TY - JOUR
T1 - Blockage of triangle leakage zones in heat exchanger with helical baffles
AU - Wang, Simin
AU - Ming, Yusheng
AU - Chen, Kang
AU - Zhang, Zaoxiao
AU - Wen, Jian
AU - Xue, Yulan
N1 - Publisher Copyright:
© All Rights Reserved
PY - 2014/9/1
Y1 - 2014/9/1
N2 - Four fan-shaped baffles are used to form a pitch in shell side of heat exchangers with helical baffles. There are two triangular leakage zones between the two adjacent baffles, making the shell-side fluid deviate from ideal plug flow and degrading the heat transfer performance of the heat exchanger. In this paper, the structure of fold baffle is used to block the external triangular leakage zones, so the shell-side fluid flows in approximately continuous spiral flow. The heat transfer experiments are used to evaluate the performance of the improved heat exchanger. The experimental results show that the shell-side heat transfer coefficient is increased by 11.6%-21.6% and the overall heat transfer coefficient is increased by 6.7%-19.1% with an average value of 16.9%, compared with that of conventional heat exchanger with plain baffles. The heat transfer of improved heat exchanger is intensified obviously. Although the shell-side pressure drop increases correspondingly, the increment in pumping power consumption is limited. The values of thermal performance factor are all above 1.0, with an average value of 1.071.It demonstrates that taking into account heat transfer coefficient and pressure drop, better integrative performance is obtained through the configuration optimization of baffles. It is benefit to optimizing design for heat exchangers with helical baffles.
AB - Four fan-shaped baffles are used to form a pitch in shell side of heat exchangers with helical baffles. There are two triangular leakage zones between the two adjacent baffles, making the shell-side fluid deviate from ideal plug flow and degrading the heat transfer performance of the heat exchanger. In this paper, the structure of fold baffle is used to block the external triangular leakage zones, so the shell-side fluid flows in approximately continuous spiral flow. The heat transfer experiments are used to evaluate the performance of the improved heat exchanger. The experimental results show that the shell-side heat transfer coefficient is increased by 11.6%-21.6% and the overall heat transfer coefficient is increased by 6.7%-19.1% with an average value of 16.9%, compared with that of conventional heat exchanger with plain baffles. The heat transfer of improved heat exchanger is intensified obviously. Although the shell-side pressure drop increases correspondingly, the increment in pumping power consumption is limited. The values of thermal performance factor are all above 1.0, with an average value of 1.071.It demonstrates that taking into account heat transfer coefficient and pressure drop, better integrative performance is obtained through the configuration optimization of baffles. It is benefit to optimizing design for heat exchangers with helical baffles.
KW - Experimental validation
KW - Fold baffle
KW - Heat exchanger with helical baffles
KW - Heat transfer
KW - Optimization
KW - Triangular leakage zone
UR - https://www.scopus.com/pages/publications/84907217286
U2 - 10.3969/j.issn.0438-1157.2014.09.011
DO - 10.3969/j.issn.0438-1157.2014.09.011
M3 - 文章
AN - SCOPUS:84907217286
SN - 0438-1157
VL - 65
SP - 3389
EP - 3394
JO - Huagong Xuebao/Journal of Chemical Industry and Engineering (China)
JF - Huagong Xuebao/Journal of Chemical Industry and Engineering (China)
IS - 9
ER -