Boiling or condensing inside vertical tube are not evaluated by any single equation today. Both directions of phase change go through 'flow regimes' in which the each phase may be turbulent, transition, or laminar by velocity or annular, bubble, sheer, flooded (ect.) by shape. These condition are determined and analyzed in increments that are weighted over the length of the tube. Short of the data and tools, you might estimate from text (Kern) or web resources.