2016
DOI: 10.1016/j.ijthermalsci.2016.04.010
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Prediction of heat transfer coefficients of shell and coiled tube heat exchangers using numerical method and experimental validation

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Cited by 89 publications
(16 citation statements)
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“…In 2016 Ashkan Alimoradi et al [19] have proposed that the heat transfer of shell and helically coiled tube heat exchangers. To investigate the effect of physical properties of fluid, operational, and geometrical parameters, numerical and experimental methods were used on Nusselt numbers of both sides.…”
Section: Literature Reviewmentioning
confidence: 99%
“…In 2016 Ashkan Alimoradi et al [19] have proposed that the heat transfer of shell and helically coiled tube heat exchangers. To investigate the effect of physical properties of fluid, operational, and geometrical parameters, numerical and experimental methods were used on Nusselt numbers of both sides.…”
Section: Literature Reviewmentioning
confidence: 99%
“…With the condenser pressure and fluid composition determined, the cycle can then be analysed using the real world climate data provided, according to well-established thermodynamic techniques [19,38]. The pinch point temperature in the evaporator is taken to be 5 • C as before, and a further 5 • C of superheat is added at the expander inlet to ensure a pure vapour with no droplets is fed into the expander, allowing the evaporator pressure to be calculated using the equations T 3 = T heat source − 5 and P evap = P sat at (T = T 3 − 5).…”
Section: Numerical Modellingmentioning
confidence: 99%
“…The Nusselt number is the ratio of total to conductive heat transfer in a fluid, and is generally calculated for each case using empirical correlations to experimental data. Alimoradi and Veysi [38] give a rough correlation for the Nusselt number in a shell-and tube heat exchanger of: (20) where Re is the Reynolds Number and Pr is the Prandtl Number of the fluid:…”
Section: Numerical Modellingmentioning
confidence: 99%
“…A few investigations on finless heat exchangers were carried out in order to find Nusselt number of shell side [39]. A few relationships were derived by Alimoradi et al [40], to estimate the Nusselt number of these sort of heat exchanger. According to the literature review, by using size and volume fraction of solid phase in addition to temperature accurate predictive models are achievable for a single nanofluid [41][42][43][44][45].…”
Section: Introductionmentioning
confidence: 99%