If the condensation occurs at the outside surface of the tubes, then the equation for the heat transfer coefficient cab be represented as which one of the following?

• A. hVER=0.943\([\frac{K^3 p^2 g h_{fg}}{μx(T_{sat} – T_L)}]^{0.25}\)
• B. hVER=1.13\([\frac{K^3 p^2 g h_{fg}}{μx(T_{sat} – T_L)} ]^{0.25}\)
• C. hVER=0.723\([\frac{K^3 p^2 g h_{fg}}{μx(T_{sat} – T_L)} ]^{0.25}\)
• D. hVER=0.725\([\frac{K^3 p^2 g h_{fg}}{μx(T_{sat} – T_L) }]^{0.25}\)