Open AccessExperimental study on heat transfer characteristics of annular flow between vertical concentric pipe
Author(s) -
Zeyu Tao,
G.S. Jia,
Xiangzhao Meng,
L.Y. Zhang,
John C. Chai
Publication year - 2019
Publication title -
iop conference series. earth and environmental science
Language(s) - English
Resource type - Journals
eISSN - 1755-1307
pISSN - 1755-1315
DOI - 10.1088/1755-1315/268/1/012014
Subject(s) - nusselt number , heat transfer , mechanics , concentric tube heat exchanger , concentric , micro heat exchanger , dynamic scraped surface heat exchanger , heat exchanger , convective heat transfer , reynolds number , materials science , heat transfer coefficient , thermodynamics , fin , critical heat flux , geometry , turbulence , physics , composite material , mathematics
Concentric pipe heat exchangers have been utilized extensively in practical project, such as petroleum, chemical, geothermal energy utilization and other fields. The study of annular flow between vertical concentric pipes is dominated by boiling heat transfer, while the study of forced convection heat transfer for single-phase flow is scarce. In this paper, an experimental investigation is carried out to study of the flow and heat transfer characteristics of the annular flow between vertical concentric pipes. The annular in a vertical concentric pipe heat exchanger with 25mm ring gap is tested with different volume flow rates and different constant heat flow densities. The results show that the Nusselt number of annular flow between vertical concentric pipes increases with Reynolds number. The local convective heat transfer coefficients reduce with the distance from the top to the bottom, which lead to a gradually increased trend in the fluid temperature along the flow direction. Based on the experimental data, an empirical equation of the Nusselt number is obtained to evaluate the overall heat transfer performance of vertically concentric pipe heat exchangers.