<p>Lithium-ion battery (LIB) incidents remain challenging to mitigate because thermal runaway (TR) cells retain substantial internal heat, which can drive re-ignition and thermal runaway propagation (TRP) if suppression cooling is delayed or under-designed. This study combines pure-water spray cooling experiments on a 51 Ah prismatic NCM cell undergoing TR with a validated three-dimensional heat-transfer model to quantify how spray duration (<InlineEquation ID="IEq1"> <EquationSource Format="TEX">\(\:\tau\:\)</EquationSource> </InlineEquation>), total sprayed mass (<InlineEquation ID="IEq2"> <EquationSource Format="TEX">\(\:{M}_{spray}\)</EquationSource> </InlineEquation>), nozzle height (<InlineEquation ID="IEq3"> <EquationSource Format="TEX">\(\:{H}_{spray}\)</EquationSource> </InlineEquation>), and cell properties govern cooling outcomes. Cooling performance is evaluated using the rebound-peak temperature after spray termination (<InlineEquation ID="IEq4"> <EquationSource Format="TEX">\(\:{T}_{reb}\)</EquationSource> </InlineEquation>) and the cumulative exposure time above 150&#xa0;°C (<InlineEquation ID="IEq5"> <EquationSource Format="TEX">\(\:{t}_{&gt;150\:^\circ\:C}\)</EquationSource> </InlineEquation>), where 150&#xa0;°C is adopted as a conservative threshold for propagation risk. A validated three-dimensional transient heat-transfer model was established to describe post-TR spray cooling, internal heat redistribution, and temperature rebound. Under <InlineEquation ID="IEq6"> <EquationSource Format="TEX">\(\:{M}_{spray}\)</EquationSource> </InlineEquation> = 5&#xa0;kg and <InlineEquation ID="IEq7"> <EquationSource Format="TEX">\(\:{H}_{spray}\)</EquationSource> </InlineEquation> = 0.25&#xa0;m, τ ≈ 310&#xa0;s minimizes <InlineEquation ID="IEq8"> <EquationSource Format="TEX">\(\:{t}_{&gt;150\:^\circ\:C}\)</EquationSource> </InlineEquation> while keeping <InlineEquation ID="IEq9"> <EquationSource Format="TEX">\(\:{T}_{reb}\)</EquationSource> </InlineEquation> low. The existence of an optimal <InlineEquation ID="IEq10"> <EquationSource Format="TEX">\(\:\tau\:\)</EquationSource> </InlineEquation> reflects a trade-off: short <InlineEquation ID="IEq11"> <EquationSource Format="TEX">\(\:\tau\:\)</EquationSource> </InlineEquation> is limited by internal heat conduction and induces strong post-spray rebound, whereas long <InlineEquation ID="IEq12"> <EquationSource Format="TEX">\(\:\tau\:\)</EquationSource> </InlineEquation> reduces the impingement mass flux and slows the early-stage cooling rate. Increasing <InlineEquation ID="IEq13"> <EquationSource Format="TEX">\(\:{M}_{spray}\)</EquationSource> </InlineEquation> reduces <InlineEquation ID="IEq14"> <EquationSource Format="TEX">\(\:{t}_{&gt;150\:^\circ\:C}\)</EquationSource> </InlineEquation> with diminishing returns, and increasing <InlineEquation ID="IEq15"> <EquationSource Format="TEX">\(\:{H}_{spray}\)</EquationSource> </InlineEquation> monotonically degrades performance. Across prismatic cells, the recommended <InlineEquation ID="IEq16"> <EquationSource Format="TEX">\(\:\tau\:\)</EquationSource> </InlineEquation>shifts with cell geometry and thermal load, consistent with the role of thermal diffusion in post-spray heat redistribution. Finally, a Gaussian process regression surrogate model was developed to predict <InlineEquation ID="IEq17"> <EquationSource Format="TEX">\(\:{T}_{\text{r}\text{e}\text{b}}\)</EquationSource> </InlineEquation>, <InlineEquation ID="IEq18"> <EquationSource Format="TEX">\(\:{t}_{&gt;150,\text{D}\text{S}}\)</EquationSource> </InlineEquation>, <InlineEquation ID="IEq19"> <EquationSource Format="TEX">\(\:{t}_{&gt;150,\text{A}\text{S}}\)</EquationSource> </InlineEquation>, and <InlineEquation ID="IEq20"> <EquationSource Format="TEX">\(\:{t}_{&gt;150,\text{t}\text{o}\text{t}\text{a}\text{l}}\)</EquationSource> </InlineEquation> from spray conditions and cell-related parameters. Grouped five-fold cross-validation yielded <InlineEquation ID="IEq21"> <EquationSource Format="TEX">\(\:{R}^{2}=0.989-0.997\)</EquationSource> </InlineEquation>, supporting rapid screening of spray settings within the investigated parameter ranges.</p>

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Impact of Water Spray Conditions on Cooling of Thermal-Runaway Lithium-Ion Battery: Mechanisms and Optimization

  • Shenghao Luo,
  • Zhengguo Zhang,
  • Ziye Ling,
  • Xiaoming Fang,
  • Shuping Wang

摘要

Lithium-ion battery (LIB) incidents remain challenging to mitigate because thermal runaway (TR) cells retain substantial internal heat, which can drive re-ignition and thermal runaway propagation (TRP) if suppression cooling is delayed or under-designed. This study combines pure-water spray cooling experiments on a 51 Ah prismatic NCM cell undergoing TR with a validated three-dimensional heat-transfer model to quantify how spray duration ( \(\:\tau\:\) ), total sprayed mass ( \(\:{M}_{spray}\) ), nozzle height ( \(\:{H}_{spray}\) ), and cell properties govern cooling outcomes. Cooling performance is evaluated using the rebound-peak temperature after spray termination ( \(\:{T}_{reb}\) ) and the cumulative exposure time above 150 °C ( \(\:{t}_{>150\:^\circ\:C}\) ), where 150 °C is adopted as a conservative threshold for propagation risk. A validated three-dimensional transient heat-transfer model was established to describe post-TR spray cooling, internal heat redistribution, and temperature rebound. Under \(\:{M}_{spray}\) = 5 kg and \(\:{H}_{spray}\) = 0.25 m, τ ≈ 310 s minimizes \(\:{t}_{>150\:^\circ\:C}\) while keeping \(\:{T}_{reb}\) low. The existence of an optimal \(\:\tau\:\) reflects a trade-off: short \(\:\tau\:\) is limited by internal heat conduction and induces strong post-spray rebound, whereas long \(\:\tau\:\) reduces the impingement mass flux and slows the early-stage cooling rate. Increasing \(\:{M}_{spray}\) reduces \(\:{t}_{>150\:^\circ\:C}\) with diminishing returns, and increasing \(\:{H}_{spray}\) monotonically degrades performance. Across prismatic cells, the recommended \(\:\tau\:\) shifts with cell geometry and thermal load, consistent with the role of thermal diffusion in post-spray heat redistribution. Finally, a Gaussian process regression surrogate model was developed to predict \(\:{T}_{\text{r}\text{e}\text{b}}\) , \(\:{t}_{>150,\text{D}\text{S}}\) , \(\:{t}_{>150,\text{A}\text{S}}\) , and \(\:{t}_{>150,\text{t}\text{o}\text{t}\text{a}\text{l}}\) from spray conditions and cell-related parameters. Grouped five-fold cross-validation yielded \(\:{R}^{2}=0.989-0.997\) , supporting rapid screening of spray settings within the investigated parameter ranges.