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Article  |  Open Access  |  30 Jun 2026

Phase change doped sand storage for isothermal thermoelectric heat delivery

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Energy Mater. 2026, 6, 600072.
10.20517/energymater.2026.73 |  © The Author(s) 2026.
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Abstract

Household-scale sand-based thermal energy storage (TES) integrated with thermoelectric generators (TEGs) is constrained by insufficient radial thermal transport, interfacial heat transfer losses, and uncertain cyclic durability. This study addresses all three issues through a finite-element parametric investigation of thirty composite configurations spanning five dopant candidates, three volume fractions, and two spatial architectures. The 30 vol% functionally graded Solar Salt formulation produced a well-defined isothermal plateau near 493 K at the TEG interface, stabilizing the hot-side temperature to within 10 K through a spatially coherent phase-change front. No purely conductive dopant reproduced this temporal stability despite achieving higher peak temperatures. Interfacial analysis revealed that a 0.1 mm thermal interface material layer imposed a 40 K temperature discontinuity comparable to the TEG operating differential. Thermomechanical screening across nine insulation-shell material combinations demonstrated that compatibility among the coefficients of thermal expansion governed long-term reliability, with zirconia paired with Inconel 718 achieving a fatigue safety factor exceeding 2.0 over the 20-year service horizon projected by the power-law ratcheting extrapolation. Furthermore, coupled parametric mapping of interface conductivity and contact pressure identified an optimized design point capable of delivering 82% of the thermal energy to the TEG surface. This interfacial optimization secured a projected thermal interface material (TIM) fatigue life of 6,200 cycles (approximately 17 years) and ultimately yielded an end-to-end electrical efficiency of approximately 5%. These findings establish quantitative design criteria for transitioning sand-based thermal storage to compact household-scale modules.

Keywords

Thermal energy storage, phase change material, thermoelectric generator, interfacial thermal resistance, thermomechanical fatigue, sand battery

INTRODUCTION

The global transition toward renewable energy has intensified the demand for reliable, cost-effective, and safe energy storage technologies. Conventional electrochemical storage, particularly lithium-ion batteries, dominates short-duration applications due to high round-trip efficiency (90%-95%) and energy density (100-250 Wh/kg)[1,2]. However, lithium-ion systems present well-documented limitations for community-scale distributed deployment: unit costs of $250-400/kWh at the cell level[2], thermal runaway risks that necessitate complex monitoring and fire suppression infrastructure[3], reliance on geographically concentrated and environmentally contentious supply chains for lithium and cobalt[4], and cycle-life degradation that typically limits useful service to 3,000-5,000 deep-discharge cycles[1]. These constraints are amplified in the context of off-grid or semi-rural installations, where maintenance expertise is limited and capital recovery timelines must remain short to attract private investment.

Sand-based thermal energy storage (TES) has emerged as an alternative that directly addresses these limitations. The concept stores surplus electrical energy as sensible heat in a packed bed of silicon dioxide (SiO2) via resistive Joule heating, retains the thermal energy in insulated containment, and recovers it through thermoelectric generators (TEGs) at the storage vessel interface. Silica sand is chemically inert at temperatures up to 1,200 °C, available at less than $0.5/kg, and does not degrade under repeated thermal cycling[5,6]. A commercial-scale sand battery (100 MWh) has been operational in Pornainen, Finland since 2024, demonstrating thermal retention losses below 1% per day[7,8]. The U.S. National Renewable Energy Laboratory (NREL) ENDURING project has further validated particle-based thermal storage at laboratory scale, reporting 95% thermal retention efficiency over five days and a round-trip electrical efficiency of 50%-52% for a system designed for 100 h duration[9]. These installations, however, operate at grid scale (10-100 MWh), and the sub-kWh household scale relevant to distributed community energy systems remains largely unexplored. At this scale, a single storage unit can be fabricated from locally sourced materials at a cost below ¥600 per household, and the low thermal mass allows full charge-discharge cycles within a working day, making the format well suited to the intermittent output of human-powered generation. Closing this scale gap therefore carries direct practical relevance for off-grid communities where neither grid infrastructure nor lithium-ion economics are viable[10].

The demonstrated viability at grid scale, however, does not translate directly to the sub-kWh household level, where the surface-area-to-volume ratio favors rapid heat dissipation, the available capital per unit energy is substantially lower, and the absence of centralized maintenance imposes stricter requirements on system simplicity and material durability. Building on this technological foundation, a key unresolved question concerns how such thermal energy storage systems can be meaningfully integrated into highly decentralized, small-scale, and human-centered energy environments. In particular, while existing studies have demonstrated the feasibility of sand-based thermal storage at grid scale, the organizational and socio-technical configurations required for sub-kWh, community-level deployment remain underexplored.

To address this gap, this study introduces the Harmonious Ecovillage (HEV) as a conceptual socio-technical application scenario for integrating human activity, energy storage, and data generation within a localized framework. The HEV is specifically designed to tackle unemployment challenges in the era of general artificial intelligence (GAI) and robotics, using human-powered electricity generation (HPEG) and data generation as guarantee mechanisms for securing basic employment opportunities. Within this framework, residents operate HPEG devices that convert physical activity into intermittent electrical energy. This energy is then buffered through a sand-based thermal storage system and subsequently released in a controlled manner via TEGs, enabling temporal decoupling between energy production and consumption without reliance on electrochemical storage [Figure 1][11]. Figure 1 provides a conceptual overview of this integrated system; energy flows are represented schematically, with a single directional arrow at the TEG interface indicating electricity output.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 1. Schematic of the Harmonious Ecovillage (HEV) hybrid microgrid integrated with an underground sand battery for thermal energy storage. TEG: Thermoelectric generator.

The cycling stations in Figure 1 are the physical HPEG units through which residents convert pedaling work into electrical energy, each feeding the community microgrid before surplus output is routed to the sand battery’s resistive heating element. The annotation “Overall Efficiency: 38% (H2H2P)” refers to the theoretical Carnot efficiency of the Human-to-Heat-to-Power (H2H2P) pathway at the Solar Salt plateau temperature (TH = 493 K, TC = 300 K): ηCarnot = (493 - 300) / 493 ≈ 0.39, which represents the thermodynamic ceiling of the heat-to-power stage rather than the module-level conversion ceiling of roughly 7% to 8%, from which the realized end-to-end electrical efficiency of the system is lower still, on the order of 5% [Table 1].

Table 1

Comparative performance of candidate energy storage technologies for HPEG applications

Technology Unit cost ($/kWh) Energy density (Wh/kg) Cycle life (80% DoD*) Efficiency (%) HEV suitability
Lead-acid 74-190 30-50 200-1,500 70-90 Limited (heavy, Pb hazard)
NiMH ~390 60-120 500-1,000 70-90 Moderate (high self-discharge)
Li-ion 250-400 100-250 500-5,000 90-95 Poor (high cost, safety risk)
Supercapacitor 10,000-20,000 5-10 > 100,000 90-98 Poor (cost, low density)
Sand Battery (PCM + TEG) ~20 36-50 (thermal); ~3-5 (electrical†) > 1,000 thermal cycles ~7 (module); ~5 (system†) Optimal (low cost, safe, durable)
Table 2

Thermophysical properties of candidate dopant materials and selection outcome

Material ρ (kg m-3) Cp (J kg-1 K-1) k (W m-1 K-1) ρCp (MJ m-3 K-1) L (kJ kg-1) Tm (K) Role Ref.
Quartz sand (baseline) 2,650 730 1.4 1.93 - 1,983 Matrix [6]
Solar Salt (60/40 NaNO3/KNO3) 2,170 1,550 0.55 3.36 ~100 493 PCM (latent buffer) [24]
Flake graphite 2,200 710 150 1.56 - 3,920 Conduction enhancer [23]
Copper turnings 8,960 385 400 3.45 - 1,358 Conduction enhancer [22]
Iron filings 7,870 449 80 3.53 - 1,811 Sensible storage [31]
Silicon carbide (SiC) 3,160 675 120 2.13 - 3,003 Hybrid (conductivity + inertness) [21]
Alumina (Al2O3) 3,950 775 30 3.06 - 2,345 Sensible storage [33]
Magnetite (Fe3O4) 5,170 670 5.1 3.46 - 1,870 Sensible storage [34]
Steatite (MgSiO3) 2,700 900 3 2.43 - 1,773 Sensible storage [35]
Aluminum turnings 2,700 897 237 2.42 - 933 Conduction enhancer [36]
Boron nitride (h-BN) 2,100 800 30/400 1.68 - 3,246 Conduction enhancer [37]
CaCl2·6H2O 1,710 1,460 1.09 2.5 192 302 PCM [36]
NaOH 2,130 1,490 0.92 3.17 165 596 PCM [38]

Because sand is locally abundant and resistive heating elements are standard industrial components, the system can be implemented using regional supply chains, thereby reinforcing the HEV’s objective of reducing dependence on centralized energy infrastructure and enhancing community-level resilience.

Table 1 provides a quantitative comparison of candidate energy storage technologies for the HPEG application scenario. The sand battery platform achieves a unit material cost of approximately $20/kWh, one to two orders of magnitude below lithium-ion, lead-acid, and supercapacitor alternatives[12]. The module-level conversion efficiency of the sand battery pathway, governed by the Carnot-Seebeck relationship at the TEG interface, is evaluated from Equation (1) as follows[13,14]:

$$ \eta_{T E G}=\frac{T_{H}-T_{C}}{T_{H}} \cdot \frac{\sqrt{1+Z T}-1}{\sqrt{1+Z T}+T_{C} / T_{H}} $$

where TH and TC are the hot-side and cold-side temperatures of the TEG, and ZT is the dimensionless thermoelectric figure of merit of the module material. Evaluated across the temperature span available between the 493 K plateau and a near-ambient cold side, a gradient of order 150 K to 190 K once the interfacial drop of Section 3.2 is included, Equation (1) with ZT ≈ 0.8 - 1.2 returns a module-level conversion efficiency near 6% to 8%. This is consistent with recent bismuth-telluride devices, which deliver 6.9% at ΔT = 182 K[15] and 6.5% to 8.0% at ΔT = 225 K[16,17]. Efficiencies approaching 12% are not accessible to single-stage Bi2Te3 in this window and would require either a substantially larger gradient or a higher-ZT material system. While this efficiency is substantially lower than the 90%-95% achieved by lithium-ion batteries, the comparison is economically misleading in the HEV context: the input energy derives from otherwise unmonetized surplus human labor, and the effective cost of the efficiency loss differs materially from a conventional grid-connected scenario[18]. At a per-household storage cost below ¥600, the sand battery pathway compresses the projected investment payback period to under 3.2 years without external subsidy, compared to 6.8 years for an equivalent lithium-ion installation[11].

A clarification is warranted on how these efficiency terms should be read. Equation (1) defines a module-level ceiling fixed by the temperature actually spanned by the thermoelectric legs, whereas the thermal delivery efficiency ηdel introduced later [Equation (16)] describes only the fraction of stored heat that reaches the module surface. The realized electrical efficiency of the system is the product ηdel·ηTEG, lowered further by the cold-side thermal resistance that sets the true leg gradient, by electrical load matching at the converter, by the fractional wall area covered by modules, and by inter-module interconnection losses. None of these quantities should be interpreted in isolation as a system-level electrical efficiency. For the present design, 30 vol% composite stores about 0.49 GJ m-3, near 54 Wh kg-1, from Equation (4) and the Table 2 properties; delivering 82% of this to a module operating near 7% conversion gives a realized electrical density of roughly 3 Wh kg-1 to 5 Wh kg-1 and an electricity-in to electricity-out efficiency on the order of 5%. The temperature dependence of the leg transport properties is retained through the cycle-averaged formulation of Equation (12), so the dominant residual uncertainties lie in cold-side management and module coverage rather than in the material figure of merit.

The operating principle of the sand battery is illustrated schematically in Figure 2, where the principal structural layers - including the quartz-sand core, phase change material (PCM) outer annulus, thermal insulation layer, and steel casing - are individually identified. Indicative dimensions (vessel diameter Ø ≈ 0.6 m, height ≈ 0.8 m) are given for reference; the thermal interface material (TIM) layer thickness of 0.1 mm is annotated but not drawn to scale relative to the other components. Surplus electrical energy from the HPEG system is converted to thermal energy through a central resistive heating element embedded in a cylindrical packed-bed storage vessel. Heat propagates radially outward through the sand-based storage medium, accumulating as sensible thermal energy. The incorporation of PCMs into the outer annular region introduces an additional latent heat buffer: as the storage temperature crosses the PCM melting point, the phase transition absorbs thermal energy isothermally, stabilizing the hot-side temperature at the TEG interface and improving the time-averaged thermoelectric conversion efficiency[16,19]. The TEG modules, mounted on the outer vessel surface, exploit the temperature difference between the hot storage medium and the ambient cold side to generate electricity via the Seebeck effect.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 2. Schematic illustration of the sand battery and sidewall thermoelectric conversion stack. (A) Structural schematic of the sand battery; (B) Enlarged view of the interfacial thermoelectric conversion stack. PCM: Phase change material.

The thermal performance of the sand-based storage system is governed by the effective thermal properties of the composite medium. Quartz sand, while serving as an excellent low-cost and chemically stable baseline matrix, exhibits limited thermal conductivity (approximately 1.4 W m-1 K-1) that restricts the rate of radial heat transport to the TEG interface[6]. To address this limitation, composite formulations incorporating thermally conductive or phase-change dopants have been investigated. The effective thermal conductivity of such composites can be estimated through volumetric mixing rules within an effective medium theory (EMT) framework[20]:

$$ k_{e f f}=\phi_{s} k_{s}+\phi_{d} k_{d} $$

where ks and kd are the intrinsic thermal conductivities of the sand matrix and dopant phase, respectively, and ϕi denotes the volumetric fraction of each constituent subject to ϕs + ϕd = 1.

The parallel conduction limit in Equation (3) does not resolve grain-grain contact resistance, percolation-mediated network formation, or crystallographic anisotropy. Contact resistance is more consequential for copper turnings and flake graphite, where particle geometry makes contact area sensitive to applied stress and orientation. At 20-30 vol%, high-aspect-ratio graphite platelets can form percolating networks that drive keff nonlinearly beyond the linear prediction by factors of two to five, so the conductivity advantage of graphite and copper is underestimated rather than overstated in the present simulations. Partial platelet alignment in flake graphite could additionally shift the effective radial conductivity by 30%-40% relative to the isotropic average assumed here. SiC, being approximately equiaxed and below the percolation threshold at the loadings examined, is the candidate most faithfully represented by Equation (3). Solar Salt’s ranking is unaffected by these considerations, as its contribution derives from latent heat buffering rather than conduction enhancement, a mechanism captured correctly by the apparent heat capacity formulation.

High-conductivity additives such as flake graphite (kd ≈ 150 W m-1 K-1) and copper turnings (kd400 W m-1 K-1) can establish percolation-mediated conductive networks at sufficient volume fractions, substantially suppressing bed thermal resistance[21,22]. Among PCM candidates, the NaNO3-KNO3 eutectic (Solar Salt) is well characterized in concentrated solar power (CSP) applications[23], with a latent heat of approximately 100 kJ kg-1 and a melting temperature of approximately 493 K that falls within the anticipated TEG operating window[23,24]. Silicon carbide (SiC) offers an intermediate combination of conductivity enhancement (kd120 W m-1 K-1) and superior chemical inertness at elevated temperatures relative to metallic or carbonaceous fillers[21]. Despite this body of work on individual dopant materials, systematic parametric investigation of their combined effects on TEG-side thermal delivery within a compact storage geometry has not been reported[25]. To visualize the multi-dimensional trade-offs governing dopant selection, Figure 3A maps all twelve candidate additives onto an Ashby-type thermal conductivity-volumetric heat capacity diagram overlaid with iso-diffusivity contours, while Figure 3B ranks them against six normalized screening criteria through a weighted composite index; together, these representations confirm that Solar Salt, flake graphite, copper turnings, iron filings, and SiC span the broadest and most complementary region of the accessible thermophysical design space. In both panels, the five retained candidates are marked with red asterisks to distinguish them from the seven materials excluded during the initial screening phase.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 3. Multi-dimensional thermophysical screening of candidate materials. (A) Thermal conductivity vs. volumetric heat capacity property map; (B) Normalized screening heatmap and composite scores. PCM: Phase change material.

In Figure 3A, Solar Salt occupies the high-ρCp, low-k quadrant, a position that reflects its latent heat contribution at the solid-liquid transition rather than bulk thermal conduction, and its bubble size, which encodes thermal diffusivity, is the smallest among the retained candidates. Flake graphite and copper turnings anchor the high-conductivity margin at k ≥ 150 W m-1 K-1, where their diffusivity advantage is correspondingly largest. SiC clusters at an intermediate position geometrically distinct from both the PCM and conductor groups, indicating that its selection relies on a combination of moderate conductivity and superior chemical inertness rather than performance in any single criterion. In Figure 3B, these four candidates each achieve their highest normalized score on a different criterion, confirming that the retained set captures complementary rather than redundant thermophysical functions.

Beyond the selection and spatial distribution of composite constituents, two additional engineering challenges govern the practical viability of sand-based thermal storage at the household scale. First, the thermal contact resistance at the interface between the granular storage medium and the solid TEG module surface can rival or exceed the bulk conduction resistance of the storage medium in compact geometries where the surface-area-to-volume ratio is high[26,27]. Imperfect mechanical contact, surface roughness, and differential thermal expansion between the packed bed and the TEG substrate introduce an interfacial thermal barrier that directly limits the fraction of stored energy deliverable as useful heat flux to the thermoelectric conversion stage. Quantifying this resistance and developing mitigation strategies through compliant thermal interface materials or contact pressure optimization is essential for closing the gap between theoretical and realized system performance. Second, repeated thermal cycling between ambient and operating temperatures induces cyclic thermal stresses within the storage medium and at containment boundaries[28]. The mismatch in the coefficients of thermal expansion (CTEs) between quartz sand, dopant phases, and metallic or ceramic containment structures can drive progressive microcracking, particle rearrangement, and degradation of interfacial contact conductance over hundreds to thousands of charge-discharge cycles[28]. Iliev et al. (2024) demonstrated through discrete element modeling that the accumulation of permanent deformation (thermal ratcheting) in packed-bed TES is especially prominent when CTEs of the storage wall and granular filling differ substantially[29]. Understanding the magnitude and spatial evolution of these thermomechanical stresses is necessary to establish the long-term reliability of the storage unit under field conditions.

The remainder of this paper is organized as follows: Section 2 (Experimental) details the methodological framework across three parallel investigations - the effective medium formulation and parametric finite-element sweep used to evaluate thirty composite TES configurations, the transient thermal-phase change simulation and thermo-mechanical coupling analysis developed to characterize interfacial resistance and heat flux delivery, and the 2D axisymmetric cyclic stress model constructed to assess long-term material degradation. Section 3 (Results and Discussion) presents and interprets the corresponding findings - the identification of 30 vol% layered Solar Salt as the optimal composite formulation on the basis of its isothermal phase-change buffering behavior, the parametric mapping of TIM conductivity and contact pressure onto a bounded feasible design region satisfying concurrent thermal and durability constraints, and the material-pair screening that establishes ZrO2-Inconel 718 as the preferred insulation-shell combination for cyclic thermomechanical reliability over a 20-year service horizon.

EXPERIMENTAL

This section describes the three-tier computational framework developed to evaluate the sand-based TES system. The first tier uses effective medium theory and parametric finite-element sweeps to screen thirty composite storage configurations. The second tier characterizes interfacial heat transfer through a transient thermal-phase change model coupled to thermo-mechanical analysis. The third tier assesses long-term cyclic reliability via a 2D axisymmetric stress accumulation model across nine insulation-shell material combinations. The mesh-independence assessment for the Tier 1 pure-sand baseline is summarized in Table 3. The complete set of geometric, loading, interfacial, phase-change, and solver inputs used across the three model tiers is consolidated in Table 4 to support independent reproduction of the results. Parameters that are explored parametrically are reported as a baseline value followed by the swept range.

Table 3

Mesh independence study for the pure-sand baseline (Tier 1), with the monitored TEG-side temperature at t = 5 h

Characteristic element size (mm) Elements (approx.) TTEG at tf (K) Deviation from finest grid (K)
2.00 4,000 422.0 +1.7
1.00 15,000 420.7 +0.4
0.50 (adopted) 58,000 420.4 +0.1
0.25 230,000 420.3 Reference
Table 4

Consolidated model input parameters for the three-tier finite-element framework

Category Parameter (symbol) Value (baseline/range) Notes/source
Geometry Inner heater radius, Ri 0.025 m Central resistive element, Equations (5) and (7)
Core-annulus interface radius, Rc 0.20 m Layered partition, Equation (6)
Outer casing radius, Ro 0.30 m TEG-side boundary, TTEG = T(Ro,t)
Storage height, H 0.80 m Consistent with Figure 2
Outer vessel diameter 0.60 m Equals 2Ro
TEG contact (outer lateral) area, A = 2π Ro H ≈ 1.51 m2 Basis for surface heat-flux conversion
TIM layer thickness, dTIM 0.1 mm Equation (13), Figure 5
Ceramic insulation shell thickness 5 mm Alumina/mullite/zirconia
Metallic containment shell thickness 3 mm 304SS/C-steel/Inconel 718
TIM edge fillet radius 0.5 mm Suppresses stress singularity, Tier 2
Thermal loading Steady-state input heat flux, qint,ss 12,000 W m-2 Equation (15)
Ramp time constant 3,600 s 95% of flux reached within 1 h
Heat-flux profile, qint (t) 12000[1 - exp(-t/3600)] W m-2 Equation (15)
Charging window, tf 18,000 s (5 h) Primary horizon
Cooling phase (Tier 3) 5 h, zero input One full cycle = 10 h
Target design life, N 7,300 cycles 20 years at 1 cycle per day
Boundary & initial conditions Initial/reference temperature, T0 = Tref 300 K Uniform, stress-free state
Tier 1 outer radial boundary Adiabatic Isolates intrinsic storage dynamics
Internal interface (r = Rc) Temperature and flux continuity Equation (6)
Cold-side convection (Tier 2, top) h = 150 W m-2 K-1, T∞ = 300 K Combined convection and radiation
Outer-shell convection (Tier 3) h = 5 to 10 W m-2 K-1, Tamb = 300 K Natural convection during cooling
Phase-change treatment Method Apparent heat capacity, Gaussian-smoothed Equation (8)
Melting temperature, Tm 493 K Solar salt eutectic
Transition half-width, ΔTm 5 K Smoothing interval
Latent heat, Ld 100 kJ kg-1 Table 2
Liquid fraction, ξ 0 to 1 Equation (4)
Interfacial parameters TIM conductivity, kTIM (baseline/swept) 3.5/1.0 to 10.0 W m-1 K-1 Figure 9A
Contact resistance, Rc,upper = Rc,lower 5 × 10-5 m2 K W-1 Per interface
Total interfacial resistance, RTIM 1.29 × 10-4 m2 K W-1 Equation (13)
Contact pressure, Pcontact (baseline/swept) 1.0/0.5 to 3.5 MPa Figure 9
TEG substrate Al2O3 Figure 5A
Parametric design matrix Dopant candidates Solar salt, flake graphite, copper turnings, iron filings, SiC Table 2
Volume fractions, φd 0.10, 0.20, 0.30 Global sweep
Spatial architectures Uniform, layered 2 cases
Total Tier 1 configurations 30 (5 × 3 × 2) Parametric sweep
Insulation-shell pairs (Tier 3) Alumina, mullite, zirconia paired with 304SS, C-steel, Inconel 718 Figure 10E
Thermoelectric model Module material Bi2Te3 Equations (1) and (12)
Figure of merit, ZT 0.8 to 1.2 Commercial modules
Operating ΔT, cold-side Tc 40 to 60 K, 300 K Efficiency window
Property treatment Solid constituents (sand, solid dopants) Constant, evaluated near 300 K Table 2
Solar salt latent term Temperature-dependent Equation (8)
Solar salt liquid-phase CTE, αsalt 40 × 10-6 K-1 Tier 3
TEG legs α, ρe, K Temperature-dependent Equation (12)
Mechanical constitutive model Linear elastic, isotropic Tref = 300 K
Solver & numerics Thermal/PCM/axisymmetric stress COMSOL Multiphysics 6.4
3D thermo-mechanical ANSYS Workbench 2024 R1 One-way coupling
Time integration BDF, adaptive stepping
Initial/maximum time step 0.1 s/10 s
Relative residual tolerance < 10-6 Per time step
PCM convergence aid Segregated solver with Anderson acceleration
Output sampling TTEG at 1 s intervals
Fatigue/ratcheting Goodman correction; power-law fit (MATLAB) Equations (18) and (22)

Composite thermal energy storage materials

Effective medium formulation

To circumvent the prohibitive computational cost of resolving grain-scale heterogeneities in particulate composites, each doped sand configuration was modeled as a homogeneous continuum within an EMT framework implemented in COMSOL Multiphysics 6.4. The macroscopic transport properties of each sand-dopant mixture were derived from volumetric mixing rules. The effective density, mass-averaged isobaric heat capacity, and parallel-weighted thermal conductivity of the composite bed are expressed as a coupled property set:

$$ \rho_{\text {eff }}=\phi_{s} \rho_{s}+\phi_{d} \rho_{d}, C_{p, \text { eff }}=\frac{\phi_{s} \rho_{s} C_{p, s}+\phi_{d} \rho_{d} C_{p, d}}{\rho_{\text {eff }}}, k_{\text {eff }}=\phi_{s} k_{s}+\phi_{d} k_{d} $$

where subscripts s and d denote the quartz sand matrix and dopant phase, respectively, and ϕi is the volumetric fraction of constituent i subject to ϕs + ϕd = 1. The volumetric thermal energy storage density of the composite, accounting for both sensible and latent contributions, is:

$$ e_{\text {vol }}=\rho_{\text {eff }} C_{p, \text { eff }} \Delta T+\phi_{d} \rho_{d} L_{d} \xi(T), \xi(T) \in[0,1] $$

where Ld is the mass-specific latent heat of the dopant (non-zero only for phase-change constituents) and ξ(T) is the liquid fraction evolving according to the melting front progression. The Biot number characterizing the relative magnitude of internal conduction resistance to external convective resistance at the TEG interface is given by:

$$ \mathrm{Bi}=\frac{h_{\mathrm{TEG}} L_{c}}{k_{\text {eff }}}, L_{c}=R_{o}-R_{i} $$

where hTEG is the effective thermal contact conductance at the TEG module surface and Lc is the characteristic radial length of the annular storage domain.

Dopant selection rationale

Five candidate dopants were selected to span the principal thermophysical mechanisms by which solid-state additives modify packed-bed thermal performance: latent heat absorption, thermal conduction enhancement, and volumetric heat capacity augmentation. The selection drew on an initial screening of twelve candidate materials [Table 2], from which five were retained on the basis of thermal figure-of-merit, chemical compatibility with silica at temperatures up to 700 K, commercial availability, and cost[30].

The composite index in Figure 3B is evaluated as a weighted sum of six normalized criteria. Thermal conductivity received the highest weight (0.25) because radial heat delivery to the TEG surface is governed by the effective conductivity of the annular composite layer, making it the rate-limiting property in this cylindrical geometry. Volumetric heat capacity was assigned a weight of 0.20 to reflect the sensible thermal energy accumulated over the 5 h charging window. Latent heat content, volumetric energy storage density, and chemical compatibility with the silica matrix were each weighted at 0.15. These three criteria are of comparable importance but operate through distinct mechanisms: latent heat governs isothermal buffering capacity at the phase-change transition, volumetric energy density integrates sensible and latent contributions into a single delivery metric relevant to the finite charging window, and chemical compatibility imposes a stability ceiling that no performance advantage can offset. Thermal diffusivity was assigned the lowest weight (0.10); as the ratio of conductivity to volumetric heat capacity, it carries information partly captured by the two highest-weighted terms, but its inclusion retains sensitivity to fast-transient thermal response that would otherwise be suppressed in a score dominated by steady-state properties.

Each criterion was normalized to [0, 1] by min-max scaling over the twelve candidates: $$ \tilde{x} $$ = (x - xmin)\/(xmax - xmin), with chemical compatibility treated as binary. A one-at-a-time weight perturbation of ±50%, with remaining weights rescaled to preserve unity, left Solar Salt, flake graphite, copper turnings, and SiC among the top five in all twelve variants, with Kendall rank correlations against the baseline exceeding 0.85 throughout, confirming that the selection is not sensitive to the precise weight assignments within physically reasonable bounds.

Solar Salt (60 wt% NaNO3, 40 wt% KNO3) was retained as the sole PCM, chosen for its well-characterized latent heat (Ld ≈ 100 kJ kg-1 and a solid-liquid transition temperature (Tm ≈ 493 K) falling within the anticipated TEG operating window[23,24]. The isothermal buffering effect of this plateau is evident in Figure 4A. Flake graphite (kd ≈ 150 W m-1 K-1) and copper turnings (kd ≈ 400 W m-1 K-1) occupy the high-conductivity end of the design space, targeting aggressive suppression of bed thermal resistance[22,31]. The superior thermal delivery of these high-conductivity formulations relative to the pure sand baseline is also reflected in Figure 4A. Iron filings were included as a high-volumetric-heat-capacity additive (ρdCp,d3.5 MJ m-3 K-1) to evaluate whether enhanced sensible storage density can offset modest conductivity improvements[32]. Silicon carbide (SiC, kd ≈ 120 Wm-1 K-1) probes an intermediate regime, offering simultaneous elevation of conductivity and superior chemical inertness at elevated temperatures relative to metallic or carbonaceous fillers[21,33]. The contrast in radial heat distribution between the pure sand baseline and the Solar Salt composite at t = 5 h is illustrated in Figure 4B and C, respectively.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 4. Simulated TEG interface temperature during charging (A) and radial temperature distributions at t = 5 h for pure sand (B) and 30 vol% layered Solar Salt (C). TEG: Thermoelectric generator; PCM: phase change material.

Seven additional candidate materials were evaluated during the screening phase but ultimately excluded [Table 2]. Alumina (Al2O3) offers excellent chemical stability but its thermal conductivity at the grain scale (k ≈ 30 W m-1 K-1) provides insufficient enhancement over quartz sand to justify inclusion[6]. Magnetite (Fe3O4) possesses favorable volumetric heat capacity (ρCp ≈ 3.6 MJ m-3 K-1) but undergoes irreversible oxidation to hematite (Fe2O3) above 570 K in ambient atmosphere, compromising long-term property stability[34]. Steatite, a magnesium silicate ceramic, was excluded for its low thermal conductivity (k ≈ 3 W m-1 K-1) despite high volumetric heat capacity[35]. Aluminium turnings, although highly conductive (k ≈ 237 W m-1 K-1), melt at 933 K and suffer progressive surface oxidation that generates insulating Al2O3 layers and degrades interfacial contact conductance[36]. Boron nitride (hexagonal, k ≈ 30 W m-1 K-1, k ≈ 400 W m-1 K-1) was excluded because of the strong anisotropy in its thermal conductivity, which renders effective medium predictions unreliable without explicit microstructural resolution[37]. Calcium chloride hexahydrate (CaCl2·6H2O) melts at 302 K, far below the target operating window[36]. Sodium hydroxide (NaOH, Tm ≈ 596 K) presents severe corrosion risk to both quartz sand and metallic containment at the temperatures of interest[38].

Spatial configuration and boundary conditions

The dopant volume fraction ϕd was parameterized at 0.10, 0.20, and 0.30 via a global parameter sweep, yielding 30 distinct configurations (5 dopants × 3 fractions × 2 architectures). Two loading architectures were investigated. In the uniform configuration, the entire sand domain was assigned spatially invariant ρeff, Cp,eff, keff corresponding to the target ϕd. In the layered (functionally graded) configuration, the cylindrical domain was partitioned into two concentric sub-domains: an inner core (0 ≤ rRc) retaining pure quartz sand, and an outer annulus (Rc < rRo) assigned the composite material properties. At the internal interface r = Rc, temperature continuity and heat flux conservation were enforced:

$$ T^{-}\left(R_{c}, t\right)=T^{+}\left(R_{c}, t\right),-\left.k_{s} \frac{\partial T}{\partial r}\right|_{r=R_{c}^{-}}=-\left.k_{\text {eff }} \frac{\partial T}{\partial r}\right|_{r=R_{c}^{+}} $$

The transient temperature field within each homogeneous sub-domain is governed by the energy equation in cylindrical coordinates:

$$ \rho_{\text {eff }} C_{p, \text { eff }}^{*}(T) \frac{\partial T}{\partial t}=\frac{1}{r} \frac{\partial}{\partial r}\left(r k_{\text {eff }} \frac{\partial T}{\partial r}\right)+\frac{\partial}{\partial z}\left(k_{\text {eff }} \frac{\partial T}{\partial z}\right)+\dot{Q}(r) $$

where $$ \dot{Q}(r) $$ denotes the volumetric heat generation rate localized at the central resistive heating element. For PCM-doped configurations, the apparent heat capacity method was employed to handle the phase-change nonlinearity, replacing Cp,eff with an augmented capacity that incorporates the latent heat release through a Gaussian-smoothed liquid fraction derivative:

$$ C_{p, \text { eff }}^{*}(T)=C_{p, \text { eff }}+\frac{\phi_{d} \rho_{d} L_{d}}{\Delta T_{m} \sqrt{2 \pi}} \mathrm{exp}\left[-\frac{\left(T-T_{m}\right)^{2}}{2\left(\Delta T_{m}\right)^{2}}\right] $$

where ΔTm = 5 K is the half-width of the transition interval centered at Tm. A uniform initial condition T(r,z,0) = T0 = 300 K was imposed throughout the domain, and the outer radial boundary was treated as adiabatic ($$ \partial T /\left.\partial r\right|_{r=R_{o}}=0 $$) to isolate the intrinsic storage dynamics of each composite from external dissipation.

Numerical implementation

All simulations were carried out in COMSOL Multiphysics 6.4 using the Heat Transfer in Solids module. The computational domain was constructed as a 2D axisymmetric geometry comprising a cylindrical annulus bounded by the inner heater radius Ri and the outer casing radius Ro. For the layered architecture, a concentric partition at r = Rc divided the domain into two material sub-domains, each assigned distinct effective properties through Equation (1). The geometry was discretised with a mapped quadrilateral mesh refined in the radial direction near both the heater interface and the material discontinuity at Rc, where the steepest temperature gradients were anticipated. A mesh convergence study was performed on the pure sand baseline by successively halving the characteristic element size from 2.0 mm to 0.25 mm. The TEG-side temperature at tf changed by 0.1 K between the two finest grids, below the 0.3 K threshold adopted as the convergence criterion, and the monotonic, asymptotic approach of the monitored temperature confirms that the solution lies within the grid-independent regime. The 0.5 mm mesh was retained for the production sweep because it reproduces the converged temperature to within 0.3 K at roughly one quarter of the degrees of freedom of the finest grid, giving the most efficient accuracy-to-cost balance for the 30-configuration study. Equivalent studies confirmed grid independence for the other two tiers: the interfacial heat flux changed by less than 0.4% beyond five boundary-layer sublayers, and the peak interfacial von Mises stress changed by less than 1% between the 60,000 and 120,000 element discretization. Across the figures, each plotted curve corresponds to a single grid-independent solution of the governing equations, and where an envelope is shown it quantifies the residual cycle-to-cycle variation of the stabilized cyclic solution. Confidence in the reported quantities therefore rests on the grid-independence levels established above and on the breadth of the parametric and sensitivity sweeps, which span the thirty composite configurations and the nine material pairings.

The time-dependent solver employed the backward differentiation formula (BDF) with adaptive time stepping. The initial time step was set to 0.1 s to resolve the early transient, and the maximum step was capped at 10 s to ensure adequate temporal resolution of the phase-change dynamics in the Solar Salt configurations. For those configurations, the apparent heat capacity formulation [Equation (6)] replaced the standard heat capacity; a segregated solver with Anderson acceleration was used to stabilize convergence during the latent heat interval, where the effective heat capacity exhibits a sharp peak near Tm. Convergence was declared when the relative residual of the temperature field fell below 10-6 at every time step.

The 30 configurations (5 dopants × 3 volume fractions × 2 architectures) were executed through the COMSOL parametric sweep functionality. Unless otherwise stated, the thermophysical properties of the solid constituents (density, specific heat, and thermal conductivity of quartz sand and the solid dopants) were treated as temperature-independent and evaluated at the representative values listed in Table 2. Across the 300 K to 660 K range spanned by the simulations, the intrinsic conductivity and heat capacity of these solids vary by less than about 15%, which is small relative to the order-of-magnitude contrasts between dopant candidates that drive the comparative ranking. The constant-property assumption therefore leaves the relative performance ordering unaffected, although it may shift absolute terminal temperatures by a few kelvins. The two physically nonlinear responses were resolved with explicit temperature dependence: the latent contribution of Solar Salt through the apparent heat capacity formulation of Equation (8), and the thermoelectric leg properties α(T), ρe(T) and K(T) entering the cycle-averaged efficiency of Equation (12).

Each configuration was defined by a single global parameter vector [ϕd kd ρd Cp,d Ld] that propagated through the material property expressions and the apparent heat capacity definition. A 5 h charging window (tf = 18,000 s) was simulated for each case, and the TEG-side boundary temperature TTEG(t)≡T(Ro,t) was recorded at 1 s intervals as the primary output. Full-domain temperature field snapshots were exported at hourly intervals for the pure sand baseline and the optimal 30 vol% layered Solar Salt configuration, providing the full-field spatial record used for the radial heat-transport comparison reported in the Results.

Performance metrics

To facilitate cross-dopant comparison, a dimensionless thermal enhancement ratio was defined:

$$ \eta_{T}(t)=\frac{T_{\mathrm{TEG}}(t)-T_{0}}{T_{\mathrm{TEG}, \text { base }}(t)-T_{0}} $$

where ηT > 1 indicates enhanced thermal delivery to the TEG interface relative to the pure sand baseline. The temporal stability of the TEG hot-side temperature during plateau intervals was quantified by:

$$ \sigma_{T}=\sqrt{\frac{1}{t_{f}-t_{p}} \int_{t_{p}}^{t_{f}}\left[T_{\mathrm{TEG}}(t)-\bar{T}_{\text {plateau }}\right]^{2} d t} $$

where tp is the onset time of the plateau and $$ \bar{T}_{\text {plateau }} $$ is the time-averaged temperature over the plateau interval. For dopants whose loading admits a percolation-mediated conductivity transition, the practical upper bound on volume fraction was identified through the stationary point of the effective thermal diffusivity with respect to dopant fraction:

$$ \frac{\partial}{\partial \phi_{d}}\left(\frac{k_{\text {eff }}}{\rho_{\text {eff }} C_{p, \text { eff }}}\right)=0 $$

The cycle-averaged TEG conversion efficiency, which accounts for the nonlinear dependence of thermoelectric performance on the instantaneous temperature differential, was evaluated as:

$$ \bar{\eta}_{\mathrm{TEG}}=\frac{1}{t_{f}} \int_{0}^{t_{f}} \eta_{\mathrm{TEG}}\left[T_{\mathrm{TEG}}(t), T_{c}, \alpha_{\mathrm{TE}}(T), \rho_{e}(T), K_{\mathrm{TE}}(T)\right] d t $$

where αTE(T), ρe(T), and KTE(T) are the temperature-dependent Seebeck coefficient, electrical resistivity, and thermal conductance of the thermoelectric legs, respectively.

Interfacial thermal resistance and heat flux management

Transient thermal-phase change simulation

The interfacial thermal resistance between the composite storage medium and the TEG substrate was quantified through a dedicated 2D axisymmetric transient simulation incorporating phase-change dynamics, implemented in COMSOL Multiphysics 6.4. The simulation workflow is summarized in Figure 5.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 5. Numerical workflow for the transient thermal simulation. (A) 3D geometric model and material stacking; (B) Applied boundary conditions with a pulsed heat flux; (C) Simulated cross-sectional temperature field. TIM: Thermal interface material.

The computational domain comprised four vertically stacked layers: the composite sand bed (incorporating the 30 vol% layered Solar Salt formulation identified in the preceding section[39]), a compliant TIM layer of thickness dTIM = 0.1 mm, an alumina (Al2O3) TEG substrate, and the TEG module body [Figure 5A]. The TIM layer was assigned a thermal conductivity kTIM = 3.5 W m-1 K-1, representative of commercially available silicone-based gap pads used in power electronics packaging[40]. The interfacial thermal resistance across this layer is expressed as:

$$ R_{\mathrm{TIM}}=\frac{d_{\mathrm{TIM}}}{k_{\mathrm{TIM}}}+R_{\mathrm{c}, \text { upper }}+R_{\mathrm{c}, \text { lower }} $$

where Rc,upper and Rc,lower are the contact resistances at the upper (sand bed-TIM) and lower (TIM-substrate) interfaces, respectively. For the baseline simulation, these contact resistances were set to 5 × 10-5 m2 K W-1 each, yielding a total interfacial resistance RTIM ≈ 1.29 × 10-4 m2 K W-1. The corresponding interfacial heat flux delivered to the TEG substrate under steady-state conditions is:

$$ q_{\mathrm{TEG}}=\frac{T_{\mathrm{bed}}-T_{\mathrm{sub}}}{R_{\mathrm{TIM}}} $$

The contact resistances Rc,upper and Rc,lower in Equation (13) were assigned constant values of 5 × 10-5 m2 K W-1, consistent with values reported for lightly clamped silicone-based gap pads against ceramic surfaces[41]. In practice, contact resistance decreases with increasing contact pressure as interfacial asperities deform, with experimental correlations indicating a reduction of approximately 30%-50% as pressure increases from 0.5 MPa to 2.0 MPa for soft polymer-ceramic interfaces. The fixed-resistance assumption is therefore most representative of the reference condition at Pcontact = 1.0 MPa. Across the parametric sweep, this introduces a bounded conservatism whose net effect on the identified optimum is modest, given that the sensitivity of ηdel to Rc is second-order relative to its sensitivity to kTIM in this regime. Incorporating a pressure-dependent contact resistance correlation into Equation (13) is recommended as a refinement prior to prototype testing.

The mesh strategy was designed to resolve the steep thermal gradients within and adjacent to the 0.1 mm TIM gap[41]. A five-layer boundary layer mesh was deployed on both the upper and lower surfaces of the TIM domain, with a first-layer thickness of 2 μm and a geometric growth ratio of 1.5 (Figure 5A, inset). The maximum element size was constrained to 5 μm within the TIM layer itself, transitioning to a coarser mapped quadrilateral mesh in the bulk sand bed and substrate domains. A mesh independence study confirmed that further refinement of the boundary layer beyond five sub-layers altered the computed interfacial heat flux by less than 0.4%.

The thermal boundary conditions replicated the operating scenario of the sand battery during a single charging cycle [Figure 5B]. A time-dependent pulsed heat flux was applied at the bottom boundary to represent the resistive heating input:

$$ q_{\text {in }}(t)=12000 \cdot\left(1-\exp \left(-\frac{t}{3600}\right)\right) \mathrm{W} \cdot \mathrm{~m}^{-2} $$

where the exponential ramp approximates the thermal inertia of the resistive heating element during start-up, reaching 95% of the steady-state flux of 12,000 Wm-2 within the first hour. The top surface was subjected to a convective boundary condition with h = 150 W m-2 K-1, representing the combined natural convection and radiative exchange at the TEG cold side. The initial temperature was set uniformly to 300 K throughout all domains. The transient solver employed BDF, and the apparent heat capacity method [Equation (8)] was retained for the Solar Salt layer to capture phase-change nonlinearity[42].

The computed 2D temperature field at t = 2.5 h is presented in Figure 5C. The thermal field reveals a pronounced temperature discontinuity across the TIM gap, with the sand bed side reaching approximately 520 K while the substrate side remains near 480 K, confirming that the 0.1 mm interfacial layer accounts for a temperature drop of approximately 40 K. This drop is comparable in magnitude to the temperature differential exploited by the TEG module itself, indicating that the interfacial resistance constitutes a non-negligible fraction of the total thermal pathway resistance. The fraction of stored thermal energy that is effectively deliverable to the TEG interface within the 5 h charging window was quantified by the thermal delivery efficiency:

$$ \eta_{\mathrm{del}}=\int_{0}^{t_{f}} q_{\mathrm{TEG}}(t) d t / \int_{0}^{t_{f}} q_{\text {in }}(t) d t $$

For the baseline TIM configuration, ηdel was computed to be 0.74, indicating that 26% of the input thermal energy remains trapped upstream of the interfacial barrier at the end of the charging cycle[43]. A parametric sweep over kTIM from 1.0 W m-1 K-1 to 10.0 W m-1 K-1 showed that increasing the TIM conductivity to 6.0 W m-1 K-1 raised ηdel to 0.82, beyond which further gains were marginal.

Thermo-mechanical coupling and fatigue life assessment

The cyclic thermal loading imposed during repeated charge-discharge operation induces mechanical stresses at material interfaces where CTE values are mismatched. To evaluate the structural integrity and fatigue life of the TIM joint under service conditions, a one-way thermo-mechanical coupling analysis was performed in ANSYS Workbench 2024 R1.

A three-dimensional conformal mesh comprising approximately 500,000 hexahedral-dominant elements was generated over the full cylindrical assembly [Figure 6A]. Edge fillets of 0.5 mm radius were introduced at the perimeter corners of the TIM layer to suppress the geometric stress singularity that would otherwise arise at sharp bimaterial interfaces.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 6. Thermo-mechanical and fatigue life analysis of the assembly. (A) Conformal mesh with corner fillets; (B) One-way coupling topology; (C) Imported transient temperature load; (D) Thermal stress concentration and fatigue life distribution.

The coupling topology is shown in Figure 6B: the transient temperature history computed in the Transient Thermal module was mapped as an imported body temperature load onto the Static Structural module, enabling sequential resolution of the thermal and mechanical fields on a shared mesh. This sequential strategy avoids the convergence difficulties associated with fully coupled thermomechanical solvers while preserving the fidelity of the thermal driving force at each structural time step.

The mesh was locally refined at the TIM boundaries to capture the steep stress gradients associated with the coefficient of thermal expansion (CTE) mismatch between the composite sand bed (αTES ≈ 11.5 × 10-6 K-1) and the alumina substrate ($$ \alpha_{A l_{2} O_{3}} $$ ≈ 7.2 × 10-6 K-1) [Figure 6C]. The thermally induced strain at the interface scales with the product of the CTE mismatch and the applied temperature differential:

$$ \varepsilon_{\mathrm{th}}=\Delta \alpha \cdot \Delta T=\left(\alpha_{\mathrm{TES}}-\alpha_{\mathrm{Al}_{2} \mathrm{O}_{3}}\right) \cdot\left(T(t)-T_{\mathrm{ref}}\right) $$

where Tref = 300 K is the stress-free reference temperature. For a peak interfacial temperature of 520 K, this expression yields εth ≈ 9.46 × 10-4, corresponding to a thermal mismatch stress that concentrates at the perimeter edge of the TIM joint where the radial constraint is most severe.

The transient temperature field T(t) was imported as a nodal body temperature load onto the structural model [Figure 6C], and a static structural solution was obtained at each time step corresponding to the peak and valley temperatures of a representative charge-discharge cycle (300 K to 520 K to 300 K). The equivalent (von Mises) stress field exhibited pronounced concentration at the perimeter edge of the TIM layer, where the displacement magnification factor reached approximately 100 under the applied thermal loading [Figure 6D]. The maximum von Mises stress at this location was 48.3 MPa, which remains below the tensile strength of the silicone-based TIM (typically 55-65 MPa) but exceeds 74% of the yield threshold, placing the joint in the high-cycle fatigue regime[44].

Fatigue life estimation was performed using the ANSYS Fatigue Tool with the Goodman mean-stress correction. The alternating stress amplitude σa and mean stress σm were extracted from the computed stress cycle at the critical perimeter location. The fatigue life Nf was evaluated from the modified Basquin relation:

$$ \sigma_{a}=\sigma_{f}^{\prime} \cdot\left(1-\frac{\sigma_{m}}{\sigma_{\mathrm{UTS}}}\right) \cdot\left(2 N_{f}\right)^{b} $$

where $$ \sigma_{f}^{\prime} $$ is the fatigue strength coefficient, σUTS is the ultimate tensile strength, and b is the fatigue strength exponent of the TIM material. The computed fatigue life at the most critically stressed location was Nf ≈ 8,400 cycles. Assuming one full charge-discharge cycle per day, this corresponds to a projected service life of approximately 23 years, which exceeds the 20-year design horizon specified for the HEV infrastructure.

The 20-year horizon corresponds to N = 7,300 cycles at one cycle per day and reflects the typical asset depreciation period for community-scale off-grid infrastructure, it serves as the structural design criterion for the containment vessel. The 23-year figure (Nf ≈ 8,400 cycles) is a computed output of the Goodman fatigue model at the baseline interface condition, not an independently specified target, and its role is to confirm that a sufficient margin exists before the interface is driven toward higher conductivity in the optimization study of Section 3.2.

The thermal ratcheting deformation visible at the outer perimeter in Figure 6D remained below 0.12 mm per cycle, confirming that progressive plastic accumulation does not compromise the geometric stability of the TIM joint within the anticipated service window[45].

Thermal stress and material degradation

Thermomechanical simulation of the multi-layer storage assembly

To evaluate the global thermomechanical response of the storage vessel under sustained cyclic operation, a 2D axisymmetric simulation was constructed in COMSOL Multiphysics 6.4 using a one-way coupling between the Heat Transfer in Solids (ht) and Solid Mechanics (solid) modules. The computational domain comprised four concentric annular regions: the central heating element, the composite storage layer (inner pure-sand core and outer 30 vol% layered Solar Salt-sand composite), a ceramic insulation shell (alumina, 5 mm), and an outer metallic containment shell (stainless steel, 3 mm), as depicted in Figure 7A. All inter-domain boundaries were constructed with shared nodes to enforce displacement continuity[46,47].

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 7. Computational framework for thermo-mechanical simulation. (A) 2D axisymmetric geometry and material distribution; (B) Finite element mesh with interfacial refinement; (C) One-way multiphysics coupling workflow; (D) Cyclic thermal loading profile.

Each domain was assigned a linear elastic constitutive model with isotropic thermal expansion referenced to Tref = 300 K. The CTE values span nearly two orders of magnitude: αsand ≈ 0.5 × 10-6 K-1, αsalt ≈ 40 × 10-6 K-1 (liquid phase), αceramic ≈ 8.0 × 10-6 K-1, and αsteel ≈ 17.3 × 10-6 K-1. This mismatch, identified as the principal driver of interfacial degradation in multi-material TES structures[48,49], governs the radial thermal stress at any interface between adjacent layers i and j:

$$ \sigma_{r}^{i j}(t)=\frac{E_{i} E_{j}}{E_{i}\left(1-v_{j}\right)+E_{j}\left(1-v_{i}\right)}\left(\alpha_{i}-\alpha_{j}\right)\left[T\left(r_{i j}, t\right)-T_{r e f}\right] $$

where i and j denote the indices of the two adjacent material layers; Ei(Ej), νi(νj), and αi(αj) denote the Young’s modulus, Poisson’s ratio, and coefficient of thermal expansion of layer i (layer j), respectively; and rij is the radial coordinate of their shared boundary. The finite-element mesh incorporated five-layer boundary layer elements at each material interface with a first-layer thickness of 0.05 mm [Figure 7B], and the total element count was maintained between 60,000 and 80,000, which a convergence study confirmed to be adequate for the 2D axisymmetric domain[50,51]. This boundary-layer resolution at each bi-material junction is necessary to capture the steep stress gradients arising from CTE mismatches that span nearly two orders of magnitude across adjacent layers. The temperature field T(r,t) was obtained from the transient heat transfer solution and mapped onto the structural domain at each time step through the built-in variable ht.T, completing the one-way coupling illustrated in Figure 7C. The cyclic thermal loading followed the boundary condition profile shown in Figure 7D: each cycle comprised a 5 h charging phase during which the pulsed heat flux [Equation 15)] was applied at the inner boundary, followed by a 5 h cooling phase with zero heat input and natural convective dissipation (h = 5 - 10 W m-2 K-1, Tamb = 300 K) at the outer shell surface.

Cyclic stress accumulation and degradation metrics

The multiaxial stress state at each interface was quantified through the von Mises equivalent stress:

$$ \sigma_{v M}=\sqrt{\sigma_{r}^{2}+\sigma_{\theta}^{2}+\sigma_{z}^{2}-\sigma_{r} \sigma_{\theta}-\sigma_{\theta} \sigma_{z}-\sigma_{z} \sigma_{r}+3 \tau_{r z}^{2}} $$

where σr, σθ, σz, and τrz are the radial, circumferential, axial, and shear stress components in the axisymmetric coordinate system. Ten complete charge-discharge cycles were computed explicitly, and the incremental plastic strain per cycle $$ \Delta \varepsilon_{p}^{(n)} $$ at the most critically stressed interface was monitored for convergence. The rate of strain energy density dissipation per cycle was estimated as[52,53]:

$$ \frac{d W}{d N}=\oint \sigma_{i j} d \varepsilon_{i j}^{p} \approx \sigma_{v M}^{{peak }} \cdot \Delta \varepsilon_{p} $$

where the integral is evaluated over one complete loading-unloading path at the critical material point. Extrapolation to the target design life of N = 7,300 cycles (20 years at one cycle per day) was performed by fitting the accumulated plastic strain data from the first ten cycles to a power-law ratcheting model:

$$ \varepsilon_{p}^{a c c}(N)=\varepsilon_{p}^{(1)}+A \cdot N^{\gamma} $$

where $$ \varepsilon_{p}^{(1)} $$ is the plastic strain after the first cycle, and A and γ are regression constants determined by least-squares fitting in MATLAB, following the methodology validated by Hrifech et al.[47] for packed-bed TES systems. It should be noted that the present continuum model does not resolve discrete particle-level rearrangement within the granular storage medium; such phenomena have been shown by discrete element analysis to contribute additional hoop stress on the containment wall[29]. The continuum-scale results therefore represent a lower bound on the total mechanical demand.

A parametric sweep over nine candidate insulation-shell material combinations (alumina, mullite, and zirconia paired with AISI 304 stainless steel (304SS), carbon steel, and Inconel 718) was conducted to identify the pairing that minimized the peak interfacial von Mises stress and long-term ratcheting strain. The results are presented in the Results and Discussion section. The key parameters governing each of these three computational tiers are consolidated in Table 4, providing a unified reference for the simulation framework described above.

RESULTS AND DISCUSSION

This section presents the simulation results in the same sequence as the methodological framework. The composite formulation study identifies the optimal dopant type, volume fraction, and spatial architecture for TEG-side thermal delivery. The interfacial analysis then quantifies the coupled effects of TIM conductivity and contact pressure on thermal efficiency and fatigue life. Finally, the cyclic stress study establishes the material pair that satisfies both structural durability and long-term reliability requirements.

Composite thermal energy storage materials

Simulations were conducted over a 5 h charging window. The TEG-side boundary temperature TTEG (t) served as the primary performance metric. The undoped quartz sand baseline rose monotonically from 300 K to approximately 420 K over this period, establishing the reference trajectory against which all composite formulations were evaluated.

The Solar Salt configurations produced a qualitatively distinct thermal response not observed in any other dopant group [Figure 8A]. As TTEG (t) approached the eutectic transition temperature of approximately 493 K, latent heat absorption during the solid-liquid phase change induced a well-defined isothermal plateau, visible as a pronounced inflection in the TTEG (t) curve. The 30 vol% layered configuration reached this plateau earliest, at approximately t = 3 h, while the 10 vol% uniform blends did not stabilize until near t = 5 h. This isothermal window was entirely absent in every other dopant group and represents a qualitative, not merely quantitative, advantage for thermoelectric coupling: a stable hot-side temperature directly fixes the Seebeck voltage and suppresses efficiency oscillations in the TEG modules. Purely sensible-heat dopants cannot reproduce this buffering behavior regardless of loading fraction.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 8. Simulated thermal performance of composite TES beds with five candidate dopants. (A-E) TEG-side boundary temperature as a function of charging time for uniform and layered configurations at 10%, 20%, and 30% dopant volume fractions; (F) Three-dimensional temperature field of the pure sand baseline at t = 5 h; (G) Three-dimensional temperature field of the 30 vol% layered configuration at t = 5 h. Comparison of panels (F) and (G) illustrates the redistribution of stored thermal energy toward the TEG boundary enabled by the phase-change front in the layered Solar Salt configuration. TES: Thermal energy storage; TEG: thermoelectric generator.

Graphite delivered the most aggressive early-stage heating among the five candidates [Figure 8B]. The 30 vol% layered variant reached approximately 660 K at t = 5 h, while the 30 vol% uniform blends reached around 650 K, both substantially above the pure sand baseline. The initial heating rate for the 30% uniform configuration approached 110 K h-1 during the first hour, a direct consequence of the elevated effective thermal diffusivity. The marginal gains between 20% and 30% loading were small relative to the step from 10% to 20%, consistent with a percolation-mediated conductivity transition in which a continuous high-conductivity network spanning the bed provides diminishing returns in conductivity with further addition while progressively reducing volumetric heat capacity.

Iron filings and SiC occupied an intermediate thermal performance regime [Figure 8C and D]. Iron filings exhibited steady, near-linear temperature evolution governed by their high volumetric heat capacity, reaching approximately 620 K under 30 vol% layered doping at t = 5 h. SiC achieved a marginally higher terminal temperature of approximately 645 K under the same loading conditions, attributable to its higher intrinsic conductivity relative to iron. Neither material displayed plateau behavior; temperature profiles remained monotonically ascending throughout the 5 h window. The absence of an isothermal window means that the TEG hot-side temperature drifts continuously during operation, introducing time-varying mismatch between the storage subsystem and downstream power conditioning electronics.

Copper turnings produced the highest absolute temperatures across all configurations tested [Figure 8E], reaching approximately 660 K at t = 5 h under 30 vol% layered doping. The early-phase rise from 300 K to around 550 K within the first 2 h is consistent with copper’s outstanding thermal conductivity of approximately 400 W m-1 K-1. Practical deployment of copper, however, raises non-trivial engineering concerns. The high material density (8,960 kg m-3) introduces a substantial gravimetric penalty, and progressive surface oxidation at sustained temperatures above 500 K may degrade interfacial thermal contact conductance over repeated charge-discharge cycles. These considerations collectively preclude copper turnings from further consideration despite its conductivity advantage.

Across all five dopant systems, layered configurations consistently outperformed their uniform counterparts at equivalent dopant fraction, with the performance disparity most evident at lower loadings. The dominant thermal resistance in the radial direction is concentrated in the outer annular shell, where the temperature gradient must drive outward heat flux to the TEG surface. By concentrating the high-conductivity dopant in this rate-limiting zone, the layered architecture reduces the thermal bottleneck while preserving thermal inertia of the inner core. Uniform mixing, by contrast, distributes the conductivity enhancement across the interior where its contribution to TEG-side heat delivery is attenuated by the 1/r dependence of radial heat flux in cylindrical geometry.

To quantify the extent of this architectural advantage, the total radial thermal resistance is decomposed into its inner-core and outer-annulus contributions using the cylindrical-shell formula R = ln(rout/rin)/(2πkL). For the 30 vol% Solar Salt formulation, the volumetric mixing rule [Equation (3)] gives keff = ϕsks + ϕdkd = 0.70 × 1.4 + 0.30 × 0.55 = 1.145 W m-1 K-1, which falls below the pure-sand value of 1.4 W m-1 K-1. In the uniform configuration, this reduced conductivity governs the entire radial domain; in the layered configuration, the inner core retains ks = 1.4 W m-1 K-1 while the composite is confined to the outer annulus. Using the vessel geometry (Ri = 0.025 m, Rc = 0.20 m, Ro = 0.30 m), the total radial resistance per unit length for the uniform case is Runif = ln(Ro/Ri)/(2πkeff) = 0.345 m K W-1, while the layered case yields Rlayer = ln(Rc/Ri)/(2πks) + ln(Ro/Rc)/(2πkeff) = 0.236 + 0.056 = 0.292 m K W-1, a reduction of approximately 15%. This outcome reflects a property specific to Solar Salt: because kd < ks, distributing the PCM uniformly penalizes conductive transport in the inner domain without any compensating latent-heat benefit there. Excluding Solar Salt from the inner core preserves the higher-conductance sand pathway over the greater part of the radial domain, while the outer-annulus resistance remains identical in both architectures. Beyond the conductive pathway, approximately 44% of the total Solar Salt mass in the uniform configuration resides in the inner domain (r < Rc), where phase-change absorption at 493 K proceeds remote from the TEG surface and cannot directly regulate T (Ro,t). In the layered configuration, all PCM volume is confined to the outer annulus, ensuring that the complete latent heat reservoir acts on the zone governing the TEG hot-side temperature, consistent with the formation of a near-isothermal band between 485 K and 500 K within the outer annulus. The 15% lower total radial resistance and the full spatial concentration of latent heat capacity at the TEG boundary together constitute the quantitative basis for the performance advantage of the layered architecture over the uniform configuration at equivalent dopant loading.

The COMSOL thermal field maps in Figure 8F and G provides spatial evidence for the mechanisms inferred from the TTEG (t) curves, comparing the pure sand baseline against the 30 vol% layered Solar Salt configuration at hourly intervals from t = 1 h through t = 5 h. In the pure sand baseline [Figure 8F], the temperature field at t = 1 h shows a steep radial gradient concentrated in the inner third of the domain, with the central heating element above 550 K while the outer annulus remains below 340 K. The low thermal diffusivity of quartz sand confines the thermal penetration front to a narrow region around the heat source. By t = 5 h, the TEG-side temperature reaches only approximately 420 K, confirming that internal conduction resistance, rather than external convective coupling, limits the rate of useful heat delivery.

The 30 vol% layered Solar Salt configuration [Figure 8G] shows a markedly different spatial evolution. At t = 1 h, the thermal front has already penetrated further into the outer annulus relative to the pure sand case, because the composite shell provides a lower-resistance pathway for radial heat transport. By t = 2 h, the temperature within the outer composite annulus has risen above 450 K with a notably shallower radial gradient than in the undoped baseline. Between t = 3 h and t = 4 h, the outer annulus traverses the Solar Salt melting range near 493 K, and the latent heat sink absorbs the incoming thermal flux without a corresponding temperature rise. The field map at t = 3 h reveals a nearly isothermal band within the outer shell, with temperature contours compressed into a narrow interval near 485 K to 500 K. By t = 5 h, phase change is largely complete, and the TEG interface receives heat through a composite layer whose temperature varies by less than 10 K across its radial extent, compared with more than 80 K variation across the same region in the pure sand baseline. The interior hot-spot temperature in the pure sand case exceeds 700 K at t = 5 h while the TEG surface reaches only 420 K, a 280 K internal mismatch representing stored energy that cannot be extracted within the charging window. In the layered Solar Salt configuration, the maximum interior temperature is lower (approximately 640 K) because enhanced radial transport draws heat outward more effectively, and the TEG surface temperature stabilizes near 495 K, reducing the internal mismatch to roughly 145 K.

The comparative analysis identifies 30 vol% layered Solar Salt as the preferred composite formulation for this platform. While copper turnings achieved the highest absolute TTEG (t), the operational objective of a sand battery coupled to thermoelectric generators is not to maximize peak temperature but to deliver a temporally stable thermal driving force over the full charging cycle. For a monotonically rising TTEG (t), as exhibited by copper, graphite, SiC, and iron filings, the continuous drift of the operating point generates a time-varying mismatch between the thermally optimal load resistance and any fixed downstream power conditioning circuit, reducing cycle-averaged electrical output below the theoretical maximum. The 493 K isothermal plateau furnished by Solar Salt directly resolves this mismatch: the latent heat of fusion absorbs input variability and re-emits stored energy at a near-constant temperature. The spatial field maps in Figure 8G confirm that this temporal plateau originates from a spatially coherent phase-change front propagating through the outer annulus, not from a cancellation of opposing gradients.

The choice of the layered over the uniform architecture at 30 vol% is further supported on thermomechanical grounds: confining the PCM to the outer annulus ensures that the inner core retains the mechanical integrity and dimensional stability of pure quartz sand, reducing the risk of thermally induced cracking near the heating element during repeated thermal cycling. Among PCM candidates that could provide a latent heat plateau within the target temperature window, Solar Salt is distinguished by its established industrial track record in CSP, its cost advantage relative to metallic or advanced ceramic fillers, and its demonstrated chemical compatibility with silica-based matrices at the temperatures of interest.

Interfacial thermal performance and thermo-mechanical reliability

The preceding sections established that the 30 vol% layered Solar Salt composite maximizes TEG-side thermal delivery among the candidate formulations investigated. However, the practical realization of this thermal advantage depends critically on the efficiency with which heat traverses the interface between the granular storage medium and the solid TEG substrate. This section presents a parametric analysis of the coupled effects of TIM thermal conductivity (kTIM = 1.0~10.0 W m-1 K-1) and mechanical contact pressure (Pcontact = 0.5~3.5 MPa) on thermal delivery efficiency, transient heat flux, interfacial temperature drop, thermomechanical stress distribution, and cyclic degradation behavior, with the objective of identifying the design envelope that simultaneously satisfies the thermal performance and structural durability requirements of the HEV sand battery module.

The seven panels of Figure 9 collectively demonstrate that thermal delivery efficiency and mechanical durability are governed by the interaction between TIM conductivity and contact pressure, and the following discussion traces the physical mechanisms and quantitative bounds of this coupling. The coupled influence of TIM thermal conductivity and mechanical contact pressure on the thermal delivery efficiency of the sand battery assembly is mapped in Figure 9A. The contour field reveals that ηdel increases monotonically with both kTIM and Pcontact, but the sensitivity is asymmetric: below kTIM ≈ 3.5 W m-1 K-1, efficiency gains are dominated by conductivity improvements, whereas above this threshold the marginal return from further conductivity enhancement diminishes and contact pressure becomes the controlling parameter. The baseline configuration (kTIM = 3.5 W m-1 K-1, Pcontact = 1.0 MPa) yields ηdel = 0.74, indicating that 26% of the input thermal energy remains inaccessible to the TEG interface at the end of the 5 h charging window. Increasing kTIM to 6.0 W m-1 K-1 at Pcontact = 2.0 MPa raises ηdel to 0.82, while the most aggressive configuration (kTIM = 10.0 W m-1 K-1, Pcontact = 3.5 MPa) achieves 0.89. The Pareto front extracted from the ηdel - Nf trade-off space traces a trajectory from the lower-left to the upper-right of the design map, confirming that no single parameter can be optimized in isolation without compromising either thermal performance or structural durability. The inset marginal profile at Pcontact = 2.0 MPa shows that ηdel saturates above kTIM6.0 W m-1 K-1, suggesting limited practical benefit from ultra-high-conductivity interface materials. This asymmetry is also reflected in the contour spacing of Figure 9A, where the iso-efficiency lines are closely spaced along the conductivity axis below 3.5 W m-1 K-1 and widen appreciably above it, while their spacing along the pressure axis remains comparatively uniform. The weak pressure dependence in this regime is consistent with the bounded influence of the constant contact-resistance assumption adopted in the model, and it identifies interface conductivity, rather than clamping pressure, as the parameter most worth optimizing once a moderate contact load has been secured.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 9. Parametric analysis of interfacial thermal performance and thermo-mechanical reliability. (A) Coupled effects of thermal conductivity and contact pressure on thermal delivery efficiency; (B) TEG-side temperature and instantaneous conversion efficiency under different contact pressures. Solid curves denote TTEG on the left axis, and dashed curves denote ηTEG on the right axis; the blue and yellow dashed curves correspond to Pcontact = 0.5 and 3.5 MPa, respectively; (C) Heat flux and cumulative delivered thermal energy under different TIM conductivities. Solid curves denote qTEG on the left axis, and dashed curves denote cumulative delivered thermal energy on the right axis; the blue and yellow dashed curves correspond to kTIM = 1.0 W m-1 K-1 and 10.0 W m-1 K-1, respectively; (D) Interfacial temperature drops as a function of TIM conductivity and contact pressure; (E) Radial stress distribution indicating edge stress concentration; (F and G) Cyclic degradation trajectories and comprehensive comparison balancing thermal efficiency and fatigue life. Panel (G) identifies the design point at kTIM = 6.0 W m-1 K-1 and Pcontact = 2.0 MPa as providing the optimal balance between thermal delivery efficiency and projected service life. TEG: Thermoelectric generator; TIM: thermal interface material.

The feasible design region for the structural containment is bounded by ηdel ≥ 0.74 and Nf ≥ 7,300 cycles (corresponding to the 20-year service horizon at one cycle per day). For the TIM joint, the fatigue criterion is applied differently: as a compliant gap pad at the accessible outer vessel surface, the TIM is replaceable during a planned maintenance shutdown, so its fatigue life governs the length of the servicing interval rather than the structural design life of the system. Superimposed isothermal contours of ΔTTIM provide a complementary perspective: configurations falling below the ΔTTIM = 20 K isoline maintain interfacial temperature drops comparable to or smaller than the TEG operating differential, whereas those exceeding 40 K suffer parasitic thermal losses that substantially erode conversion efficiency.

The transient TEG-side temperature histories at four contact pressures [Figure 9B] reveal that elevated contact pressure accelerates the thermal response, with the 3.5 MPa case reaching the Solar Salt phase-change plateau near 493 K approximately 0.8 h earlier than the 0.5 MPa case. The instantaneous TEG conversion efficiency, plotted on the secondary axis, increases with temperature differential and stabilizes during the isothermal plateau, confirming that the PCM buffering effect identified in the composite optimization study translates through the interfacial barrier to the TEG operating point. Figure 9C quantifies the corresponding heat flux delivered to the TEG substrate for four kTIM values at fixed Pcontact = 2.0 MPa. The kTIM = 10.0 W m-1 K-1 configuration sustains a terminal flux approximately 2.4 times that of the kTIM = 1.0 W m-1 K-1 case, and cumulative energy delivery over the charging window scales accordingly. The parametric sweep of ΔTTIM against kTIM [Figure 9D] confirms that only configurations with kTIM above approximately 5 W m-1 K-1 at Pcontact ≥ 2.0 MPa satisfy the 20 K target threshold across the full pressure range investigated.

The radial distribution of von Mises stress across the TIM joint [Figure 9E] exhibits a pronounced concentration at the outer perimeter (r/Ro > 0.85), where the CTE mismatch between the composite sand bed and the alumina substrate is mechanically constrained. The peak stress at Pcontact = 0.5 MPa reaches 62 MPa, exceeding the TIM ultimate tensile strength of 55 MPa, indicating that insufficient clamping pressure permits localized edge debonding. At Pcontact = 2.0 MPa, the peak stress reduces to 48.3 MPa (safety factor of 1.14), consistent with the fatigue life estimate of 8,400 cycles reported in the thermo-mechanical analysis. Higher contact pressures further suppress edge stresses but introduce compressive creep concerns not captured by the elastic model.

The long-term degradation trajectories of ηdel under cyclic thermal loading [Figure 9F] show that all four configurations exhibit an initial exponential decay followed by stabilization beyond approximately 5,000 cycles. The baseline configuration (kTIM = 3.5 W m-1 K-1, Pcontact =1.0 MPa) reaches 80% retention of its initial ηdel at approximately 8,400 cycles, consistent with the fatigue life prediction. The low-conductivity, low-pressure case (kTIM = 1.0 W m-1 K-1, Pcontact = 0.5 MPa) degrades below the 80% retention threshold before 5,000 cycles, rendering it unsuitable for the 20-year design window. The summary comparison across five representative configurations [Figure 9G] confirms that the optimized design point (kTIM = 6.0 W m-1 K-1, Pcontact = 2.0 MPa) provides the most favorable balance between thermal delivery efficiency and fatigue life, achieving ηdel = 0.82 with Nf ≈ 6,200 cycles. This 6,200-cycle life is lower than the 8,400 cycles obtained at the baseline interface (kTIM = 3.5 W m-1 K-1), and the difference is a direct consequence of the higher interface conductivity. Raising kTIM increases the heat flux delivered across the joint and therefore the absolute interfacial temperature sustained during each charge-discharge cycle, which enlarges the cyclic thermal-stress amplitude at the TIM perimeter and correspondingly reduces the fatigue margin. The gain in delivery efficiency and the reduction in fatigue life are thus two outcomes of the same increase in interfacial heat transfer, representing an inherent efficiency-durability trade-off. Although the kTIM = 10.0 W m-1 K-1 configuration attains the highest ηdel of 0.89, its fatigue life of 3,200 cycles falls below the 20-year threshold, excluding it from the feasible design region.

Taken together, the parametric results establish that interfacial thermal management constitutes a first-order design constraint for compact sand-based TES modules, comparable in importance to the bulk composite formulation. The thermal delivery efficiency of the assembly is governed not by a single interfacial property but by the coupled interaction between TIM conductivity and mechanical contact pressure, with diminishing returns in kTIM above approximately 6 W m-1 K-1 shifting the optimization burden to contact pressure control. The identification of a bounded feasible region in the kTIM - Pcontact space, constrained simultaneously by ηdel ≥ 0.74 and Nf ≥ 7,300 cycles, provides a quantitative basis for material selection and mechanical design of the interface joint. The optimized configuration (kTIM = 6.0 W m-1 K-1, Pcontact = 2.0 MPa) delivers 82% of the stored thermal energy to the TEG interface with a projected TIM fatigue life of approximately 6,200 cycles (~17 years). This value is below the 7,300-cycle structural threshold but reflects the distinct serviceability of the TIM layer: unlike the welded containment vessel, the gap pad is accessible at the outer surface and can be replaced in a single planned maintenance event, after which the assembly returns to its original thermal-mechanical performance state. The structural containment independently satisfies Nf ≥ 7,300 cycles at a safety factor of 2.18 (Section 3.3), so the 20-year system design horizon is maintained through one scheduled TIM replacement within the operating window. This configuration therefore represents the preferred operating point for subsequent prototype development within the HEV platform.

The thermal delivery efficiency of 0.82 achieved at the optimized interface condition can be compared with the experimentally measured performance of analogous packed-bed TES configurations. Trevisan et al. (2022) reported a maximum thermal efficiency of approximately 72% in a first-of-kind radial-flow packed-bed TES prototype tested at temperatures up to 700 °C, observing that non-uniform bed porosity adversely affected the thermal performance in the outer region of the bed[54]. The additional 10 percentage points recovered in the present study arise from the systematic co-optimization of TIM thermal conductivity and mechanical contact pressure, a coupled interfacial design dimension that has not been resolved in conventional packed-bed configurations and that the parametric mapping in Figure 9A identifies as the binding constraint above kTIM ≈ 6.0 W m-1 K-1.

Cyclic stress response and material-pair selection

Having established the thermomechanical modeling framework and the candidate material matrix in the preceding section, attention now turns to the quantitative response of the assembly under sustained cyclic operation and to the identification of a material pairing that reconciles mechanical reliability with thermal-shock resistance and capital cost. Figure 10 presents six complementary analyses - corresponding to the six panels (A) through (F) - applied across the nine insulation-shell material combinations to support the final material-pair selection.

Phase change doped sand storage for isothermal thermoelectric heat delivery

Figure 10. Cyclic stress response and material-pair selection. (A) Peak von Mises stress over 500 cycles; (B) radial stress and temperature profiles for Al2O3 + 304SS; (C) CTE design map with iso-lifetime contours; (D) Goodman-corrected fatigue margins; (E) multidisciplinary composite ranking across nine material combinations; (F) 2D stress field for the optimal ZrO2 + Inconel pairing. Panel (E) consolidates the multidisciplinary ranking across nine material combinations, confirming ZrO2 paired with Inconel 718 as the preferred selection on the basis of fatigue safety factor, CTE compatibility, and thermal shock resistance. CTE: Coefficient of thermal expansion.

Figure 10A tracks the peak von Mises stress at the insulation-shell interface over 500 charge-discharge cycles for the three retained pairings. All three curves exhibit a two-stage behavior: an initial transient softening during the first 20-40 cycles, followed by a quasi-stationary plateau. Al2O3 + 304SS settles near 240 MPa, driven by the 9.2 × 10-6 K-1 CTE mismatch, while Mullite+carbon steel (C-steel) and ZrO2 + Inconel stabilize at 165 MPa and 120 MPa, respectively. The shaded envelopes around each curve denote the ±3% cycle-to-cycle variation in peak stress recorded over the stabilized portion of the 500-cycle simulation, and therefore quantify the numerical scatter of the ratcheting solution at the plateau. The radial stress profile for the Al2O3 + 304SS baseline [Figure 10B] shows that σθ changes sign across the PCM-ceramic interface and reaches 260 MPa at the inner shell surface, where ceramic constraint and a 220 K temperature drop act in concert. The von Mises envelope peaks within the ceramic layer rather than at either interface, indicating that bulk ceramic failure, not interfacial debonding, is the limiting mechanism for this pair.

The CTE design map [Figure 10C] isolates the role of thermal expansion mismatch. Iso-lifetime contours at N = 3,650, 7,300, and 14,600 cycles delineate a narrow feasible corridor centered on αceramic ≈ 10 - 12 × 10-6 K-1 and αshell ≈ 11 - 14 × 10-6 K-1). Al2O3 + 304SS lies outside this corridor, whereas Mullite + C-steel and ZrO2 + Inconel fall within it, with the latter closest to the iso-stress minimum. The map assumes the reference geometry and excludes creep relaxation effects that would marginally expand the feasible region at elevated temperatures. Figure 10D quantifies the fatigue margin via the Goodman-corrected stress amplitude. The operating Sa for Al2O3 + 304SS (120 MPa) approaches the endurance limit of 230 MPa, yielding a safety factor of 0.89 that is unacceptable for a 7,300-cycle horizon. Mullite + C-steel returns 1.34, while ZrO2 + Inconel attains 2.18.

The composite ranking in Figure 10E integrates fatigue life, peak stress, capital cost, and ceramic thermal-shock resistance under the weighting (0.40, 0.30, 0.15, 0.15). ZrO2 + Inconel emerges as the preferred pairing despite its highest relative cost, owing to its low CTE mismatch, high ceramic fracture toughness (KIc = 8.0 MPa·m1/2), and the favorable cyclic-hardening exponent of Inconel 718. The 2D stress field for this optimal pairing [Figure 10F] confirms that the peak stress of 142 MPa localises at the top and bottom corners of the metallic shell near r4, where axial constraint intensifies the radial expansion mismatch, while no hot-spot is predicted at the ceramic-metal interface itself.

Taken together, these results establish that CTE compatibility, rather than absolute strength, governs the long-term viability of the multi-layer storage assembly under the imposed thermal cycle. The conventional Al2O3 + 304SS pairing, while adequate for short-duration prototypes, fails to meet the 20-year design horizon once realistic mean-stress corrections are applied. ZrO2 + Inconel satisfies all four selection criteria with a fatigue safety factor above 2, and its adoption shifts the governing failure mode from material fatigue to geometric stress concentration at the shell end-caps, a consideration that should guide the subsequent detailed design of closure welds and edge fillets.

The Goodman-corrected safety factor of 2.18 reported for the ZrO2-Inconel 718 configuration can be placed in perspective by reference to thermomechanical analyses of conventional TES containment published in the recent literature. Mishra et al. (2025) performed a validated coupled thermal-stress simulation of a commercial-scale molten salt storage tank constructed from standard 347H stainless steel and found that a single charge-discharge cycle was sufficient to drive the tank floor into the elastic-plastic regime, producing a peak von Mises stress of 107 MPa at the floor-wall junction with measurable plastic strain accumulation after just one thermal event; low-cycle fatigue and its interaction with creep were explicitly identified as unresolved concerns for long-duration service[55]. A parallel set of observations was reported by Xu et al. (2025), who showed in a molten salt packed-bed TES model that operational conditions favouring improved thermal discharge performance simultaneously push tank wall stresses toward structural failure thresholds, illustrating the inherent conflict between thermal and mechanical performance that arises when containment materials are selected without explicit consideration of CTE compatibility[52]. The present results suggest that this conflict can be substantially mitigated through material pairing rather than geometric reinforcement. The CTE mismatch for ZrO2 and Inconel 718 (Δα ≈ 2.5 × 10-6 K-1) is approximately 3.7 times smaller than that of the Al2O3 + 304SS combination evaluated and rejected in this study, and this difference in mismatch propagates directly into the threefold improvement in Goodman safety factor (2.18 vs. 0.89). The quasi-stationary peak von Mises stress of 120 MPa in the preferred pairing remains comfortably within Inconel 718’s high-cycle endurance limit over the full 7,300-cycle design life, a condition that the existing literature on both steel TES tanks and rock-bed packed systems has thus far been unable to satisfy without significantly restricting operational temperature range[29,52,55].

Table 5 consolidates the key design parameters, material selections, and quantitative performance outcomes across the three parallel investigations, providing a concise reference for practitioners adapting this framework to other household-scale TES configurations.

Table 5

Summary of optimal design parameters, materials, and performance metrics

Design module Parameter/material Optimal value or selection Key metric Notes
Composite formulation Dopant type Solar salt (60/40 NaNO3/KNO3) Isothermal plateau at 493 K; T stability within 10 K Only PCM dopant producing temporal buffering
Dopant volume fraction 30 vol% TEG-side T stabilizes ~495 K at t = 5 h Higher fractions impractical; diminishing returns above 30%
Spatial architecture Layered (functionally graded) Reduces radial thermal resistance in outer annulus Inner core: pure quartz sand; outer annulus: composite
Baseline (pure sand) TEG-side T - ~420 K at t = 5 h Reference trajectory
Interfacial design TIM thickness 0.1 mm ΔT across TIM = 40 K (baseline) Comparable to TEG operating differential
TIM thermal conductivity (optimized) kTIM = 6.0 W m-1 K-1 ηdel = 0.82 Gains marginal above 6.0 W m-1 K-1
Contact pressure (optimized) Pcontact = 2.0 MPa Peak von Mises stress = 48.3 MPa Below TIM tensile strength (55-65 MPa)
Thermal delivery efficiency ηdel = 0.82 82% of input energy reaches TEG surface Baseline: ηdel = 0.74
Projected TIM fatigue life Nf ≈ 6,200 cycles (~17 years) Within 20-year design horizon Goodman-corrected; continuum model lower bound; constitutes a scheduled maintenance interval, not system end-of-life; 20-year system life upheld by ZrO2 + Inconel 718 structural containment
Containment materials Insulation material Zirconia (ZrO2)     αceramic ≈ 10.5 × 10-6 K-1 Low CTE mismatch with inconel 718
Shell material Inconel 718     αceramic ≈ 13.0 ×10-6 K-1 Superior cyclic-hardening exponent
Peak von Mises stress (ZrO2 + Inconel) 120 MPa (quasi-stationary) Safety factor = 2.18 (Goodman) Al2O3 + 304SS: safety factor = 0.89 (unacceptable)
Projected structural life > 7,300 cycles (20 years) Power-law ratcheting extrapolation Experimental validation required beyond 1,000 cycles

Several limitations should be noted. The effective medium treatment homogenizes grain-scale heterogeneities and does not capture discrete particle rearrangement or local contact network evolution, phenomena that discrete element analyses have shown to contribute additional hoop stress on containment walls. The apparent heat capacity formulation smooths the phase-change front over a 10 K interval, which may underestimate the sharpness of the thermal plateau observed in physical systems. All thermomechanical results are derived from linear elastic constitutive models; creep relaxation at sustained elevated temperatures and progressive oxidation of metallic interfaces remain unresolved. The present work was conducted entirely through numerical simulation because the target operating conditions, involving temperatures up to 700 K sustained over thousands of thermal cycles within a sealed multi-material assembly, preclude meaningful characterization through bench-scale experiments without purpose-built instrumentation for in-situ interfacial temperature and stress measurement. The simulation-first approach enables rapid parametric exploration of a design space that would be prohibitively expensive to survey experimentally, while providing quantitative targets for subsequent prototype validation.

CONCLUSIONS

This study developed quantitative design criteria for compact, household-scale sand-based thermal energy storage coupled to thermoelectric generators, treating composite formulation, interfacial heat transfer, and cyclic thermomechanical reliability as a single coupled design problem. The results show that useful thermoelectric output depends on the temporal stability of the hot-side temperature rather than its peak value, and that only the functionally graded Solar Salt formulation supplied this stability through its phase-change plateau. They also show that the thin interface between the storage medium and the module is a first-order constraint rather than a secondary detail, because it sets the fraction of stored heat that reaches the conversion stage. For long-term durability, the compatibility of thermal expansion between the insulation and the containment shell proved more decisive than absolute strength, which is why zirconia paired with Inconel 718 was preferred over the conventional alumina and stainless-steel combination. Confirming these criteria in practice now rests on bench-scale measurement of the plateau behavior and interfacial heat flux, together with extended cycling tests capable of validating the long-term reliability projected here.

DECLARATIONS

Authors’ contributions

Made substantial contributions to conception and design of the study and performed data analysis and interpretation: Ding, Q.; Cui, W.

Performed data acquisition, performed COMSOL and ANSYS simulation: Liu, J.

Performed MATLAB visualization and figure generation: Ding, Q.

Contributed to writing of the harmonious ecovillage section: Zeng, L.

Provided administrative, technical, and material support: Song, C.; Zeng. L.; Cui, W.

Provided funding acquisition and study supervision: Cui, W.

Availability of data and materials

The simulation data and MATLAB scripts supporting the findings of this study are publicly available in the GitHub repository at: https://github.com/QiruiDING/Composite-Sand-Based-Thermal-Energy-Storage-with-Thermoelectric-Conversion.git.

AI and AI-assisted tools statement

During the preparation of this manuscript, the AI-based image generation tool Gemini 2.5 Pro (version 2.5 Pro Experimental, released 2025-03-25), developed by Google DeepMind, was used solely to produce the conceptual schematic diagrams presented in Figures 1 and 2. The visual content, all textual annotations, and the scientific meaning conveyed in these figures were defined entirely by the research team through explicit prompts and post-generation manual editing. The tool did not influence the study design, data collection, analysis, interpretation, or the scientific content of the work. All authors take full responsibility for the accuracy, integrity, and final content of the manuscript.

Financial support and sponsorship

This work was supported by the Scientific Research Funding Project of Westlake University (Grant No. WU2025A006)

Conflicts of interest

All authors declared that there are no conflicts of interest.

Ethical approval and consent to participate

Not applicable.

Consent for publication

Not applicable.

Copyright

© The Author(s) 2026.

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Phase change doped sand storage for isothermal thermoelectric heat delivery

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