Numerical investigation on non-Newtonian fluid flowing in heat exchanger with different elliptic aspect ratios and helical angles. (August 2018)

• Record Type: Journal Article
• Authors: Lin, Wenzhu; Ling, Ziye; Fang, Xiaoming; Gao, Xuenong; Zhang, Zhengguo
• Is Part Of: Applied thermal engineering. Volume 141(2018)
• Page Start: 164
• Page End: 173
• Publication Date: 2018-08
• Subjects: Elliptic tube -- Elliptical aspect ratio -- Helical angle -- Heat exchanger -- Numerical simulation; Heat engineering -- Periodicals; Heating -- Equipment and supplies -- Periodicals; Periodicals; 621.40205
• DOI: 10.1016/j.applthermaleng.2018.05.119
• Languages: English
• ISSNs: 1359-4311

Abstract

Highlights: The performance of non-Newtonian fluid in a novel heat exchanger was investigated. Different helix angles and helical aspect ratios were studied numerically. The best helix angle and helical aspect ratio were proposed. Abstract: In this paper, the heat transfer and flow performance of the non-Newtonian fluid on the shell side of heat exchanger combined with elliptic tubes and helical baffles were numerically investigated, different helix angles and helical aspect ratios were studied to improve the heat exchanger's overall performance. An aqueous solution with 3.0% weight fraction of carboxymethyl cellulose (CMC) was selected as the working fluid, which was a kind of non-Newtonian fluid with low viscosity and good stability. The results showed that the increasing aspect ratio improve the heat transfer, but also lead to higher pressure drop. The heat exchanger with aspect ratio between 2.5 and 3.0 has the best heat transfer and flow performance. For the helical angle, both the heat transfer rate and pressure drop increase with the smaller angle . Thermal performance factor (TPF) is taken to evaluate the comprehensive performance, the result showed that when helical angle is 40°, both the TPF and the heat transfer coefficient per pressure drop h o ·Δ P o −1 get the most satisfying value.