Experimental investigation on performances of trisection helical baffled heat exchangers for oil/water–water heat transfer

• Published in: Energy conversion and management Vol. 101; pp. 460 - 469
• Main Authors: Chen, Ya-Ping, Wang, Wei-han, Wu, Jia-Feng, Dong, Cong
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 01.09.2015
• Subjects: Baffles; Circumferential overlap of baffles; Fluid dynamics; Fluid flow; Heat exchangers; Heat transfer coefficients; Heat transfer enhancement; Helical; Helical baffled heat exchangers; Incline angle of baffle; Performance experiments; Pressure drop; Tubes; Heat transfer enhancement; Helical baffled heat exchangers; Performance experiments; Incline angle of baffle; Circumferential overlap of baffles
• ISSN: 0196-8904; 1879-2227
• DOI: 10.1016/j.enconman.2015.05.042

•Oil/water–water heat transfer performance tests of different schemes were conducted.•12–28° incline angled helical baffle heat exchangers and segment one were studied.•Smaller incline angle is, higher are the shell side ho, Δpo and comprehensive index.•Both ho and ho/Δpo of 12° helical scheme are 50% higher than those of segment one.•Correlations formulae of shell side Nuo and Euzo for cothSTHXs are presented. The trisection helical baffled shell-and-tube heat exchangers have structural features of more suitable to the equilateral triangular tube layouts and less baffle parts. In particular the circumferential overlap trisection helical baffled shell-and-tube heat exchangers are of anti-shortcut structure that accommodates one row tubes in each circumferential overlapped zone between adjacent baffles for dampening shortcut leakage. The performance tests were conducted on both oil–water and water–water heat transfer in heat exchangers with equilateral triangle tube layout of 16 tubes including five helical baffle schemes with incline angles of 12°, 16°, 20°, 24°, 28° and a segmental baffled one for comparison. The test results show that both the shell side heat transfer coefficient ho and pressure drop Δpo increase but the comprehensive index ho/Δpo decreases with the increase of the mass flow rate of all schemes; and that the shell side heat transfer coefficient, pressure drop and the comprehensive index ho/Δpo decrease with the increase of the baffle incline angle at certain mass flow rate, except that the curves of comprehensive index ho/Δpo of 12° and 16° helical baffle schemes are almost coincide. The average values of shell side heat transfer coefficient, the comprehensive index ho/Δpo of the 12° helical baffled scheme are about 50% higher than those of the segmental one with almost same pressure drop. The correlation equations for shell side Nusselt number and axial Euler number are presented varying with axial Reynolds number, Prandtl number and helical baffle incline angle.