2018
DOI: 10.1016/j.renene.2017.11.062
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Experimental performance analysis of low concentration ratio solar parabolic trough collectors with nanofluids in winter conditions

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Cited by 127 publications
(39 citation statements)
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“…Rehan et al [51] experimentally studied the effect of Al 2 O 3 and Fe 2 O 3 nanoparticle dispersed in water with different weight fraction ranging from 0.2-0.3% and flow rates (1-2 L/min) on the thermal efficiency of the PTC in winter. It was concluded that at 2 L/min flow rate and 0.3 wt %, Al 2 O 3 /water and Fe 2 O 3 /water nanofluid application enhances the thermal efficiency by 13% and 11%, respectively.…”
Section: Experimental Studiesmentioning
confidence: 99%
“…Rehan et al [51] experimentally studied the effect of Al 2 O 3 and Fe 2 O 3 nanoparticle dispersed in water with different weight fraction ranging from 0.2-0.3% and flow rates (1-2 L/min) on the thermal efficiency of the PTC in winter. It was concluded that at 2 L/min flow rate and 0.3 wt %, Al 2 O 3 /water and Fe 2 O 3 /water nanofluid application enhances the thermal efficiency by 13% and 11%, respectively.…”
Section: Experimental Studiesmentioning
confidence: 99%
“…The usage of Al 2 O 3 and Fe 2 O 3 nanoparticles in water with different concentrations (0.20%, 0.25%, and 0.30%) was recently studied by Rehan et al The authors reported an increase in the thermal efficiency by 13% with Al 2 O 3 and 11% with Fe 2 O 3 mixed with water. Moreover, Subramani et al tested the usage of TiO 2 /water nanofluid in the PTC using different volume fractions (0.05%, 0.10%, and 0.20%).…”
Section: Thermal Performance Improvement By Adding Nanoparticlesmentioning
confidence: 99%
“…Finally, to extend the optical path length of the solar radiation, a coating with a high reflectance is applied on the top‐half surface of the outer tube. For the dual‐nanofluid DAPTSC, the geometrical concentration ratio can be estimated as W /( D 2 + 2 × 3 t g ) ≈ 55, where W is the width of parabolic mirror (see Figure ). We assumed the uniform velocity at the inlet such that the mass flow rate in each tube can be expressed simply as m˙1=f1×truem˙ and m˙2=f2×truem˙, where truem˙ is the total mass flow rate (ie, truem˙=m˙1+m˙2) and f is the fraction of cross‐sectional area of each tube.…”
Section: Theoretical Modelmentioning
confidence: 99%