Abstract
An experimental investigation was made on the condensation of water steam in a vertical corrugated duct. The data have been correlated as follows
Co=5.11Re−0.431 150 ≤ Re ≤ 350 Co = 0.034311Re−0.425350 ≤Re ≤l000
The vertical corrugated duct is constructed of two corrugated plates with corrugation inclination angles of β = 0 and β = 45° respectively (relative to the overall flow direction).
The condensation heat transfer coefficient in the corrugated duct is more than two times higher than that of bulk condensation on a vertical plate. A physical model was proposed to explain the heat transfer enhancement. Attention was also paid to the effect of exit steam velocity on the heat transfer during partial condensation. It was demonstrated that the heat transfer in the corrugated duct was strongly affected even at a low exit velocity, which was different from the case of bulk condensation on a vertical plate. Experimental apparatuses and the method for examining their reliability are described in detail.
KEYWORDS: