Abstract
Conventional plain baffles are often used in heat exchangers with helical baffles. There are two X-shaped triangular leakage zones between the two adjacent plain baffles, which decrease heat transfer performance of the heat exchanger obviously. The improved configuration of ladder-type fold baffle was proposed. Folded panels of the two adjacent ladder-type fold baffles contact closely to eliminate the triangular leakage zones and thus the shell-side flow field is improved significantly. The experimental results show that the overall heat transfer coefficient of the improved heat exchanger with ladder-type fold baffles increases by an average value of 21.4% compared with that of conventional heat exchanger with plain baffles. And the shell-side heat transfer coefficient increases by an average value of 27.3%. However, the increment in pumping power penalty due to the increase of shell-side pressure drop is 2~80 W. The thermal performance factor TEF is enhanced by 14.8%~24.2%, with an average value of 19.5%. In addition, heat exchangers with ladder-type fold baffles are convenient in localization and installation. The results of this paper are of great significance in the optimum design of the heat exchanger.
| Original language | English |
|---|---|
| Pages (from-to) | 795-801 |
| Number of pages | 7 |
| Journal | Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities |
| Volume | 29 |
| Issue number | 4 |
| DOIs | |
| State | Published - 1 Aug 2015 |
Keywords
- Flow field improvement
- Heat exchanger with helical baffles
- Heat transfer enhancement
- Ladder-type fold baffles
- Triangular leakage zone
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