2019
DOI: 10.1016/j.applthermaleng.2019.113821
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On the thermal stratification inside a spherical water storage tank during dynamic mode

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Cited by 23 publications
(8 citation statements)
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“…A CFD analysis of Li et al [66] showed that the higher effective discharging efficiency (about 14% in average) could be obtained with the shower-type inlet distributor compared to the simpleinlet case (flow rate ranges from 5 to 15 L min −1 ). Furthermore, the perforated plate design has been widely used as the multi-branch type distributor in the packed-bed TES systems, [20]; (c) perforated plate [67]; (d) incline flat plate [14]; (e) overflow tubular [67]; (f) moving plate [68]; (g) compoundpipe stratifier [69]; (h) porous pipe [70]; (i) perforated tube [71]. Reprinted with permission from refs.…”
Section: Flow Distributormentioning
confidence: 99%
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“…A CFD analysis of Li et al [66] showed that the higher effective discharging efficiency (about 14% in average) could be obtained with the shower-type inlet distributor compared to the simpleinlet case (flow rate ranges from 5 to 15 L min −1 ). Furthermore, the perforated plate design has been widely used as the multi-branch type distributor in the packed-bed TES systems, [20]; (c) perforated plate [67]; (d) incline flat plate [14]; (e) overflow tubular [67]; (f) moving plate [68]; (g) compoundpipe stratifier [69]; (h) porous pipe [70]; (i) perforated tube [71]. Reprinted with permission from refs.…”
Section: Flow Distributormentioning
confidence: 99%
“…The multi-branch type is usually fabricated with the multiple ports to divide the inertial-force-controlled injected flow into many minor streams [51,54,[66][67][68][69][70][71][72]. A CFD analysis of Li et al [66] showed that the higher effective discharging efficiency (about 14% in average) could be obtained with the shower-type inlet distributor compared to the simple-inlet case (flow rate ranges from 5 to 15 L min −1 ).…”
Section: Flow Distributormentioning
confidence: 99%
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“…Without the need for experimental measurements, the CFD method can achieve a more realistic thermal stratification characterization by using high temporal and spatial resolutions. The models for CFD methods can be classified into one‐dimensional (1D) models, 2,16–20 two‐dimensional (2D) models, 21–23 and three‐dimensional (3D) models 24–32 . For the 1D models, energy balance over each control volume is conducted, thus leading to a series of coupled partial differential equations in time and vertical height 20 .…”
Section: Introductionmentioning
confidence: 99%