“…Nomenclature: Alt, altitude in the experimental location (m); P, pressure in the experimental location (kPa); W, weight (g); MLR, mass loss rate (g/s); _ m ′ , mass loss rate (g/s); _ m ′′ , mass loss rate per square meter (g/m 2 s); _ m ′ b , mass loss rate during the boilover period mass loss rate (g/s); _ m ′ s , mass loss rate during the quasi-steady period (g/s); λ, thermal conductivity (kW/m · K); T f , flame temperature near the burner surface (K); T s , fuel surface temperature (K); D, diameter of fuel pan (m); h, convection coefficient (kW/m 2 · K); σ, Stephen Boltzmann constant; κ, effective absorption coefficient (m −1 ); T B , boiling point (K); T C , boilover critical temperature at the water-fuel interface (K); q ′′ s;c , nucleate boiling critical heat flux (W/m 2 ); t p , the time when boilover premonitory period starts (s); t b , the time when boilover occurs (s); ΔT excess , superheat temperature difference (K); χ, η, θ, percentage constant; C 1 , C 2 , A, B, k, constant; ΔH c , heat of combustion (kJ/mol); t, burning time (s); c p , specific heat capacity J/(kgK); T 0 , initial temperature of the water-fuel interface (K); h fg , evaporation latent heat (KJ/kg); R, thermodynamic constants; d, thickness of the waterfuel interface (m); ρ inter , density of the water-fuel interface (g/m 3 ); m inter , mass of the water-fuel interface (g); Rad, radiation (W/m 2 ); S, sound pressure level (dB); I Rad , intensity of the boilover based on radiation; I S , intensity of the boilover based on sound pressure level; I m , intensity of the boilover based on mass loss rate; P, pressure in the experimental location (kPa); T C , boilover critical temperature (K) Subscripts: N, normal pressure; L, low pressure Hua et al's 7 experimental examinations demonstrated that boilover only happens after the fuel-water interface temperature has reached the boiling point of water, and it can be the criterion of boilover premonitory period. Inamura et al 8 and Garo and Vantelon 9 found an important feature, which has been proved by many studies; the fuelwater interface temperature must be around 120°C, when a boilover occurs. Ferrero et al 10 carried out a series of large-scale pool fire experiments to improve knowledge of the thin-layer boilover phenomenon.…”