how all of us should act here (and in all other open source projects). But it is always better to have something like this in advance and it does not harm. I highly welcome to have a written code of conduct. Thanks Kirk, for taking care.
  • Systems engineering and modeling

    General Discussion
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    @kirk @sepi I think Bert's models are free to download off his site, but if you wanted to read the paper, I'm happy to email them to you or you can reach out to him for a copy.
  • Sourcing parts

    General Discussion
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    kirkK
    On it, thanks @sepi !
  • All-copper

    Electrolyte Development
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    @Vorg The reaction is not of elemental iodine with Zinc metal, it is of triiodide with Zinc metal. While this reaction is very exothermic, it is not explosive in this context because of a few reasons: While all the Zn is deposited at the same spot the oxidized iodine is distributed through the entire catholyte volume, so if the membrane ruptures it takes a while for the reaction to happen, it doesn't all happen at once. There is a lot of water here, which carries a lot of thermal load. While you can generate a lot of heat on membrane rupture, it isn't even enough to boil the solution at 100% SOC (from my experience). Per point 1, only a small fraction of iodine is able to react at any given point and for more to react flow must be present. Zn here is bulk Zn, it is not powedered or finely divided at all I have seen this happen experimentally at high SOC at 2M KI using photopaper. The membrane ruptured at high SOC and what I saw was the volume all shift mostly to one side and the potential drop very quick. Nothing exploded, melted or anything that dangerous. Untreated photopaper is obviously not intended to be a long term use membrane, it is intended as a viable membrane to carry out short term testing that is very easily accessible. To use it long term it is necessary to increase its lifetime with a PVA coating or something along these lines. The most dangerous scenario in my experience is solid iodine forming in the cathode, blocking flow and causing tubing to unhook, this then splashes charged electrolyte, which is a considerably greater hazard. The use of triethylene glycol seeks to mostly prevent this scenario, but it is still possible if very high currents are used or the cell is overcharged to high potentials (>1.6V). With the above said, the anolyte and catholyte hold a lot of energy and mixing them obviously instantaneously discharges all that energy. At 10mL of total volume this is not much, around 250mWh but when using larger volumes this is a considerable risk and larger scale devices must be created and tested with this potential scenario in mind. About the copper, oxygen in it would ruin the electrolyte because it would oxidize Cu+ to Cu+2 and this reaction would also increase the pH of the anolyte. This would eventually cause Cu hydroxide to fall out and kill the device. To recover the cell you would need to purge the electrolyte with Argon, cycle the solution over Cu metal to reduce the oxidized Cu2+ back to Cu+ and add hydrochloric acid to adjust the pH back to the proper level if necessary. To run a cell like this you need to make the system quite airtight and ensure the electrolyte is purged with Argon from the start. An idea to test for a period under oxygen-present conditions is to keep a piece of sacrificial copper in the anolyte reservoir to make sure that any Cu2+ that is formed is reduced back, so that way you would only succumb to the slow pH up creep. However this means that the CE you measure isn't really fair, because you are not accounting for a huge chunk of active material present there. It can be useful however to cycle and perhaps get some insights into other sections of the system under a regular atmosphere. However I don't honestly know if this is good enough, as the reaction of Cu+ with oxygen is quite fast. The copper chloride (I) initial electrolyte is usually prepared like this (under copper metal) to make sure there is no Cu2+ present when first loading the electrolyte into the device.

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