TY - JOUR
T1 - Experimental investigation on heat transfer performance of heat exchanger with ladder-type fold baffles
AU - Wen, Jian
AU - Yang, Hui Zhu
AU - Xue, Yu Lan
AU - Tong, Xin
AU - Wang, Si Min
N1 - Publisher Copyright:
©, 2015, Zhejiang University. All right reserved.
PY - 2015/8/1
Y1 - 2015/8/1
N2 - 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.
AB - 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.
KW - Flow field improvement
KW - Heat exchanger with helical baffles
KW - Heat transfer enhancement
KW - Ladder-type fold baffles
KW - Triangular leakage zone
UR - https://www.scopus.com/pages/publications/84942041997
U2 - 10.3969/j.issn.1003-9015.2015.04.004
DO - 10.3969/j.issn.1003-9015.2015.04.004
M3 - 文章
AN - SCOPUS:84942041997
SN - 1003-9015
VL - 29
SP - 795
EP - 801
JO - Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities
JF - Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities
IS - 4
ER -