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1)  longitudinal flow of shell heat exchanger
纵流式换热器
1.
The heat transfer process and pressure drop of the longitudinal flow of shell heat exchanger with different percentage of opening were studied using a simplified model while the Reynolds numbers were (5 000),(10 000),(15 000) and(20 000.
5的孔板支撑纵流式换热器,在雷诺数为5 000,10 000,15 000和20 000时的传热和压降情况,讨论了流体的雷诺数、支撑板的开孔度及开孔方式对传热系数和压降的影响。
2)  longitudinal flow shell side heat exchanger
壳程纵流式换热器
3)  tube-shell heat exchanger with longitudinal flow of shellside
纵流管壳式换热器
1.
Several typical supporting structures of tube bundles of a tube-shell heat exchanger with longitudinal flow of shellside were reviewed, and their performance were compared with.
分析了纵流管壳式换热器的壳程管束支承的常见结构型式 ,通过对各种支承结构对壳程流体流动、传热和抗振等性能影响的定性比较 ,提出一种新型的支承结构型式 ,该结构不仅具有以往结构所具有的降低壳程流动阻力、节能和不易结垢等特点 ,而且还具有单位面积上布管数多、结构紧凑和传热效率高等优
4)  longitudinal shell-and-tube heat exchanger
纵流壳程换热器
5)  longitudinal and helical flow shell-and-tube exchanger
纵向多螺旋流管壳式换热器
6)  spirally longitudinal shell-and-tube thermal exchanger
螺旋纵流管壳换热器
1.
Heat transmiting principle and realization of spirally longitudinal shell-and-tube thermal exchanger;
螺旋纵流管壳换热器的传热机理与实现
补充资料:咏黄山寄程太守式之
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