摘要
对波形折流杆换热器与传统的弓形折流板换热器的传热性能及壳程流阻性能进行了工业实验研究 ,结果证明 。
A industrial experimental investigation of heat exchangers with curve-ROD baffle and with segmental baffle was carried into execution. The shell-side and tube-side heat transfer and pressure drop performances were studied. Two equations using the Reynolds number could predict the heat transfer coefficient of the shell-side and tube-side. The integrated characteristics of the curve-ROD baffle heat exchanger are superior to that of the segmental baffle one.
出处
《压力容器》
2004年第4期10-12,22,共4页
Pressure Vessel Technology
关键词
波形折流杆
弓形折流板
换热器
传热性能
流体阻力
curve-ROD baffle
segmental baffle
heat exchanger
heat transfer preformances
pressure drop
