Convective Heat Transfer in a Helical Coil Solar Thermal Collector

Author(s):  
Allan May ◽  
Tadhg S. O’Donovan

Three dimensional solar concentrators can achieve concentration ratios in excess of 100 and optical efficiencies in excess of 95% throughout the day without the need for tracking. A helical coil heat exchanger has been designed and investigated numerically as the receiver for this solar thermal application. A computational fluid dynamics (CFD) model of a laminar flow in the heat exchanger was developed in ANSYS CFX and a uniform wall flux boundary condition applied to the outer surface. Due to the curvature of the pipe, Dean Vortices were setup within the flow that substantially increased the overall heat transfer to the solar receiver without significantly increasing the pressure drop across the heat exchanger. A full parametric study is conducted to investigate the effects of geometric properties (dimensionless pitch, coil radius etc) and flow variables (Reynolds number, Dean number, Helical number). The variation of the circumferentially averaged heat transfer coefficient with distance along the heat exchanger is reported. It has been shown that the flow is fully developed after approximately 3.5 turns of the heat exchanger coil and will remain stable throughout the remainder of the heat exchanger.

Author(s):  
Qasim Saleh Mahdi ◽  
Sahar A. Fattah ◽  
Firas Juma

Experimental investigation of heat transfer enhancement in heat transfer coefficient of shell and helical coil tube heat exchanger with and without addition nanofluid is carried out in the present work. Experimental work is included two parts: the first one is included design of helical coil heat exchanger with optimum curvature ratio (17), an optimum helical coil pitch has been used to study the heat transfer coefficient without nanofluid. The second part is included studying the effect of using (Oxide Titanium TiO2) nanoparticle powder with 20 nm diameter is dispersed in distilled water with different volume concentrations (0.2, 0.4, 0.6, and 0.8) % by volume on heat transfer coefficient. The experimental results showed that, when nanofluid was used there is an increase in heat transfer coefficient and thermal conductivity by (20) %. An empirical correlation has been found to show the variation of Nusselt number with Dean number by using nano fluid with error of (±5%).


Author(s):  
A.A. Aleksandrov ◽  
I.V. Barmin ◽  
S.K. Pavlov ◽  
V.V. Chugunkov

The paper focuses on hydrocarbon fuel cooling in launch vehicles, specifically considering experimental technique and results obtained during investigation of one of the primary heat exchanger parameters, that is, heat transfer coefficient of the heat exchanger surface. We present a model of efficient hydrocarbon fuel cooling by means of intensifying heat transfer on the external heat exchanger surface due to nitrogen sparging causing active motion in the liquid heat carrier. We obtained quantitative data regarding heat transfer on the external surface of a helical-coil heat exchanger located in a two-phase medium consisting of antifreeze and nitrogen, in the temperature range of 243--293 K. We derived a similarity equation for calculating heat transfer coefficient on the external heat exchanger surface, which is required to determine the heat exchanger surface area and to compute heat transfer from hydrocarbon fuel to the two-phase medium consisting of antifreeze and nitroge.


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