Three-Dimensional Thermocline Dynamics In Thermal Storage Tanks

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Journal of Applied Fluid Mechanics, Vol. 14, No. 5, pp. 1483-1495, 2021.Available online at www.jafmonline.net, ISSN 1735-3572, EISSN 9Three-Dimensional Thermocline Dynamics in ThermalStorage TanksS. S. Ratnu and K. V. Manu†Department of Aerospace Engineering, Indian Institute of Space Science and Technology,Thiruvananthapuram, 695547, Kerala, India†Corresponding Author Email: manukv@iist.ac.in(Received August 28, 2020; accepted March 14, 2021)ABSTRACTIn this work, a series of three-dimensional unsteady numerical simulations are performed to study the stabilityand interface dynamics of a thermocline-based lab-scale single tank Thermal Energy Storage system (TES).The stability of thermocline is analysed by introducing relatively cold fluid for a short period at the inlet of theTES. Numerical simulations are performed for three inlet flow disturbances (weak, medium and strong) andthree stratification levels (sharp, moderate and large). The fluid injected at the inlet rolls-up and interacts withthe thermocline which causes spatio-temporal disruption of the stable stratification inside the TES. It was foundthat the three-dimensional simulations bear some resemblance to the two-dimensional case but also showcrucial differences. The propagation of the injected cold fluid and the subsequent interaction with thethermocline are analysed. A wide gamut of flow structures is identified inside the TES depending on the degreeof stratification and level of disturbance. Finally, the oscillatory nature of interface and associated mixingmechanism are addressed. The simulation indicates that the oscillations at the interface are through thesuccessive generation of countersign vorticity which retards/suppresses the propagation of the vortex ring. Inthe case of large interface, internal waves are generated by the periodic array of vortices which generates astanding wave pattern near the Brunt-Vä isä lä frequency.Keywords: Stratified storage system; Vorticity dynamics; Baroclinicity; Buoyancy frequency.NOMENCLATUREACpatwood numberspecific heatDpdiameter of the tankpressureheight of the tankradial distance from center of piperadius of the pipethermal conductivitybuoyancy frequencyReynolds numberRichardson numbertemperaturehrRkNReRiT1.tVx flow Timeaxial component of velocityaxial distance of the pipethermocline thicknesscirculationkinematic viscositydensity of the fluidnon-dimensional time scale for starting flows SubscriptchdINTRODUCTIONConcentrated solar power (CSP) systems areaffordable, eco-friendly energy technology for largescale conversion of solar energy to electricity. CSPsystems can generate uninterrupted electricity ondemand through the efficient use of thermal energycold-fluid propertieshot-fluid propertiesdisturbance fluid propertiesstorage systems (Medrano et al. 2010; Gil et al.2010). It has been identified that the cost of storagesystems can be minimized up to 35% by storing thehot and cold fluid in a single-tank system in stratifiedconfiguration (Yang and Garimella 2010; Kearney etal. 2003). However, maintaining a stablestratification under various operating conditions isone of the major challenges associated with single

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 1. Schematic of thermocline storage concept.tank TES. The implementation of molten tank basedsingle tank TES system and associated strategies arediscussed in the recent experimental works of Yuanet al. (2018) and Advaith et al. (2021).dimensional simulations. They have observedKelvin- Helmholtz-like waves in the threedimensional simulations.For high temperature CSP applications, molten salt,(a eutectic mixture of sodium and potassium nitrate)are commonly employed as heat transfer fluid (HTF)(Reddy 2011). Compared with other organic HTF,molten salt allows wider working temperature range,efficient thermal stability and relatively low vaporpressure. Recently, a series of two-dimensionalComputational Fluid Dynamics (CFD) studies wereconducted to study the impact of varioushydrodynamic instabilities and associated mixing ina molten salt based lab-scale TES (Manu et al. 2015;Manu et al. 2016; Hatte et al. 2016; Tinaikar et al.2016). Characteristic flow features of RayleighTaylor (RT) instabilities such as bubble and spikelike structures are observed in the numericalsimulations of Manu et al. (2016). The effects ofAtwood number and Froude number on thethermocline mixing dynamics induced by RTinstabilities are analysed by Manu et al. (2015). Thetransient nature of thermocline under subsequentcyclic chargingdischarging are analysed by Hatte etal. (2016). In an interesting work, Tinaikar et al.(2016) experimentally and numerically analysed themixing dynamics induced by successive laminarvortex pairs. Tinaikar et al. (2016) observed that theflow features of thermocline under externalperturbations are analogous to the vortexstratifiedinterface interactions experiments (Linden 1973;Dahm et al. 1989; Orlandi et al. 1998).In a single tank thermocline storage system the lessdense hot-fluid is stored above the denser cold fluidin stratified configuration (Fig. 1). A completestorage process in a single tank TES involves mainlythree process: charging, storing and discharging.During the charging process, hot fluid from the solarcollection field enters into the tank from the top andforces out the existing cold fluid from the bottom ofthe tank (Fig. 1), while during the dischargingprocess, hot fluid from the top, pumps to the powerblock to generate electricity and re-enters from thebottom at a comparatively less temperature. Theseprocesses cause heat exchange between hot and coldof the fluid resulting the formation of hightemperature gradient region known as ‘thermocline’.Theoretically, in a TES, the hot fluid sits at the tophalf while the cold fluid positioned at the bottom-halfof the tank. Extensive review regarding the workingand performance of molten salt based TES can befound in Gonzá lez- Roubaud et al. (2017) and Sureshand Saini (2020).Different heat and mass transfer phenomena thatoccur in a TES can have an adverse effect on thermalstratification (Qin et al. 2012). For example, duringthe charging process, relatively cold fluid can enterthe TES due to the diurnal variation of solarradiation. This can cause distortion of thermalstratification and undesirable mixing of hot and coldfluid inside the TES. The entrainment of cold fluidinto hot fluid can cause an increase in thethermocline thickness thereby affecting thestratification efficiency. Quantitative comparison ofinstabilities that occurred in two dimensional andthree dimensional simulations are performed by VanBerkel et al. (2002) in a thermocline based waterstorage tank. In two-dimensional simulations theentrainment velocity was 40% higher than that foundin the corresponding three dimensional simulations.Also, a higher level of internal waves and morekinetic energy is present at large scales in two-Dahm et al. (1989) posited that for thin interfaces,barocliinc production and topology of the vorticesformed at the interface are governed by Atwoodnumber and vorticity-based Froude number.However, in case of thick interface , the interactionmechanism and associated mixing are governed bythickness of the interface, distance between thevortices, Atwood number and Froude number.Recently, Advaith et al. (2017) conductedexperiments on the interaction of vortex ring with afinite thickness stratified interface mimicking thethermocline-disturbance interaction observed in1484

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.TES. They have classified vortex ring interfacemechanism into three regimes (non-penetrative,partially penetrative and extensively penetrative)based on maximum penetration length. Theimportance of three dimensional effects are revealedthe from the recent time-resolved stereoscopicParticle Image Velocimetry (stereo PIV)measurements of Olsthoorn and Dalziel (2017). Theyhave observed that the time scale associated with theinstability growth decreases with increasingRichardson number. The effect of Pclet and theAtwood number on thermal stratification is reportedby Shaikh et al. (2018).Fig. 2. Schematic of computational domain andboundary conditions:(a) three dimensional view; (b) two-dimensionalcross sectional view.In this work the stability of a molten salt based singleTES is analysed for different flow configurationsusing CFD. The results are presented using importantnon-dimensional numbers. Hence the reportedresults can be easily ported to other types of storageas well. The goal of this work is to gain insight intothe three dimensional transient dynamics of thethermocline and its stability which are consistentwith the practical conditions. The effects ofthermocline thickness on various flow features havebeen studied in detail.The governing equations are:This paper is organized as follows. The details ofgoverning equations, boundary and initial conditionsused for the present study are provided in sections2.1 and 2.2. A grid independence analysis is given insection 2.3. In section 3, the flow physics behind themixing mechanism have been analysed for nine flowconditions. Initially, the initial development of threetypes of disturbances is analysed (section 3.1). Theinterface mechanisms between a weak disturbancewith sharp, moderate and large interface thicknesslevels are analysed in section 3.21. The interactionbetween a medium disturbance with sharp, moderateand large interface thickness levels are analysed insection 3.22. In section 3.23, the interaction betweena strong disturbance with with sharp, moderate andlarge interface thickness levels are analysed. Finally,oscillatory nature of he interface associated withbaroclinic production of vorticity is analysed insection 3.3. The results are summarized in section 4. ( v ) 0 t(1) ( v ) ( vv ) p ( ) g t(2) ( E ) (v ( E p)) (k T ) t(3) ()2 v v T . VI 3 WhereE h p FLUENT implements the SIMPLE algorithm forsolving the Navier-Stokes equations for variabledensity flow. Spatial discretization of the convectivefluxes is performed with a second-order upwindscheme. Body-force weighted scheme for pressurediscretization was used to incorporate gravitationalforce terms and second order implicit scheme usedfor transient terms. The scaled absolute values of theresiduals, for velocities and temperature, were set to10 5 as convergence criteria for each time step.Under-relaxation factor of 0.3 and 0.7 were selectedfor pressure and momentum respectively. The time2. NUMERICAL METHODOLOGYTES is modelled as a cylindrical three-dimensionaldomain of diameter (D) 150 mm and height(h) 500mm. The aspect ratio(h/d) for lab scale geometryused is 3.34, which is the comparable with that usedin industrial applications. The schematic ofcomputational domains with boundary conditions areshown in Figure 2. Here, x and z coordinatescorrespond to radial directions and y coordinatecorrespond to axial direction. Velocity in radial, axialdirections are represented by u and v respectively.The properties of hot, cold and disturbance fluids aredenoted by sub-scripts h, c and d respectively. Thegrid was generated by Pointwise V18R3.step used for the simulations is t 2 10 3 s sov tthat the CFL number () was kept below 0.1 for xall the simulations. Molten salt (HITEC salt) withfollowing thermo-physical properties Xu et al. 2012was used as the HTF2.1 Governing equations (T ) 2090 0.636T ( C)(4)C p (T ) 1443 0.172T ( * C )(5)k(T) 0.443 0.00019 T(C)(6)[ (T ) 22.714 0.12T 2.281 10 4 T 2A commercially available program ANSYSFLUENT 16.2 was used for solving transient threedimensional mass, momentum and energyconservation equation. 7 3 1.474 10 T1485] 10 3(C)(7)

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021. 0.079 0 t 0.25 sVd t 0.25 s 02.2 Initial and boundary conditionsThe velocity boundary condition is applied at theinlet and the outlet of the TES as in the twodimensional simulations of (Tinaikar et al. 2016).Adiabatic thermal condition is applied for the storagetank walls by setting a zero heat flux at the wallsurface. At side walls, top plane and bottom plane(except inlet and outlet of domains) no-slip andadiabatic conditions are assigned. 610 KTd 651K0s t 0.25 st 0.25 s(9)(10)The disturbance velocity and temperature at inlet areas follow; for medium disturbance: 0.079 0s t 0.50 sVd t 0.50 s 0 610 KTd 6510s t 0.50 st 0.50 s(11)(12)The disturbance velocity and temperature at inlet areas follows; for strong disturbance: 0.079 0 s t 0.75 sVd t 0.75 s 0 610 KTd 6510s t 0.75 st 0.75 s(13)(14)The following definitions are used to define Atwoodnumber ( A ), Reynolds number(Re) and circulationbased Reynolds number.A Fig. 3. Non-dimensional temperature profileprofile (sigmoid function). c h c h(15) dVd d(16) 2 (17)Re Temperature profile is initialized by the followingsigmoid profile as shown in Fig. 3. This distributionof temperature at the end of the charging process canbe represented by the sigmoid profile as shown invarious studies (Zachar et al. 2003; Flueckiger et al.2013).T Tc Th Tc1 e m( y n)Rev Here, is the circulation strength.Here, in Eq. 16 the diameter of the pipe is selectedas one of the length scales to define Reynoldsnumber asduring in many vortex-ring-inducedstratified mixing studies Shy (1995), Olsthoorn andDalziel (2017). However, in the present case, theinlet flow is discontinuous as evident in Eq. 9. Hencea better way to calculate the ratio of inertia andviscous force is to use circulation-based Reynoldsnumber which is used in vorticity dominated flows.This alternate definition allows us to include theeffect of flow duration as shown in many otherexperimental and numerical works Dahm et al.(1989), Orlandi et al. (1998). The followingdefinitions are used to define Richardson number,Richardson number based of circulation and Froudenumber.(8)Here, m represents the shape parameter whichdetermines the thermocline thickness and ndesignates the axial location of the thermocline. Thethickness of thermocline calculated using thefollowing expression Th TcHere, Th is the lowest y value at which thetemperature reached 0.99 Th and Th is the largestvalue at which the temperature attains a value of 1.01Tc . Here, the values of Th and Tc are 651K and563K. Disturbances were introduced by adding thecolder fluid at inlet through a port with a 7.5 mm( d ) with Velocity Vd and temperature Td into thestable thermocline which is maintained at the centerof the tank. The temperature ( Td 610 ) hastemperature higher than cold fluid temperature andlower than hot fluid temperature( Tc Td Th ).Ri g ( c h )d hVd2Riv AR(18)(19)where, R a3 g / 2Fr The disturbance velocity and temperature at inlet areas follows; for weak disturbance:1486VdNd(20)

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Table 1 Simulation details.Caseτd(s)ReRiδ/hARRiv 20.068915.4510.581where, N and 0 g ( y ) 0 y3. RESULTSThe two-dimensional view of the instantaneous non T Tc dimensional temperature plots T * atTh Tc variousnon-dimensionalized timeinstance* tVd(t ) of weak disturbance cases (SC1, MC1hand LC1) are shown in Figs. 5 (a), (b) and (c). Theevolution of the flow disturbance inside the TEShappens in three distinct phases: the initial roll-up,vortex-thermocline interaction and recovery phase.During the initial phase, the added disturbance fluid h c2Here, a is the distance between two vortex centre.The non-dimensional numbers along with otherparameters are tabulated in table 1.2.3. Mesh Independent AnalysisA mesh independent analysis is conducted todetermine the optimum grid to capture the flowphysics. Initially, three types of meshes of sizes254 600 254 (Fine mesh), 127 300 127(medium mesh) and 64 150 64 (coarse mesh)were considered for the simulations. Figure 4 showsthe effect of grid resolution on temperature atrolls- up near the inlet port region ( t * 0.47 ). Theinterface is unaffected by the added perturbationduring the initial phase. Subsequently, in the secondphase ( 0.47 t * 1.89 ) the rolled up flow structurepenetrates the lighter hot-fluid and impinges on thethermocline region.t * 0.47 . The difference between fine grid andmedium grid is negligible. Here, the maximumdifference in velocity and temperature are 1.2\% and3.00\% respectively. Hence to reduce computationalcost and time, grid 127 300 127 (medium mesh)is considered for further simulations.Depending upon the interface thickness and strengthof the disturbance, a wide gamut of flow patterns areformed near the thermocline region. This interactionmechanisms are analogous to the vortex ring- densityinteraction interaction experiments of (Linden1973;Dahm et al. 1989; Orlandi et al. 1998; Advaithet al. 2017) and various two dimensional simulations(Manu et al. 2015; Manu et al. 2016;Tinaikar et al.2016).Unfortunately, to our knowledge noexperimental data is available for direct comparisonwith Molten salt based TES.In Fig. 6 the numerical simulations results arecompared with the visualization experiments of(Dahm et al. 1989). As shown in the Fig.6 for similarAR value ( AR 0.1 ) the flow features are similarwith the the experimental observations of (Dahm etal. 1989). This interaction causes oscillation ofthermocline region. Finally, during the recoveryphase ( t * 1.89 ), thermocline oscillations areobserved and a new thermocline with increasedthickness is established.Fig. 4. Mesh independent analysis.1487

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 5. Temperature contour at different flow instances; case SC1.ring detachment phenomena was not observed asdepicted in Fig.7 (c). In this case, the disturbancefluid propagates as a jet-like structure rather than avortex ring as observed in the other two cases.A close up view of the vortex ring structure formednear the inlet port is shown in Fig. 8. The vortex ringdisplays as a vortex pair in the side view as observedin the two-dimensional simulations. The downwardpropagating vortex ring interacts with thermoclinewhich is kept at the center of the TES.Fig. 6. Qualitative comparison with theexperiments of Dahm et al.3.2 Second phase: Impingement of coherentstructures3. 1 First Phase: Vortex formationIn order to effectively understand the vortex ringthermocline interaction mechanism, the collision ofthe coherent structures with three differentstratification levels (different thermocline thickness)are systematically analysed.The initial development of three-dimensional vortexstructures for three opening duration at various nondimensionalized time instance ( t * tVd / h ) isdepicted in fig.7. Soon after the injection, therelatively cold fluid rolls-up and coherent vorticalstructures are formed near the inlet section. Theevolution of three types of disturbances are analysed v uby plotting the contour of z vortcity ( z ) x yas shown in Fig.7.3. 2. 1 Evolution of weak disturbanceThe interface dynamics of weak disturbance withsharp, moderate and large interface are depicted inFig.9. The injected vortex ring propagates towardsthe thermocline and touches the upper layer ofthermocline at t * 1.42 . In case of sharp interface(SC1) the vortex ring barely penetrates the upperlayer of the thermocline (Fig. 9 (a)). In this case thevortex ring thermocline interaction is analogous tovortex ring-wall interactions. With increase in flowtime, the vortex ring spreads in the radial directionsas shown in Fig. 9 (b).In case of relatively short opening duration, (weak disturbance) two isolated vortex rings are formed asshown in Fig. 7 (a). For medium disturbances, a shorttail is formed behind the downward propagatingprimary vortex ring Fig. 7 (b). In case of largeopening duration, (strong disturbance) the vortex1488

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 7. Vorticity iso-surfaces at selected time instant ( z 1.5s -1 ).Fig. 8. Vortex ring (a) Isometric view, (b) Front View, (c) side view d) top view.In the case of moderate interface, (MC1) the vortexring partially penetrate the interface as shown inFigs. 9 (c) and (d).Here, a part of the vortex ring penetrates through thethermocline while the remainder recoils upwardforming a plume structure (Figs. 9(e) and (f)) as inthe experimental study of Advaith et al. (2017).Subsequently, the vortex ring shrinks in size andfinally diffuses in the interface region. At later flowtime, after a few rebounds, a new thermocline isestablished with increased thickness.In the case of large interface, (LC1) the vortex ringpenetrates into thermocline cause oscillations inaxial and radial directions. Baroclinic production ofopposite signed vortices are observed in this case.1489

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 9. Iso-surfaces of vorticity at two time instance: (a), (b) sharp interface; (c), (d) moderate interface;(e) and (f) large interface.Fig. 10. Temperature and Velocity profile at center line at selected time instant a)T (y) for sharpinterface b)v (y) for sharp interface c)T (y) for medium interface d)v (y) for medium interface e)T (y)for strong interface f)v (y) for strong interface.Figure 10 shows the variation of temperature andvelocity in axial direction at four time instants (at thecenter of the tank). The propagation of weakdisturbance in the axial direction are evident in thetemperature and velocity plots (Figs. 10 (a) and (b)respectively).the disturbance propagates downstream which altersthe temperature and velocity profiles. Here, in thecase of sharp interface, the disturbance is not strongto penetrate the top part of the interface. This isevident in the velocity profile graphs Fig. 10 (b). Theaxial profiles of temperature and velocity formoderate interface thickness case (MC1) are shownin Fig. 10 (c) and (d) respectively. Due to the additionof flow perturbations, the temperature profiles areinitially distorted near the inlet and this distortionmigrates downwards with increase in flow time.Distortions inside the thermocline region are evidentThe upper part of of the sigmoid profile is distortedby the flow disturbance. During initial stages(t * 0.23) the bulk of the inserted cold fluid(formed coherent structure) is at the top part of TES(0.8 h* 1) which causes inflections intemperature and velocity profiles. At later flow timein this case ( t * 1.9 ).1490

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 11. Iso-surfaces of vorticity (ωz 1.5s 1) at two time instance (a) sharp interface, (b) Mediuminterface, (c) Large interface.The velocity profiles (Fig.10 (d)) are qualitativelysimilar to SC1 case. In the case of large interface(LC1), some difference in the interaction mechanismare evident in the temperature and axial velocityprofiles (Figs.10 (e) and (f)). Inflections inside thethermocline regions are observed in the case of largeinterface thickness (Fig. 10(e)). Positive values ofaxial velocity are observed in this case. This isrelated to the upward propagation of baroclinicallygenerated plume- like structures.profiles are quantitatively similar to weakdisturbance cases as shown in Fig. 12 (d)). In the caseof large interface thickness, the sigmoid profile issignificantly disturbed by the impingement ofvertical structure as shown in Fig. 12 (e)). Here, thecomplex interactions inside the thermocline createsmultiple inflectional points in the velocity profiles(Fig. 12 (f)).3. 2. 2 Evolution of medium disturbanceHere, the outer surface removal of the jet-likestructure is reminiscent to the banana peeling processas observed in experimental study of Shy (1995).Typical interface dynamics of medium disturbancewith sharp, moderate and large interface are shownin Fig. 11. In the case of medium disturbances (SC2,MC2 and LC2) the interface dynamics isAnother important aspect of strong disturbance is theoscillations observed during the recovery phase (postimpingement period) which will be discussed in thesection 3.4.complicated by the tail of the coherent structures. ForSc2 (sharp interface case), the vortex ring hardlypenetrates and the interface remains flat after theimpingement as shown in Fig. 11 (a). At later flowtime, the disturbance propagates in the radialdirection (Fig. 11 (b)). In the case of moderateinterface thickness (MC2), multiple small scalestructures are observed to orbit around the primaryvortex ring near the interface as region as shown inFigs. 11 (c) and (d). Here, the spreading of thevorticity in the radial direction is less compared withSC2. In the case of large interface (LC2), the vortexring -thermocline interaction creates a crater insidethe thermocline region as shown in Fig. 11 (e) . Thecold fluid stored in bottom half splashes upwardsbecause of this interaction. Complex small scalestructures are formed in the interface region due tothe baroclinc generation of vorticity (Fig. 11 (f)).Vorticity contour of strong disturbance with differentinterfaces are shown in Fig. 13. The temperatureprofiles shows negligible penetration for SC3 case(Fig. 14 (a)). For SC3 case increase in magnitude ofvelocity component is associated increase in theduration of flow disturbance (Fig. 14 (b)). Upwardpropagation of vortical structures are observed in theinterface region for all the cases as evidenced in Figs.14 (b) (d) and (f). In the case of moderate and largeinterface thickness (MC3 and LC3) a significantalteration in the sigmoid profiles are observed duringthe interaction period (Figs. 14 (c) and (e)).3. 3 Third phase: Thermocline oscillations andSpectraDuring the post-impingement period (recoveryphase), continuous damping oscillations ofthermocline are observed in the simulation.Thermocline oscillations are observed for all thesimulation cases. However, the amplitude ofoscillations is highest for strong disturbances cases.In the case of moderate interface thickness, thepartial penetration of disturbance is evident in thetemperature profiles (Fig. 12 (c)). The velocity1491

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 12. Temperature and Velocity profile at center line at selected time instant (a) T (y) for sharpinterface, (b)v (y) for sharp interface, (c) T (y) for medium interface, (d) v (y) for medium interface,(e) T (y) for strong.Fig. 13. Iso-surfaces of vorticity(ωz 1.5s 1) at two time instance a) sharp interface b)Mediuminterface c)Large interface.In order to quantify the nature of oscillationstemporal variation of axial and radial velocity and thecorresponding spectra at the center of thethermocline are plotted in Figs. 15 and 16. Here, theamplitude of oscillations decreases with increase inthermocline thickness as shown in Fig. 15. Theobtained peak frequency from the FFT analysisscales with the buoyancy frequency (Brunt-Vä isä läfrequency). Brunt-Vä isä lä frequency is tabulated intable 2.In order to understand the flow dynamics during thethermocline oscillations phase, the vorticity plotduring one cycle is plotted in Fig. 17. Here, thethermocline oscillations near the thermocline regionis connected with the generation of baroclinicvorticity. Figure 17 indicates that the oscillations atthe inferface are through the successive generation ofcountersign vorticity which retards/suppresses thepropagation of the disturbance.1492

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.Fig. 14. Temperature and Velocity profile at center line at selected time instant (a) T (y) for sharpinterface, (b) v (y) for sharp interface, (c)T (y) for medium interface, (d)v (y) for medium interface, (e)T (y) for strong interface, (f) v (y) for strong interface.Fig. 15. Temporal variation of axial velocity and spectra.Fig. 16. Temporal variation of radial velocity and spectra.1493

S. S. Ratnu and K. V. Manu / JAFM, Vol. 14, No. 5, pp. 1483-1495, 2021.REFERENCESAdvaith, S., K. Manu, A. Tinaikar, U. K. Chetia andS. Basu (2017). Interaction of vortex ring witha stratified finite thickness interface. Physics ofFluids 29(9), 093602.Advaith, S., D. R. Parida, K. Aswathi, N. Dani, U. K.Chetia, K. Chattopadhyay and S. Basu (2021).Experimental investigation on single-mediumstratified thermal energy storage system.Renewable Energy 164, 146–155.Fig. 17. Vorticity production at the interface.Table 2 Parameters of under- dampedoscillations induced by flow disturbance at r* 0,h* 0.5CaseBrunt-V𝑎̈ is𝑎̈ l𝑎̈ frequencyPeak hm, W., C. Scheil and G. Tryggvason (1989).Dynamics of vortex interaction with a densityinterface. Journal of Fluid Mechanics 205, 1–43.Flueckiger, S. M., Z. Yang and S. V. Garimella(2013). Review of molten-salt thermocline tankmodeling for solar thermal energy storage. HeatTransfer Engineering 34(10), 787–800.Gil, A., M. Medrano, I. Martorell, A. Lázaro, P.Dolado, B. Zalba and L. F. Cabeza (2010). Stateof the art on high temperature thermal energystorage for power generation. part 1concepts,materials and modellization. Renewable andSustainable Energy Reviews 14(1), 31–55.For large interface case the internal waves aregenerated by the periodic array of vortices whichgenerates a standing wave pattern near the BruntVä isä lä frequency.Gonzál

instabilities that occurred in two dimensional and three dimensional simulations are performed by Van Berkel et al. (2002) in a thermocline based water storage tank. In two-dimensional simulations the entrainment velocity was 40% higher than that found in the corresponding three dimensional simulations.

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