( where A is the water latent heat of vaporization, Nu=hD/k, and Sh Dhp/D12, neglecting both thermal radiation (it is li

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answerhappygod
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( where A is the water latent heat of vaporization, Nu=hD/k, and Sh Dhp/D12, neglecting both thermal radiation (it is li

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Where A Is The Water Latent Heat Of Vaporization Nu Hd K And Sh Dhp D12 Neglecting Both Thermal Radiation It Is Li 1
Where A Is The Water Latent Heat Of Vaporization Nu Hd K And Sh Dhp D12 Neglecting Both Thermal Radiation It Is Li 1 (189.16 KiB) Viewed 35 times
Where A Is The Water Latent Heat Of Vaporization Nu Hd K And Sh Dhp D12 Neglecting Both Thermal Radiation It Is Li 2
Where A Is The Water Latent Heat Of Vaporization Nu Hd K And Sh Dhp D12 Neglecting Both Thermal Radiation It Is Li 2 (306 KiB) Viewed 35 times
( where A is the water latent heat of vaporization, Nu=hD/k, and Sh Dhp/D12, neglecting both thermal radiation (it is likely to be considerable since convection is so low in a stagnant situation) and blowing effects on heat transfer. (b) Show that the result of part a can be reduced to = Cpai (Tw - Ts) A = Le @ 10 F Wis 1 - @ 10 where the Lewis number Le is defined as Le = D₁2/a and a = k/pCp. (c) For the case of T 70°F, determine the value of T (an iterative solution procedure is required since w₁o depends on the unknown T). How long will a 0.1-in.-diameter droplet last if evaporating at this equilibrium rate?
where A is the water latent heat of vaporization, Nu = hD/k, and Sh= Dhp/D12, neglecting both thermal radiation (it is likely to be considerable since convection is so low in a stagnant situation) and blowing effects on heat transfer. (b) Show that the result of part a can be reduced to ( Co (Tw - T}) A = Le W10 - WIS 1 - @ 10 where the Lewis number Le is defined as Le = D₁2/a and a = k/pCp. (c) For the case of T,= 70°F, determine the value of T, (an iterative solution procedure is required since w₁o depends on the unknown T). How long will a 0.1-in.-diameter droplet last if evaporating at this equilibrium rate?
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