With enough discharging momentum, the heat transfer coefficient could be maximized mostly. As the diameter of the water droplets from the WMFSS is very small, the total area A is also increased. The heat extraction due to water drops evaporation q2 can be expressed in terms of weight of water W, specific heat of water Cpw, specific heat of steam Cps, latent heat of vaporization of water and temperature differences Δt1, (whereΔt1 = tB - tL) andΔt2, (whereΔt1 = tS - tB).
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With enough discharging momentum, the heat transfer coefficient could be maximized mostly. As the diameter of the water droplets from the WMFSS is very small, the total area A is also increased. The heat extraction due to water drops evaporation q2 can be expressed in terms of weight of water W, specific heat of water Cpw, specific heat of steam Cps, latent heat of vaporization of water and temperature differences Δt1, (whereΔt1 = tB - tL) andΔt2, (whereΔt1 = tS - tB). ))
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With enough discharging momentum, the heat transfer coefficient could be maximized mostly. As the diameter of the water droplets from the WMFSS is very small, the total area A is also increased. The heat extraction due to water drops evaporation q2 can be expressed in terms of weight of water W, specific heat of water Cpw, specific heat of steam Cps, latent heat of vaporization of water and temperature differences Δt1, (whereΔt1 = tB - tL). AndΔt2, (WhereΔt1 = tS - TB).
)).
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With enough, discharging momentum the heat transfer coefficient could be maximized mostly. As the diameter of the water. Droplets from the WMFSS is, very small the total area A is also increased. The heat extraction due to water drops evaporation. Q2 can be expressed in terms of weight of, water W specific heat of water Cpw specific heat, of, steam Cps latent heat of. Vaporization of water and temperature differences Δ T1, (where Δ T1 = tB - tL) and Δ T2, (where Δ T1 = tS - tB).).
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