Thermodynamic performance of a novel shell-and-tube heat exchanger incorporating paraffin as thermal storage solution for domestic and commercial applications

•Experimental thermal evaluation of paraffin in novel shell-and-tube heat exchanger.•Longitudinal fins supplements the impact of natural convection on phase transition.•Phase front propagations of paraffin in shell container are turbulent in nature.•Compare to Re, Ste has more pronounced impact on t...

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Veröffentlicht in:Applied thermal engineering 2019-09, Vol.160, p.114007, Article 114007
Hauptverfasser: Khan, Zakir, Khan, Zulfiqar Ahmad
Format: Artikel
Sprache:eng
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Zusammenfassung:•Experimental thermal evaluation of paraffin in novel shell-and-tube heat exchanger.•Longitudinal fins supplements the impact of natural convection on phase transition.•Phase front propagations of paraffin in shell container are turbulent in nature.•Compare to Re, Ste has more pronounced impact on thermal performance enhancement.•ε¯-NTU correlations capacitate inlet operating conditions of HTF and desirable PCM. This article is focused to evaluate thermal performance of commercial grade paraffin in a novel shell-and-tube heat exchanger with multi-tube passes and longitudinal fins as latent heat storage (LHS) system. Thermal performance assessments of latent heat storage system are conducted with respects to charging/discharging power, accumulative thermal energy storage/retrieval, thermal efficiencies and effectiveness, heat transfer characterisation and nature of melt front propagation. The average charging and discharging powers are significantly enhanced by 75.53% and 27.04% with an increase in temperature gradient between paraffin and inlet water from 52 °C to 62 °C and 15 °C–5 °C, respectively. Likewise, the maximum charging and discharging powers are augmented from 2.15 kW to 2.63 kW and 5.18–10.37 kW with an increase in flow rate from 1.5 to 3 l/min, respectively. Furthermore, the average effectiveness, Nu-Ra and heat transfer coefficient are significantly improved with an increase in temperature gradient and moderately reduced with upgrading volume flow rate. The range of Rayleigh numbers for charging cycles have indicated turbulent nature of melt front movement and supportive behaviour of longitudinal fins orientations towards natural convection. Empirical correlations for average effectiveness and Nu-Ra are developed from experimental results to facilitate design estimation for employment of proposed LHS systems in domestic and commercial applications. These empirical correlations, to evaluate feasibility and employability of LHS systems in practical applications such as domestic hot water supply and space heating to maintain control room temperature, have been successfully implemented in real operating conditions.
ISSN:1359-4311
1873-5606
DOI:10.1016/j.applthermaleng.2019.114007