Forced convective condensation in miniature channels is investigated numeri
cally. Capillary blocking that occurs due to condensation in a horizontal m
iniature tube and between parallel plates is simulated by using the Volume
of Fluid (VOF) method. The effects of vapor inlet velocity, saturation temp
erature, surface tension, and diameter on effective condensation length, fi
lm thickness, and heat transfer coefficient are investigated. The film thic
kness and the condensation length decrease as the hydraulic diameter or the
distance between parallel plates decreases. When the total mass flow rate
drops, the condensation length decreases significantly.