TANG Xiaomin, WANG Hongda, YE Qiang, et al. Impact of stack spatial arrangement on gas precipitation and flow distribution uniformity in iron-chromium flow batteries[J]. Energy Storage Science and Technology, 2026, 15(6): 2224-2233.
TANG Xiaomin, WANG Hongda, YE Qiang, et al. Impact of stack spatial arrangement on gas precipitation and flow distribution uniformity in iron-chromium flow batteries[J]. Energy Storage Science and Technology, 2026, 15(6): 2224-2233.DOI: 10.19799/j.cnki.2095-4239.2025.1080.
Impact of stack spatial arrangement on gas precipitation and flow distribution uniformity in iron-chromium flow batteries
During the operation of iron-chromium flow batteries
hydrogen evolution as a parasitic reaction
together with gas release caused by electrolyte depressurization or heating (i.e.
oversaturation of dissolved gases)
can lead to gas accumulation within porous electrodes. This
in turn
increases flow resistance
causes local reactant starvation
and induces electrolyte maldistribution. These effects not only reduce stack efficiency but may also pose safety risks. In large stacks employing parallel electrolyte supply
this risk is particularly pronounced owing to variations in stack spatial arrangement
uneven flow-channel resistance
and fluctuations in electrode material properties. To address this
a two-dimensional steady-state gas-liquid slip flow model is established to investigate gas distribution characteristics within porous electrodes across differently arranged stacks. This study specifically examines the effects of hydrogen evolution rate
inlet dissolved gas concentration
and supply pressure difference on gas accumulation and electrolyte flow rate. The results show that increasing the hydrogen evolution current density markedly raises gas saturation and decreases the relative permeability of the liquid phase
making the upper stacks more prone to severe gas blockage. Elevated inlet dissolved gas concentration triggers rapid gas precipitation at the electrode inlet
with accumulation progressing along the flow direction. This exacerbates uneven flow distribution among stacks
causing electrolyte flow rate reductions that exceed 18% in upper stacks. Furthermore
maintaining an adequate feeding pressure difference is essential for ensuring sufficient electrolyte supply and effective gas removal. To keep the average gas saturation below 1%
the required pressure difference for upper stacks (45 kPa) must be 15 kPa higher than for lower stacks (30 kPa). Therefore
reducing stack height differences and lowering inlet dissolved gas concentration are key measures for suppressing gas-phase precipitation and ensuring uniform electrolyte flow distribution.
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references
ZHANG H M, LU W J, LI X F. Progress and perspectives of flow battery technologies[J]. Electrochemical Energy Reviews, 2019, 2(3): 492-506. DOI:10.1007/s41918-019-00047-1.
WEBER A Z, MENCH M M, MEYERS J P, et al. Redox flow batteries: A review[J]. Journal of Applied Electrochemistry, 2011, 41(10): 1137-1164. DOI:10.1007/s10800-011-0348-2.
ZENG Y K, ZHAO T S, ZHOU X L, et al. The effects of design parameters on the charge-discharge performance of iron-chromium redox flow batteries[J]. Applied Energy, 2016, 182: 204-209. DOI:10.1016/j.apenergy.2016.08.135.
FANG M L, ZHANG Y, QIAO L, et al. Research progress of iron-chromium flow batteries technology[J]. Energy Storage Science and Technology, 2022, 11(5): 1358-1367.
ZHOU Y, HAN P Y, NIU Y C, et al. Fabrication of metal-organic framework-derived C-Bi/CC electrode materials and their electrochemical properties in ICRFB[J]. Energy Storage Science and Technology, 2024, 13(2): 381-389.
WU M, NAN M J, YE Y J, et al. A highly active electrolyte for high-capacity iron-chromium flow batteries[J]. Applied Energy, 2024, 358: 122534. DOI:10.1016/j.apenergy.2023.122534.
WANG H D, YE Q, CHENG P, et al. A gas-liquid slip flow model for predicting bubble distribution and electrolyte blockage in porous electrodes of flow batteries[J]. International Journal of Heat and Mass Transfer, 2025, 251: 127357. DOI:10.1016/j.ijheatmasstransfer.2025.127357.
YE Q, DAI J C, CHENG P, et al. Gas evolution induced vicious cycle between bubble trapping and flow choking in redox flow battery stacks[J]. International Journal of Heat and Mass Transfer, 2024, 221: 125100. DOI:10.1016/j.ijheatmasstransfer. 2023.125100.
YANG J P, YE Q. Effects of electrodeposition of bismuth in an operating ironchromium redox flow battery base on a strategy of slow release of Bi 3+ across the membrane[J ] . Energy Storage Science and Technology, 2023, 12(4): 1075-1082.
ZHANG Y J, YE Q, NI M. The impact of in-situ hydrogen evolution on the flow resistance of electrolyte flowing through the carbon felt electrode in a redox flow battery[J ] . Journal of Power Sources, 2023, 564: 232837. DOI:10.1016/j.jpowsour.2023. 232837.
YE Q, ZHANG Y J, CHENG P, et al. Effects of wettability and flow direction on gas retention and flow resistance of water flowing through carbon felts with thermally induced gas evolutions[J]. International Journal of Heat and Mass Transfer, 2020, 156: 119911. DOI:10.1016/j.ijheatmasstransfer.2020.119911.
YE Q, SHAN T X, CHENG P. Thermally induced evolution of dissolved gas in water flowing through a carbon felt sample[J]. International Journal of Heat and Mass Transfer, 2017, 108: 2451-2461. DOI:10.1016/j.ijheatmasstransfer.2017.01.097.
DAI J C, YE Q, ZHAO T S. Increased electrolyte flow resistance and blockage due to hydrogen evolution in a flow battery single cell under stack electrolyte feeding conditions[J]. Journal of Power Sources, 2025, 628: 235940. DOI:10.1016/j.jpowsour. 2024.235940.
WANG X, YE Q. The aggravation of side reactions caused by insufficient localized liquid supply in an all-vanadium redox flow battery stack[J]. Energy Storage Science and Technology, 2022, 11(5): 1455-1467.
YOU X, YE Q, CHENG P. Scale-up of high power density redox flow batteries by introducing interdigitated flow fields[J]. International Communications in Heat and Mass Transfer, 2016, 75: 7-12. DOI:10.1016/j.icheatmasstransfer.2016.03.021.
WANG H D, DAI J C, YE Q, et al. Three-dimensional modeling of gas-liquid flow in iron-chromium flow battery negative electrodes featuring interdigitated flow fields[J]. International Communications in Heat and Mass Transfer, 2025, 169: 109961. DOI:10.1016/j.icheatmasstransfer.2025.109961.