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Development and Experimental Validation of an Unglazed Photovoltaic-Thermal Collector Modelica Model that only needs Datasheet Parameters Lone Meertens1* Jelger Jansen1Lieve Helsen1,2 1Faculty of Engineering Science, Department of Mechanical Engineering, KU Leuven, Belgium. *Corresponding author : [email protected] 2EnergyVille, Thor Park 8310, 3600 Genk, Belgium. Abstract This work introduces the first validated, user-friendly, and accurate open-source photovoltaic-thermal (PVT) collector model in Modelica, tailored for system-level simulation and optimization. Current state-of-the-art PVT collector Modelica models are largely limited to oversimplified, steady-state representations that fail to capture the dynamic thermal behavior inherent to real PVT systems. A comprehensive Modelica model is developed based on the ISO 9806 standard (test method for the quasi-dynamic thermal performance of solar thermal collectors), coupled with an electrical system model through an internal heat transfer coefficient. The model calibration relies exclusively on manufacturer datasheet parameters, thereby eliminating the need for parameter estimation from measurement data. The model is validated using experimental results from an unglazed PVT collector, demonstrating strong agreement for various (weather) conditions. The findings highlight that, while steady-state models may suffice for conventional solar thermal collectors (STCs), accurate PVT modeling necessitates a dynamic approach, particularly for the thermal aspects. The electrical output of the PVT collector is less sensitive to transient effects. In addition to the model formulation and validation, this work presents a user-friendly automated calibration method based on manufacturer data, and critically addresses the limitations and potential trade-offs of using exclusively datasheet-derived parameters, thereby providing a transparent tool for PVT system simulation, design, and optimization within the open-source IDEAS library. Keywords: Photovoltaic-thermal (PVT) solar collector, Modelica, PVT model validation, PVT model calibration, manufacturer datasheets 1 Introduction Physics-based system models are key for addressing the challenges of climate change and the transition towards decarbonized energy systems. These models play a key role in the effective deployment of renewable energy sources (RES) such as photovoltaic (PV), solar thermal collectors (STC), and photovoltaic-thermal (PVT) systems, enabling optimal system design and control. PVT collectors, also known as hybrid solar collectors, simultaneously convert solar radiation into electricity and heat. A key distinction exists between glazed and unglazed PVT collectors: glazed collectors often prioritize thermal efficiency, while unglazed collectors, due to their lower operating temperatures, can enhance electrical efficiency. This paper focuses on unglazed (so-called WISC1) PVT collectors, which consist of a PV module coupled with a heat exchanger and may include rear insulation to reduce heat loss. Variants without insulation perform particularly well under sub-ambient conditions, making them suitable as heat sources for heat pump systems. The unglazed collectors are typically classified according to their rear insulation and heat transfer characteristics (Lämmle et al. 2020). The favorable market conditions for unglazed PVT designs further demonstrate their relevance in various urban and industrial energy contexts (Kramer, Amrizal, et al. 2020). Modeling approaches in the PVT field range from highly accurate, detailed, component-level models to simplified methods designed for integrated system performance assessment within a broader energy context. Although Modelica is a powerful modeling language for developing interdisciplinary simulation models, no validated open-source Modelica PVT model currently exists that captures the full dynamic thermal behavior while accounting for the thermal-electrical coupling. This paper addresses this gap by presenting a novel Modelica PVT collector model, validated using experimental data from unglazed PVT collector. Moreover, the PVT model relies solely on publicly available manufacturer data, avoiding complex calibration procedures for which measurement data are needed. 2 Background The IEA SHC Task 60 “Application of PVT Systems” (2018–2020) has played a central role in evaluating PVT technologies by focusing on system operation, collector testing, system-level simulation, and global performance assessment (IEA SHC 2018). One of its key objectives 1Wind and/or infrared sensitive collectors
was to identify scenarios in which PVT systems provide added value compared to separate PV and solar thermal installations. To facilitate the integration of PVT systems into simulation environments and ensure broader adoption, Task 60 stresses the need for standardized input parameters that guarantee the “processability” of technical data for tools like TRNSYS, Polysun, Modelica, and SCenoCalc (Kramer, Amrizal, et al. 2020). This standardization is crucial due to potential variations in testing procedures among manufacturers (market fragmentation), making consistent component-level characterization essential. Therefore, Task 60 recommended the application of international standards, specifically ISO 9806 (ISO 9806 2013) for the thermal aspect and IEC 60904 for the PV component. To incentivize the use of these standards, established certification frameworks such as the Solar Keymark (ESTIF/SKN n.d.) utilize and promote them, with targeted extensions to address the hybrid interactions between electrical and thermal components. This includes specifying the operational mode of electricity generation, such as maximum power point (MPP) tracking or opencircuit (OC), as required by ISO 9806 (2013) which has been identified by Hofmann et al. (2010) as highly influential on the thermal output. Existing PVT collector models can generally be categorized into (1) those requiring detailed design data and parameter estimation, and/or (2) simplified models based on datasheet parameters. Stegmann et al. (2011) developed a datasheet-based simulation model for unglazed, liquid-cooled PVT collectors, relying solely on standard test procedures and OC-tested datasheet parameters within the TRNSYS environment. In contrast, Lämmle (2018) proposed both a collector-level model in Modelica capable of capturing the detailed optical, electrical, and thermal energy flows using detailed manufacturer data, and a system-level model in TRNSYS that assesses overall performance based on empirical efficiency curves. Other approaches focus on parameter identification of ISO 9806 parameters using measurement data: Jonas et al. (2019) presented a detailed implementation and validation procedure within TRNSYS, while Veynandt, Klanatsky, et al. (2023) extended this work using data-driven grey-box models in MATLAB. Additionally, Kang (2021) developed a Modelica-based PVT model for district heating applications, but they didn’t provide any implementation details. These existing models present several limitations: some are not implemented in Modelica, others lack sufficient implementation details, and many rely on parameter estimation of ISO 9806 parameters, requiring extensive measurement data. The work presented here offers an alternative by providing a Modelica-based PVT collector model that combines a high-fidelity physical representation with the simplicity of datasheet-only inputs. The electrical operation of a PVT collector differs from standard PV IEEE rating schemes due to the influence of heat transfer fluid (HTF) flow and the resulting temperature distribution across the PV cells (Herrando, Markides, and Hellgardt 2014; Lämmle 2018; Brottier 2019; Jonas et al. 2019). Similarly, the electricity generation mode (MPP/OC) impacts the thermal behavior of the PVT collector (Hofmann et al. 2010). The existing equations describing the thermal and electrical performance, used as the starting point in this paper, are presented in Section 2.1 and 2.2, respectively. 2.1 Thermal modeling The thermal part of a PVT collector is similar to a STC. Similarly, a good efficiency requires both effective solar absorption and efficient heat transfer to the HTF (Zondag 2008). Different mathematical models are used to describe the thermal performance of liquid heating collectors, depending on the collector type (glazed or unglazed) and the test method (steady-state or quasi-dynamic). ISO 9806 defines a steady-state model for glazed liquid-heating solar collectors, widely adopted in both testing and simulation. Its useful thermal power output is calculated by Equation 1 ˙ Qth AG =η0,hem G−a1(θm−θa)−a2(θm−θa)2,(1) where ˙ Qth is the useful thermal power output (W), AG is the collector area (m2), η0,hem is the zero-loss (optical) efficiency for hemispherical irradiance (–), Gis the global irradiance on the collector plane (Wm−2), θmand θaare the mean HTF and ambient air temperatures (K or ◦C). a1 and a2are the linear and quadratic heat-loss coefficients (Wm−2K−1and Wm−2K−2, respectively). For unglazed collectors under steady-state conditions, wind-speed and long-wave effects must be included. One convenient formulation replaces Gby a net solar irradiance G′′, which integrates the long-wave irradiance: ˙ Qth AG =G′′hη0,hem (1−bu)−(b1+b2u)θm−θa G′′ i,(2) with G′′ =G+ε αEL−σ θ4 a(3) Here, buis the collector efficiency coefficient (wind dependence) (sm−1), b1is the linear heat-loss coefficient (Wm−2K−1), b2is the wind-speed dependence of the heat-loss coefficient (Wsm−3K−1), uis the wind speed, ELis the long-wave irradiance (Wm−2) , and σis the Stefan–Boltzmann constant. To capture both unglazed/glazed types and transient effects, the quasi-dynamic model adds a thermal capacitance, dependence of direct (Gb) and diffuse (Gd) radiation via incidence-angle modifiers (Kb,Kd), and explicit wind/infrared terms: ˙ Qth AG =η0,bKb(θL,θT)Gb+η0,bKdGd−c1(θm−θa) −c2(θm−θa)2−c3u(θm−θa) +c4EL−σ θ4 a−c5 dθm dt −c6uG.(4) The quasi-dynamic model extends the steady-state form by including coefficients c1and c2, linear and quadratic
heat-loss terms analogous to a1,a2in Equation 1, with units Wm−2K−1and Wm−2K−2;c3and c6, representing wind-speed dependence of heat losses and zero-loss efficiency, with units Jm−3K−1and sm−1;c4, the sky temperature dependence of the heat-loss coefficient (-); and c5, the effective thermal capacitance, with unit Jm−2K−1. Equations 1–4 were originally developed for STCs, but are commonly applied to describe the thermal behavior of PVT systems, as no dedicated PVT testing standard currently exists. Depending on the test method (unglazed) steady-state or quasi-dynamic, manufacturer datasheets list all coefficients needed to solve the corresponding equation that gives the collector’s thermal output under specific operational and ambient conditions. Due to the strong coupling between thermal and electrical performance in PVT systems, the thermal coefficients should ideally be determined under MPP conditions. If testing is performed under OC conditions, the solar irradiance must be corrected to account for the electrical power that would be extracted under MPP operation, as outlined by Lämmle (2018). 2.2 Electrical modeling In PVT collectors, the electrical performance is highly sensitive to the temperature of the PV cells, which is influenced by the thermal coupling between the PV layer and the HTF in the STC. A low thermal resistance between the PV cells and the HTF is essential to avoid excessive PV cell temperatures, which degrade both electrical and thermal efficiency (Zondag 2008). This section focuses on two key aspects: the calculation of electrical yield using performance ratios, and the modeling of the PV(T) cell temperature, which plays a central role in determining the electrical output. 2.2.1 Electrical yield The general form of the electrical power output from a PVT collector is given by Equation 5 Pel AG =ηPV ·PRtot ·G,(5) where ηPV is the electrical efficiency at nominal conditions (–), PRtot is the overall instantaneous performance ratio (–), and Gis the global solar radiation on the PVT plane (W). The typical loss mechanisms affecting the electrical performance of PV and PVT systems are detailed and summarized in Kramer, Amrizal, et al. (2020), with their corresponding performance ratios PRIAM,PRG,PRT, PRCand PRIdenoting incidence-angle modifier losses, irradiance-related losses, PV cell temperature losses, ohmic (cable) losses and inverter efficiency losses, respectively. In this work, only the temperature-related performance ratio PRTis explicitly modeled. All other losses are grouped into a single lumped loss factor, as discussed in Section 3.1.3. The temperature dependence of the electrical efficiency is calculated following the approach by Skoplaki and Palyvos (2009) as formulated in Equation 6 PRT=1−β·(Tcell −Tnom),(6) where βis the temperature coefficient of power for the PV cells (%K−1), Tcell is the PV cell temperature, and Tnom is the nominal cell temperature under standard test conditions. 2.2.2 PV cell temperature An essential step in assessing PV efficiency and electrical yield is determining the PV cell temperature, since higher temperatures reduce performance (see Equation 6). In PV modules, cell temperature follows the module’s steadystate temperature (Lämmle 2018), whereas in PVT collectors it is governed by the HTF temperature. Solar radiation absorbed by a PV cell is partly converted to electricity; the remainder is dissipated to the ambient, influenced by wind speed, ambient temperature, and irradiance. Mounting-type-dependent cell-temperature models are reviewed in Maier et al. (2023). A simple PVT estimate equates TPV to the fluid outlet temperature Tfluid,out (Brottier 2019), as implemented in tools such as Polysun. A more accurate method extends the Hottel–Whillier–Bliss equation with a PV–fluid heattransfer coefficient UAbsFluid (Florschuetz 1976; Zondag 2008; Jonas et al. 2019). Based on Lämmle (2018) and Jonas et al. (2019), the model couples the ISO 9806 quasi-dynamic thermal collector (Equation 4) with a two-node PV performance formulation (see Section 3.1.1), linking the PV cell and the HTF via UAbsFluid (Wm−2K−1) to yield the celltemperature relation in Equation 7 Tcell =Tm+˙qth UAbsFluid ,(7) where ˙qth is the specific thermal power output of the collector (Wm−2), and Tmis the mean HTF temperature (K), calculated as the average of the HTF inlet and outlet temperatures, Tin and Tout respectively. In principle, UAbsFluid can be calculated from the series combination of the absorber-to-pipe conductive resistance, characterized by the conductive heat transfer coefficient UAbsPipe, and the pipe-to-fluid convective resistance, characterized by the convective heat transfer coefficient UPipeFluid, based on the collector geometry, material properties, and operational conditions (e.g., fluid flow rate) using analytical models or finite-element (FEM) simulations (Kramer, Amrizal, et al. 2020). However, for most commercial PVT collectors, the absorber-specific parameters required for such detailed modeling are not readily available, as only standardized test reports or manufacturer data are typically accessible. In such cases, an approximate approach needs to be applied. Stegmann et al. (2011) developed an approach for unglazed PVT collectors, using thermal parameters extracted from OC tests. Lämmle (2018) similarly proposed a procedure for glazed PVT collectors that derives UAbsFluid from standard MPP
test data using a makeshift procedure. In this work, the glazed and unglazed parameter estimation methods are integrated in the Modelica model, such that UAbsFluid can be derived solely from manufacturer datasheet parameters for MPP tested collectors, including wind-speed dependence. Details of this method are given in Section 3.1.2. 2.3 Novelty of the work Existing PVT modeling approaches (Lämmle 2018; Jonas et al. 2019) provide robust frameworks for simulating PVT systems. However, these models typically rely on detailed parameter identification procedures or proprietary datasets, often requiring experimental calibration, finite element modeling, or surface temperature measurements. While such methods can yield high accuracy, they limit accessibility and replicability for broader research and system simulations, hinder transparent product comparisons, and ultimately restrict the market uptake of PVT technology. Furthermore, existing simplified (non-validated) Modelica models often fail to capture the full dynamic thermal behavior of PVT systems and do not adequately integrate the coupling between thermal and electrical components. For instance, Stegmann et al. (2011) proposed a simplified model based on datasheet parameters, but this model is not implemented in Modelica and is strictly limited to unglazed PVT collectors, as it relies on the steadystate ISO 9806 formulation for unglazed collectors (see Equation 2) rather than the more general quasi-dynamic approach. In summary, the current literature regarding PVT modeling has two main research gaps: (1) the absence of a PVT model that leverages only publicly available datasheet parameters thereby eliminating the need for unavailable or proprietary measurement data, and (2) the absence of a comprehensive Modelica model that accurately represents the full dynamic thermal behavior of PVT systems while incorporating thermal-electrical coupling. In this work, a novel Modelica-based PVT collector model is introduced and validated with experimental data from unglazed PVT collectors. Unlike previous approaches, the proposed model relies solely on datasheet parameters, thereby eliminating the need for complex calibration procedures. Moreover, the model’s performance is critically assessed, highlighting its limitations and comparing its accuracy against methods based on detailed parameter estimation. 3 Model development In this section, the methodology used to develop, implement, and validate the novel PVT collector model is presented. In Section 3.1, the underlying modeling framework is detailed while in Section 3.2, the metrics employed to assess model accuracy are discussed. 3.1 PVT collector model The PVT collector model consists of two coupled submodels—thermal and electrical—which are detailed in Sections 3.1.1–3.1.3. To account for the changing HTF temperature along the lenght of the collector, the model is discretized into nSeg segments along the flow path. Each segment is solved in a coupled thermal–electrical loop. For clarity, the core segment index is omitted in the equations presented in the following subsections. 3.1.1 Thermal performance To model the thermal behavior of PVT collectors, a two-node, one-capacitance network is adopted (schematically presented in Figure 1), extending the ISO 9806 solar-thermal formulation. An internal heat transfer coefficient UAbsFluid couples the mean HTF temperature node Tmand the absorber (PV cell) temperature Tcell. All physical heat capacities (fluid, absorber, frame, insulation) are lumped into an effective thermal capacity ceff, which is assigned to the mean HTF temperature Tm(Fischer and Müller-Steinhagen 2009). Physically, this means that the thermal inertia of the entire collector system is at one uniform temperature Tm. The Tm-node energy balance is formulated by Equation 8 ceff dTm dt =˙qrad −˙qloss −˙qth,(8) where ˙qrad are radiative gains (Wm−2), ˙qloss conduction/- convection losses (Wm−2), and ˙qth the useful thermal output per area (Wm−2). Rearranging Equation 8 and substituting the radiative gain and loss terms from Figure 1 yields: (1) the steady-state ISO 9806 model (Equation 1), by setting ceff =0 and including only the blue terms. (2) the quasi-dynamic ISO 9806 model (Equation 4), by retaining ceff and adding the red wind-speed and sky-temperature terms. The ISO 9806 thermal network model (dashed lines in Figure 1) is available in the open-source IBPSA Modelica library for simulating STC behavior (Wetter et al. 2019), where it is based on a simplified version of the quasi-dynamic ISO 9806 model (Equation 4) with c3= c4=c6=0, thus neglecting wind and sky-temperature dependencies. This existing implementation serves as the starting point for the PVT collector model developed in this work. To extend its validity to unglazed collectors, wind-speed and long-wave loss terms are inFigure 1. Two-node, one-capacitance thermal network for PVT collectors (ISO 9806: dashed lines; extension: solid lines).
corporated, resulting in the quasi-dynamic formulation (Equation 4), which captures the effects relevant for unglazed PVT thermal operation (Stegmann et al. 2011; Fischer and Müller-Steinhagen 2009). Compared to a two-node, two-capacitance network2, this two-node, single-capacitance approach is ISO-compliant, simpler, and directly uses standardized parameters—and has been demonstrated as the preferred method for the PVT collectors investigated by Jonas et al. (2019). The specific thermal output is calculated as: ˙qth =˙mcp(Tout −Tin) AG ,(9) where ˙mis the mass flow rate (kgs−1) and cpthe HTF specific heat capacity (kJkg−1K−1). 3.1.2 Thermal–electrical coupling Both numerical and experimental approaches can be used to determine UAbsFluid for a specific absorber design. However, the absorber-specific parameters required by these methods are rarely available for commercial PVT collectors, where test reports and datasheets are usually the only information source. PVT models that rely on parameter estimation typically fit UAbsFluid alongside other thermal and electrical parameters. Since this work aims to develop an accurate PVT model based solely on datasheet inputs, a datasheet-based derivation of UAbsFluid is proposed by merging two established approaches. Stegmann et al. (2011) derived UAbsFluid from OC-mode thermal tests (including wind-speed dependence) making it valid for unglazed collectors. Lämmle (2018) generalized this to MPP-mode glazed collectors but they omitted wind effects. The MPP-mode approach is preferred because the electrical operating point significantly influences thermal performance; if only OC-mode parameters are available, the corresponding MPP coefficients can be obtained via the conversion procedure of Lämmle (2018), which properly accounts for the coupling between electrical and thermal losses and avoids physically incorrect simplifications (Kramer and Helmers 2013). Combining these two methods yields a unified, wind-dependent formulation using MPP datasheet coefficients: UAbsFluid =(τα)eff −η0,elc1+c3u+b1,el (τα)eff −η0,el−1−c6 η0,th uη0,th .(10) Here (τα)eff =0.901 for unglazed PVT collectors as reported in Lämmle (2018), and the electrical temperaturedependence coefficient is given by b1,el =|β|Gnom, where βis the temperature coefficient in %K−1and Gnom = 1000 Wm−2. When computed across varying wind speeds u, the resulting UAbsFluid values should remain approximately constant, serving as a consistency check on the datasheet parameters (Stegmann et al. 2011). 2Some PVT models introduce a second capacitance linked to Tcell to represent the thermal inertia of the PV panel, but this additional capacity cannot be determined using typically available manufacturer data. 3.1.3 Electrical performance The electrical output power Pel is calculated using the PVWatts V5 formulation (Dobos 2014) as presented by Equation 11 Pel =Pnom G Gnom 1+γ(Tcell −Tnom)(1−Ploss),(11) where Pnom is the module’s rated DC power under standard test conditions (Gnom =1000 Wm−2,Tnom =25 ◦C), Tcell is the PV cell temperature from the two-node thermal model (Equation 7), and Ploss is a constant system loss factor covering soiling, shading, mismatch, wiring and connection losses, inverter inefficiency, light-induced degradation (LID), and availability (Dobos 2014). The term 1+γ(Tcell −TSTC)in Equation 11 explicitly accounts for the temperature-dependence of the electrical efficiency, similar to the performance ratio formulation in Equation 6. All remaining losses are merged into a system loss factor (Ploss). In this study, panels are assumed unshaded with negligible soiling, yielding a Ploss of 9 % per Dobos (2014). Given PVT 2’s higher positive electrical output tolerance (up to +5 % vs. +3 % for PVT 1; see Table 1), its loss factor is reduced to 7 %. 3.2 Error analysis Model validation is performed against the measurement data (Section 4) by comparing both instantaneous power and cumulative energy for the thermal and electrical outputs. Instantaneous errors are quantified using the mean absolute error (MAE) and root mean square error (RMSE), while cumulative deviations are evaluated over the full dataset. For a scale-independent assessment, normalized MAE (nMAE) and normalized RMSE (nRMSE) are also computed. The MAE and nMAE between simulated and measured outputs are defined by Equation 12 and Equation 13 respectively. MAEY=1 n n ∑ i=1 |Ysim(ti)−Ymeas(ti)|,(12) nMAEY=MAE 1 n∑n i=1|Ymeas(ti)|.(13) The RMSE and nRMSE are defined by Equation 14 and Equation 15 respectively. RMSEY=s1 n n ∑ i=1 (Ysim(ti)−Ymeas(ti))2,(14) nRMSEY=RMSE 1 n∑n i=1|Ymeas(ti)|.(15) Where, Yrepresents either the thermal power output ˙ Qth or the electrical power output Pel, depending on the context.
Table 1. Datasheet parameters for the two PVT collectors. Parameters PVT 1 PVT 2 Electrical Agross (m2)1.66 1.64 β(%K−1)-0.41 -0.375 Pmax (Wp)280 (0/+3 %) 300 (0/+5 %) η0,el (%)16.87 18.3 Thermal c1(Wm−2K−1)7.411 10.74 c2(Wm−2K−2)0 0 c3(kJm−3K)1.7 1.1 c4(−)0.437 0.363 c5(Jm−2K−1)42200 22100 c6(sm−1)0.003 0.036 η0,th (%)0.475 0.535 4 Collector data and test sequences Experimental data from two different unglazed PVT collecors, provided directly by the authors of the respective studies, are used for validation and are briefly summarized below. The first dataset (PVT 1) was obtained from experimental measurements on an outdoor test bench at the Laboratory for Solar Energy Systems of the University of Applied Sciences (HTW Saar) in Saarbrücken, Germany. In this case, the PVT collector is an uncovered collector that features a rear cover and thermal insulation on the back of the absorber. A detailed description of this dataset and the corresponding test setup is provided in Jonas et al. (2019). The experimental measurements cover the typical days3as defined in ISO 9806 and include both standard thermal performance measurements and continuous recordings of the relevant electrical values. The second dataset (PVT 2) was obtained from the real operation of a flat-plate, uncovered, and uninsulated PVT collector on a test bench in Austria. This dataset spans 58 summer days (from July 11 til September 6) with a 5-second sampling interval. The data, which is publicly available, is described in detail in Veynandt, Inschlag, et al. (2023). A selection of the measured variables from this dataset has previously been used in the development of a grey-box PVT model (Veynandt, Klanatsky, et al. 2023). Table 1 lists the datasheet parameters describing the thermal and electrical behavior of both collectors. The thermal coefficients follow the quasi-dynamic (general) test method, following Equation 4. For PVT 2, the thermal coefficients were originally obtained under the unglazed steady-state method (Equation 2) and then converted to quasi-dynamic form (Equation 4) following the approach detailed in Solar Keymark Network (2019). 3Day type 1: η0-conditions, mostly clear sky conditions.Day type 2: Elevated operating temperature or η0-conditions, partly cloudy conditions including broken cloud and clear sky conditions.Day type 3: Mean operating temperature conditions including clear sky conditions.Day type 4: High operating temperature conditions including clear sky conditions. As both datasets did not contain all data required to do a (one-to-one) validation of the model presented in Section 3.1, some assumptions had to be made. First, for PVT 1, the measured long-wave irradiance on the tilted plane was found to be unreliable, necessitating the estimation of long-wave radiation losses from the effective sky temperature. Only the solar irradiance components on the tilted plane were measured. Estimating cloud cover (and thus sky temperature) requires horizontal-plane irradiance data to determine the diffuse fraction. In the absence of such data, the diffuse fraction is assumed identical across all orientations. This assumption affects the sky temperature estimate and, consequently, the modeled long-wave radiation losses. Second, for PVT 2 the total irradiance on the tilted collector plane is used directly in the simulation following Equation 2; accordingly, no conversion of the datasheet value for η0,hem is necessary. 5 Results and analysis This section is organized as follows: Section 5.1 validates the thermal and electrical performance against the measurement data introduced in Section 4, both in terms of instantaneous power and cumulative energy. Sections 5.2 and 5.3 examine how thermal and electrical parameters affect the model’s accuracy. 5.1 Model validation The accuracy of the PVT collector model is assessed against the two datasets introduced in Section 4, using only the datasheet coefficients from Table 1 to set up the PVT collector model. The evaluation of PVT 1 is based on Table 2 and Figure 3, while PVT 2 is assessed using Figure 2. The sole model parameter not directly provided in the datasheet, namely the overall absorber-fluid heat transfer coefficient UAbsFluid, is computed for each PVT collector using Equation 10. As discussed in Section 3.1.2, Stegmann et al. (2011) argue that similar UAbsFluid values across different wind speeds is indicative of robust datasheet parameters. In our case, both datasets exhibit a pronounced variation of UAbsFluid with wind speed, suggesting a possible inconsistency in the wind-dependent coefficients c3and c6. For the reference scenario, the wind-independent UAbsFluid values for PVT 1 and PVT 2 are 32.76 Wm−2K−1and 56.85 Wm−2K−1, respectively. Section 5.3 will further explore how the choice of UAbsFluid affects the accuracy of the predicted electrical power output. Table 2 reports the error metrics (introduced in Section 3.2) for PVT 1. For day types 1 to 3, thermal performance shows acceptable agreement between model and measurements, with energy deviation (∆E) remaining below 5 %. In contrast, day type 4 shows a significantly higher deviation of 36.7 %, indicating model limitations under high temperature difference and low irradiance conditions (see Figure 3(d)). These discrepancies likely stem from underestimated wind-dependent losses (coefficients c3and c6) and increased radiative losses due to the larger
HTF-to-ambient temperature difference. As the absolute thermal output is low in this case, model limitations have a stronger effect, leading to disproportionately large relative deviations. While the MAE and RMSE are lowest under clear-sky conditions, larger errors during variablesky periods (type 2 and type 4) point to a mismatch in the dynamic response of the thermal model, involving the c5 coefficient. Additionally, the use of a sky temperature approximation introduces uncertainty in the long-wave loss term c4, as noted in Section 4, and warrants closer examination. Electrical performance validation of PVT 1 yields normalized MAE and RMSE values below 3.1 % (Table 2), confirming the accuracy of the electrical component of the PVT collector model. Figure 2. Top: Error between the measured and simulated daily thermal and electrical energy production of the PVT 2 collector, expressed in kWhd−1, over the entire dataset. Bottom: Corresponding average wind speed during operation for each day, with high wind speed periods ( ¯u>2.5m/s) indicated by the grey sections. For PVT 2, Figure 2 compares measured and simulated daily thermal and electrical energy alongside average wind speed, and Table 2 summarizes the key error metrics. Figure 2 indicates a clear correlation between thermal energy mismatch and higher wind speeds, suggesting further investigation of the wind-dependent coefficients c3 and c6. Over the full validation period at 5-s resolution the thermal model predicts 20.4 kWh vs. 13.4 kWh measured (∆E= +53.1%), but this large error is driven by many periods of negative thermal output that would not occur in real operation. Filtering to Qth,sim(Qth,meas)>0 yields a more realistic energy error of ∆E= +6.85% (−4.7%). Electrical predictions remain robust (MAE: 3.2 W, ME: –1.8 W, ∆E=−2.9%, 83.8 kWh predicted vs. 86.3 kWh measured) and are essentially unaffected by wind speed. 5.2 Thermal parameters Thermal performance is first examined for PVT 1 under controlled conditions, followed by an assessment of deviations for PVT 2 including high wind speed operation. PVT 1: standard test conditions Analysis is based on four representative day types (Figure 3), spanning clear to overcast skies with mean HTF–ambient temperature differences of 0 K (types 1–2), 10 K (type 3) and 20 K (type 4). An artificial blower maintained a constant wind speed of 3 ms−1to 4 ms−1, such that wind effects remain uniform across cases. The stacked loss distributions represent the individual heat loss contributions within the quasi-dynamic thermal model (Equation 4), each defined by a specific datasheet coefficient. The impact of these loss terms on thermal performance is examined in the remainder of this section. The heat-loss coefficients c1and c2are excluded from further discussion due to their negligible influence on model accuracy under the given operating conditions. Wind-speed dependence (c3,c6). In this study, wind speeds during all day type measurements (Figure 3) remained within 3 ms−1to 4 ms−1, placing them at the upper edge of the ISO calibration range (0–3.5 m/s) and calling the accuracy of the wind-dependent coefficients into question. The persistent steady-state error across all day types indicates an underestimation of c6, which is significant even for day types 1–2 where c3has limited impact due to small θm−θa, while c3becomes more influential at larger temperature differences. These findings suggest that convective losses do not scale linearly beyond the calibration range. Sky-temperature dependence (c4). The c4term accounts for radiative heat losses based on the difference between ambient air and sky temperature, expressed as EL−σ θ4 a. This term is typically negative, with values around −100Wm−2for clear skies, −50Wm−2under hazy conditions, and approximately zero for overcast skies (ISO 9806 2013). In this work, the sky temperature for PVT 1 is approximated according to the assumptions in Section 4, which may introduce steady-state errors in the long-wave loss term and affect the accuracy of the thermal simulation. Thermal capacity (c5). ISO 9806 limits uncertainty in HTF heat capacity to ±10 %, yet quasi-dynamic identification often yields larger deviations (Weißmüller, Frenz, and Krämer 2012), attributable to limited variation in HTF temperature during standard tests. Calculations based on material properties and ISO weighting factors can reduce this uncertainty (Lämmle 2018). However, identified values may still fail to capture rapid irradiance transients (Stegmann et al. 2011). In this study, the datasheet c5is too large, slowing the model’s thermal response (Figure 3) and causing notable errors during fast-changing conditions. Reducing c5would sharpen transients but exacerbate steady-state bias, indicating that adjustment of c5 alone cannot resolve the dynamic mismatch. Comparison with quasi-dynamic identification. For day types 1–2, underestimation of steady-state losses leads to overestimated thermal output, implicating the skytemperature term c4and/or the wind-dependent term c6. A similar bias occurs in types 3–4, but larger θm−θa elevates the influence of c3, while the model’s slower transient response points to an overestimated thermal capacity c5. Compared to the parameter set identified by Jonas et al. (2019), the datasheet coefficients differ by
Table 2. Model validation results for PVT 1 and PVT 2. Computations use a 3-segment discretization, datasheet parameters, a loss factor of 9 % for PVT 1, and 7 % for PVT 2. For PVT 1, UAbsFluid =32.76Wm−2K−1; for PVT 2, UAbsFluid =56.85Wm−2K−1. Thermal Performance MAE (W) nMAE (%) RMSE (W) nRMSE (%) ME (W) Esim (kWh) Emeas (kWh) ∆E(%) PVT 1 (Day type 1) 18.5 3.33 20.4 3.66 18.5 3.73 3.61 3.33 PVT 1 (Day type 2) 91.5 18.8 132.2 27.1 10.7 3.06 2.99 2.19 PVT 1 (Day type 3) 58.4 19.9 92.5 31.6 12.2 2.33 2.23 4.17 PVT 1 (Day type 4) 97.4 85.7 151.2 133.0 41.7 0.78 0.57 36.7 PVT 2 10.7 111.2 33.9 352.9 5.10 20.4 13.4 53.1 PVT 2 (Qth,sim >0) 43.1 30.8 66.9 47.8 9.57 26.6 24.9 6.85 PVT 2 (Qth,meas >0) 35.2 21.0 52.1 31.2−7.86 25.5 26.8−4.7 Electrical Performance MAE (W) nMAE (%) RMSE (W) nRMSE (%) ME (W) Esim (kWh) Emeas (kWh) ∆E(%) PVT 1 (Day type 1) 1.04 0.49 1.36 0.64 0.91 1.00 1.00 0.43 PVT 1 (Day type 2) 4.30 2.48 5.34 3.08 3.72 1.14 1.11 2.15 PVT 1 (Day type 3) 2.80 1.61 3.43 1.97 2.35 1.29 1.27 1.35 PVT 1 (Day type 4) 3.26 1.98 3.88 2.36 2.78 0.86 0.84 1.69 PVT 2 3.21 5.18 6.11 9.86 −1.80 83.8 86.3−2.91 (a) Day type 1 (b) Day type 2 (c) Day type 3 (d) Day type 4 Figure 3. Comparison between simulated and measured thermal output and losses for different day types. Each subfigure shows: Top: thermal output ˙qth (model vs. measurements); Middle: temperature difference θm−θaand solar irradiance; Bottom: simulated thermal loss contributions and total loss. A single common legend (identical across day types) is displayed in day type 4.
∆c3=−1.4%,∆c4=63.1%,∆c5=11.5%,and ∆c6= −90.3%. The strong negative bias in c6, partly offset by a positive bias in c4, highlights that model limitations peak under high wind speeds, as further illustrated by the thermal behavior of PVT 2. PVT 2: high wind conditions As shown in Figure 2 and discussed in Section 5.1, the model systematically overestimates the thermal output of PVT 2, particularly under higher wind speeds. The collector frequently operates near its upper temperature limit, with a mean HTF-to-ambient temperature difference of 19.52 K, which is suboptimal for unglazed PVT collectors. This condition, resulting from the test setup described in Veynandt, Inschlag, et al. (2023), leads to phases of low or even negative thermal output. While not representative of typical operation, this validation is valuable for exposing model limitations. The pronounced overestimation under high wind conditions (occasionally exceeding 10 ms−1) suggests that the wind-dependent coefficients c3and c6do not scale linearly beyond the calibrated range. This effect is exacerbated by the uninsulated rear side of the collector, increasing its sensitivity to convective losses. Additionally, the use of a varying mass flow rate, differing from the (nominal) one used for datasheet coefficient determination, may contribute to discrepancies. Because these effects primarily affects convective heat transfer and potentially electrical performance, they will be addressed in Section 5.3. 5.3 Electrical parameters As discussed in Section 2.2.2, the PV cell temperature strongly affects the electrical efficiency of a PVT collector (see Equation 6). To account for the influence of thermal operation on the PV cell temperature, a thermal coupling between the PV cell and the HTF is introduced via the coefficient UAbsFluid, which is formulated in Equation 7. In this work, UAbsFluid is estimated using a simplified, datasheet-based method (Section 3.1.2). This section examines the impact of variations in the estimated UAbsFluid on the accuracy of the modeled electrical power output. Figure 4. Mean electrical error versus UAbsFluid for Pnom = 300 W and 315 W. Filled markers denote the estimated (datasheet-based) value of UAbsFluid. Figure 4 shows the normalized mean error in electrical output versus variations in UAbsFluid for two nominal powers: Pnom =300W and 315 W (reflecting a +5% tolerance; see Table 1). A constant system loss factor of 9% is applied throughout (Equation 11). As shown, a shift in UAbsFluid has minimal effect under good thermal coupling, while the grey band, representing uncertainty from rated power tolerance and assumed Ploss, causes greater deviation. The trend observed in Figure 4 aligns with Lämmle (2018), who found that values above 60 Wm−2K−1indicate good coupling, with little gain beyond. Hence, a simplified datasheet-based UAbsFluid suffices for accurate output predictions. Making it mass-flow dependent adds complexity without meaningful accuracy gains, as constant values already yield reliable results. 5.4 Model limitations The following limitations apply primarily to unglazed PVT collectors: (1) High wind speeds: convective losses (coefficients c3,c6) are increasingly underestimated above the ISO calibration range (≈3.5ms−1); (2) Dynamic response: thermal capacity (c5) may be misestimated, impacting the model’s transient behavior under rapidly varying irradiance. Glazed PVT collectors are not affected by (1) but remain subject to (2); this hypothesis should be investigated in future work. 6 Conclusion and future work By offering an open-source, modular, and transparent modeling framework, this work sets a significant step toward democratizing high-fidelity PVT system simulations, thereby empowering researchers, engineers, and policymakers to optimize PVT systems without relying on proprietary tools or inaccessible data. Validation against two experimental datasets demonstrated that the electrical sub-model achieves very good accuracy, with the nMAE and nRMSE both below 3.1 % for PVT 1 (day types 1–4) and 5.2 % / 9.9 % for PVT 2. The thermal model reproduces daily energy within 3.3 %, 2.2 %, 4.2 % and 36.7 % for PVT 1 day types 1–4, respectively, and 6.85 % for PVT 2 (excluding negative thermal output periods). These results confirm that, except under extreme conditions, the simplified datasheet-based approach yields reliable predictions. Limitations arise primarily for unglazed collectors for high wind speeds, where convective and radiative losses are not fully captured. Future work should validate glazed PVT collectors, whose insulation and higher operating temperatures may mitigate the limitations identified for unglazed systems. For unglazed collectors, investigations into non-linear convective formulations could better characterize the wind-dependent loss coefficients c3and c6. Refining the sky-temperature approximation is also needed to reduce steady-state radiative errors. Finally, embedding this PVT model within full energy-system simulations (e.g., district heating networks or building HVAC models) would enable end-to-end optimization of hybrid solar technologies across diverse climates and applications.