Different strategies to improve industrial heat exchange

被引:179
作者
Stehlík, P
Wadekar, VV
机构
[1] Tech Univ Brno, Inst Proc & Environm Engn, Brno 61669, Czech Republic
[2] AEA Technol Hyprotech, HTFS, Harwell, Berks, England
关键词
D O I
10.1080/01457630290098673
中图分类号
O414.1 [热力学];
学科分类号
摘要
A variety of different strategies are available to process and equipment designers to improve industrial heat transfer These range from the use of efficient forms of individual heat exchangers to the optimum utilization of the individual units in a network, generally referred to as "process integration." This article attempts to review these strategies with reference to the conventional and more recent,forms of shell-and-tube heat exchangers. In the context of a heat exchanger network, process heat transfer intensification (global intensification), i.e., network, design for maximum energy recovery, is a first important step. This needs to be then combined with heat transfer intensification in individual units/shells (local intensification). The benefits of global and local intensification are illustrated with examples of a helically baffled heat exchanger (Helixchanger), as a representative of a more recent form of shell-and-tube exchanger. Some aspects concerning the use of multistream heat exchangers are discussed, and finally, an example for optimization of a plate-type heat exchanger is presented.
引用
收藏
页码:36 / 48
页数:13
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