A unified model of multiphase heat transfer is developed for different flow patterns of gas/liquid pipe flow at all inclinations -90°t o +90°from horizontal. The required local flow parameters are predicted by use of the unified hydrodynamic model for gas/liquid pipe flow recently developed by Zhang et al. (2003aZhang et al. ( , 2003b. The model prediction of the pipe inside convective-heat-transfer coefficients are compared with experimental measurements for a crude-oil/natural-gas system in horizontal and upward-vertical flows, and good agreement is observed.Bubbly Flow and Dispersed-Bubble Flow. In multiphase heattransfer modeling, bubbly flow and dispersed-bubble flow can be treated as pseudosingle-phase flow. The fluid physical properties are adjusted on the basis of liquid holdup. In this study, the Petukhov (1970) correlation is used for dispersed-bubble flow and turbulent-bubbly flow,