Thermodynamics HW Solutions 804

# Thermodynamics HW Solutions 804 -...

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Chapter 10 Boiling and Condensation 10-22 "!PROBLEM 10-22" "GIVEN" L=0.3 "[m]" D=0.003 "[m]" "epsilon=0.5 parameter to be varied" P=101.3 "[kPa], parameter to be varied" "PROPERTIES" Fluid\$='steam_NBS' T_sat=temperature(Fluid\$, P=P, x=1) rho_l=density(Fluid\$, T=T_sat, x=0) rho_v=density(Fluid\$, T=T_sat, x=1) sigma=SurfaceTension(Fluid\$, T=T_sat) mu_l=Viscosity(Fluid\$,T=T_sat, x=0) Pr_l=Prandtl(Fluid\$, T=T_sat, P=P) C_l=CP(Fluid\$, T=T_sat, x=0)*Convert(kJ/kg-C, J/kg-C) h_f=enthalpy(Fluid\$, T=T_sat, x=0) h_g=enthalpy(Fluid\$, T=T_sat, x=1) h_fg=(h_g-h_f)*Convert(kJ/kg, J/kg) C_sf=0.0060 "from Table 8-3 of the text" n=1 "from Table 8-3 of the text" T_vapor=1000-273 "[C], assumed vapor temperature in the film boiling region" rho_v_f=density(Fluid\$, T=T_vapor, P=P) "f stands for film" C_v_f=CP(Fluid\$, T=T_vapor, P=P)*Convert(kJ/kg-C, J/kg-C) k_v_f=Conductivity(Fluid\$, T=T_vapor, P=P)
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Unformatted text preview: mu_v_f=Viscosity(Fluid\$,T=T_vapor, P=P) g=9.8 "[m/s^2], gravitational acceleraton" sigma_rad=5.67E-8 "[W/m^2-K^4], Stefan-Boltzmann constant" "ANALYSIS" "(a)" "C_cr is to be determined from Table 8-4 of the text" C_cr=0.12*L_star^(-0.25) L_star=D/2*((g*(rho_l-rho_v))/sigma)^0.5 q_dot_max=C_cr*h_fg*(sigma*g*rho_v^2*(rho_l-rho_v))^0.25 q_dot_nucleate=q_dot_max q_dot_nucleate=mu_l*h_fg*(((g*(rho_l-rho_v))/sigma)^0.5)*((C_l*(T_s_crit-T_sat))/(C_sf*h_fg*Pr_l^n))^3 "(b)" q_dot_total=q_dot_film+3/4*q_dot_rad "Heat transfer in the film boiling region" q_dot_total=q_dot_nucleate q_dot_film=0.62*((g*k_v_f^3*rho_v_f*(rho_l-rho_v_f)*(h_fg+0.4*C_v_f*(T_s_film-T_sat)))/(mu_v_f*D*(T_s_film-T_sat)))^0.25*(T_s_film-T_sat) q_dot_rad=epsilon*sigma_rad*((T_s_film+273)^4-(T_sat+273)^4) DELTAT=T_s_film-T_s_crit 10-16...
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## This note was uploaded on 01/24/2012 for the course PHY 4803 taught by Professor Dr.danielarenas during the Fall '10 term at UNF.

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