1. Introduction
Recent advances in flexible sensing continue to expand design options for skin-interfaced sensors. Representative developments include tactile sensors [
1], large-deformation fabric sensors [
2], and adaptive polymer materials [
3]. Different forms of wearable sensors enable various thermal sensing platforms by leveraging microfabrication techniques and microscale thermal-fluid transport principles for noninvasive physiological assessment [
4,
5]. At the component level, such devices can be fabricated using microscale resistive heater traces patterned and etched on flexible printed circuit boards (F-PCBs) with total thicknesses below 100 μm. Commercially available 0201 NTC thermistors have dimensions of approximately 600 μm × 300 μm × 100 μm, providing microscale temperature-sensing elements compatible with these flexible platforms. Together, these miniaturized components can be integrated into soft, flexible microsystem architectures to enable wearable micro-thermal sensors that provide multiparameter physiological information with high precision and low power consumption [
6,
7].
Continuous and noninvasive monitoring of superficial skin and vascular conditions by wearable sensors is critical for the early detection of local physiological and pathological changes. Blood flow velocity is a key indicator of local perfusion and vascular function, and abrupt changes in blood flow may signal vascular complications such as stenosis, thrombosis, or impaired tissue viability [
8,
9]. Tissue thermophysical properties, including thermal conductivity and thermal diffusivity, are also important because they depend on tissue composition and water content and may change with skin dehydration, edema, inflammation, and other alterations in the local tissue environment [
10,
11,
12,
13,
14]. Therefore, accurate characterization of both blood flow and tissue thermophysical properties can provide valuable information about vascular and skin conditions. Conventional blood flow measurement techniques, such as Doppler ultrasound and photoacoustic imaging, can provide detailed vascular information but commonly rely on specialized or relatively bulky instrumentation, coupling media, and controlled probe positioning [
15]. Measurements of tissue thermophysical properties also generally require dedicated equipment and controlled measurement conditions. These limitations make conventional techniques difficult to use for convenient, long-term, and wearable monitoring.
To address these limitations, wearable micromachined thermal sensors offer a promising alternative for continuously assessing both vascular and tissue properties [
16,
17]. These sensors apply a controlled, low-level heat input to the skin surface. The resulting skin temperature response is then monitored as heat propagates through the tissue. In a static tissue environment, the applied heat dissipates solely via thermal conduction through the skin. When blood flows through an adjacent vessel, it acts as a convective medium that transports thermal energy along the direction of the flow. Existing wearable thermal devices generally employ either steady-state spatial temperature measurements or transient thermal analysis to characterize this conjugate heat transfer process [
8,
9,
18]. Steady-state spatial methods measure temperature differences around the heater, whereas transient methods analyze the time-dependent temperature decay. Tissue thermal conductivity
ks governs the ability of heat to diffuse through the tissue and determines its conductive thermal resistance, whereas blood velocity,
Vf, controls the capacity of flowing blood to dilute thermal energy. During active thermal measurements, conduction through the tissue and convective transport by the blood flow occur simultaneously, so the skin surface temperature response is jointly influenced by
ks and
Vf. Because conventional sensors cannot separate these two contributions, predictions of either parameter can be highly inaccurate.
Prior works have addressed this thermal coupling using various sensing strategies. Sequentially combined measurements of local tissue properties, vessel depth, and upstream–downstream temperature asymmetry have been used to estimate blood velocity and direction in superficial vessels [
9]. To determine background tissue properties before estimating blood flow, a separate tissue location was used, causing risks of location- and time-dependent property change [
10]. To infer blood velocity from temperature measurements, an analytical model incorporating heat conduction and convection was applied [
18]. However, its reliance on thermal conductivity obtained via blood flow occlusion adds operational complexity and introduces measurement errors. Transient hot-film and calorimetric methods have also been developed to improve sensitivity to high biofluid flow rates by analyzing peak temperature responses [
19]. In these vascular thermal flow sensing strategies, tissue thermal conductivity
ks is typically treated as a known material property, a separately calibrated parameter, or a preliminary measurement used to support subsequent flow estimation, rather than as a simultaneous prediction target together with blood velocity
Vf. Moreover, it remains unclear whether the measurement of temperature can jointly predict both parameters with acceptable accuracy. The decoupling of
ks and
Vf is critical to minimize the prediction error for accurate assessment of skin and vascular conditions. Furthermore, simultaneous measurement at one location saves the time and effort of patients and healthcare workers.
This paper describes the design and numerical investigation of a skin-interfaced thermal sensor consisting of a central heater and three in-line thermistors for simultaneous measurement of tissue thermal conductivity ks and blood velocity Vf. The thermal sensor is attached to the skin surface, with the three thermistors aligned along a blood vessel located 1.7 mm beneath the surface. The central heater on top of the blood vessel has a diameter of 4 mm and generates heat at a low power of 0.05 W. Three miniature thermistors measure the steady-state skin temperature at the heater center and at upstream and downstream locations along the flow direction. A three-dimensional finite element analysis (FEA) model of conjugate heat transfer in vascularized skin is developed to quantify parameter sensitivities and optimize the thermal sensor design. The model is further used to simulate steady-state temperature responses to various ks (0.20~0.40 W/(m·K)) and Vf (0.01~0.10 m/s). To measure ks and Vf directly from the thermal sensor readings, we establish two distinct prediction frameworks: a data-driven machine learning (ML) model and a physics-based reduced-order model (ROM) constructed from a thermal-resistance network. Both models are trained by FEA results and simultaneously predict ks and Vf based on inputs of thermistors’ temperature measurements. The relative prediction errors are typically below 4% for ks and 10% for Vf using the ML model and below 1% and 8% using the ROM.
3. Results
Figure 1 illustrates the configuration and operating principle of the proposed thermal sensor. The thermal sensor consists of a resistive heater and three thermistors, S
u, S
m, and S
d, positioned on the skin surface with a blood vessel 1.7 mm deep in the skin tissue, consistent with the relative deep wrist vein reported by Webb et al. [
9]. S
u measures the upstream skin temperature affected by environment and heater, S
d measures the downstream temperature affected by the blood flow dilution, and S
m in heater center measures the heater temperature. A constant heating power of 0.05 W is applied to generate a localized thermal perturbation in the tissue with a heat flux of 3.979 mW/mm
2. The resulting temperature field is jointly governed by heat conduction through the surrounding tissue and convective heat dilution by the blood flow. Tissue thermal conductivity
ks controls the lateral and vertical spreading of heat away from the heater and therefore influences the magnitude and spatial extent of the surface temperature rise. By contrast, blood flow transports heat along the vessel, producing a directional thermal response and a temperature difference between the upstream and downstream sensing locations. Convective heat transport increases the downstream temperature relative to the upstream temperature. The three-thermistor arrangement is designed to capture these different thermal transport characteristics. Therefore, the combined temperature measurements
Tu,
Tm, and
Td contain distinguishable information associated with
ks and
Vf, enabling the two coupled physiological parameters to be simultaneously determined using a single heating event.
Figure 2 shows the integrated framework to design, analyze, and evaluate the proposed thermal sensor. First, a three-dimensional FEA model was established to simulate heat transfer within the tissue and blood vessel, with tissue thermal conductivity
ks ranging from 0.2 to 0.4 W/(m·K), and blood velocity
Vf ranging from 0.01 to 0.10 m/s. The
ks range was centered on a representative tissue thermal conductivity of 0.3 W/(m·K), and the upper limit of
Vf was set at 0.10 m/s, consistent with reported peripheral venous velocities [
9,
23,
24]. For each parameter combination, the model calculated the temperatures
Tu,
Tm, and
Td at the three thermistor locations, thereby generating a temperature-parameter dataset for evaluating the thermal sensor response. Two complementary approaches were then developed to predict
ks and
Vf from the three thermistor temperatures. In the machine learning approach, the FEA-generated dataset was used to train and evaluate candidate regression models. A cubic polynomial regression model with ridge regularization was selected to establish the prediction algorithm from
Tu,
Tm, and
Td to
ks and
Vf. This data-driven approach captures the nonlinear relationships between the three thermistor responses and the two target parameters. In parallel, a physics-based reduced-order model was constructed to elucidate heat transfer mechanisms by a thermal-resistance network including heat conduction through the tissue, convective heat transfer to the blood flow, lateral heat spreading between sensing regions, and heat loss to the environment. The thermal resistances and velocity-dependent parameters were calibrated and validated using the FEA results. The ROM therefore provides both a computationally efficient prediction method and a physical interpretation of how
ks and
Vf influence the measured temperatures. The ML and ROM approaches use the same three thermistor temperatures but determine
ks and
Vf through fundamentally different representations of the heat transfer process. Their predictions were compared with the corresponding FEA ground-truth values. Agreement among the ML, ROM, and FEA results evaluates not only the predictive models but also whether the proposed thermal sensor provides sufficient and distinguishable thermal information for simultaneously determining tissue thermal conductivity and blood velocity.
To evaluate the thermal response and optimize the configuration of the thermal sensor, a three-dimensional steady-state FEA model was developed in COMSOL Multiphysics 6.2. The model couples heat conduction in the tissue with convective heat transport by blood flow, thereby representing the dominant heat transfer processes of the physical system. The parameters used in the FEA model are summarized in
Supplementary Table S1.
Figure 3 shows the geometric configuration of the FEA model and the layout optimization of the thermal sensor. The thermal sensor was positioned above a subsurface blood vessel and consisted of a circular heater with a radius of 2 mm and three thermistors with a radius of 0.5 mm. The modeled tissue domain had a length of 50 mm, a width of 20 mm, and a height of 10 mm. The vessel had a radius of 1.3 mm and its center was located 1.7 mm beneath the tissue surface, resulting in a minimum tissue thickness of 0.4 mm between the vessel wall and the skin surface [
9]. Heat from the thermal sensor must conduct through the tissue before blood convection, leading to strong conjugate heat transfer between the surface heater and the blood flow. S
m was located at the heater center, and S
u and S
d were positioned upstream and downstream of the heater along the vessel axis. The locations of S
u and S
d were optimized by maximizing the absolute sensitivity of the differential temperature to blood flow velocity, that is, |d(
Td − T
u)/d
Vf|. As shown in
Figure 3D, the sensitivity increases as the downstream thermistor is positioned closer to the heater, because S
d more effectively senses the temperature field affected by blood flow convection. However, placing S
u sufficiently far upstream reduces the direct influence of the heater and provides a relatively stable upstream reference temperature. The sensitivity analysis located a point-based optimum at
dSu = 6.3 mm and
dSd = 2.0 mm, with a maximum sensitivity of approximately 13.45 °C/(m/s). The search range started at 2 mm, corresponding to the heater radius, because candidate sensor positions inside the heater footprint were excluded from the layout optimization. The point-based optimum cannot be implemented directly because each thermistor has a finite radius of 0.5 mm and must be offset from the 2.0 mm heater edge to avoid direct thermal contact with the heater. The downstream distance was therefore set to
dSd = 2.7 mm, which leaves a 0.2 mm clearance between the heater edge and the thermistor edge of S
d. The upstream distance was relaxed to
dSu = 6.0 mm to accommodate the sensor footprint and component spacing. At the selected sensor-center locations, the point-based sensitivity is 10.4 °C/(m/s), indicating that the configuration remained within the high-sensitivity region identified under the specified optimization conditions. In the implemented sensor model, the temperatures were averaged over the 0.5 mm radius thermistor areas.
Figure 4 shows the FEA results of temperature responses of the three thermistors for various
ks and
Vf. The middle-sensor temperature
Tm decreases monotonically as
ks increases from 0.20 to 0.40 W/(m·K), as shown in
Figure 4A. A larger
ks reduces the vertical and lateral conductive resistances beneath the heater, allowing the input heat to spread through a larger tissue volume more efficiently. Increasing
Vf also lowers
Tm, but it produces a smaller and nearly parallel shift in the temperature curves, with negligible influence on the curve slope.
Figure 4B analyzes the sensitivity of
Tm to
ks and shows that d
Tm/d
ks is negative and changes from −36 to −11 °C/(W/(m·K)). As
ks increases, the sensitivity magnitude decreases because the same increment in
ks produces a progressively smaller fractional reduction in conductive resistance. The sensitivity curves for different
Vf nearly overlap, meaning the shape and slope of the
Tm response are affected mainly by
ks, which makes the heater-centered thermistor suitable for determining tissue thermal conductivity. The differential temperature
Td − T
u reflects blood velocity, decreasing from 1.8~2.1 °C at
Vf = 0.01 m/s to 0.8~1.0 °C at
Vf = 0.10 m/s in
Figure 4C. At low flow, the blood cannot remove heat effectively and the downstream region near the heater is heated more strongly. As
Vf increases, enhanced convection removes heat and reduces
Td. The magnitude of d(
Td −
Tu)/d
Vf decreases from 32~37 to 3~4 °C/(m/s) as blood velocity increases in
Figure 4D, showing blood convection saturation while conduction through the tissue becomes dominant. The overlapped curves for different
ks confirm that
Td −
Tu is predominantly flow sensitive.
Figure 5 shows cross-sectional temperature fields for selected
ks and
Vf. In every case, the maximum temperature occurs directly beneath the heater, and the temperature decreases rapidly at depth. The vessel remains close to the 37 °C inlet temperature and acts as a heat sink beneath the heated surface. At
ks = 0.20 W/(m·K), heat remains confined near the heater, producing the highest local temperature. Increasing
ks to 0.40 W/(m·K) lowers the maximum temperature and diffuses heat over a wider tissue region because both vertical and lateral conduction are enhanced. The effect of
Vf is less obvious in the cross-sectional thermal profile than the effect of
ks, because blood convection transports energy primarily along the vessel axis, which is normal to the displayed plane. The results demonstrate that the heater-centered temperature reflects a strong conductivity response, and a longitudinal upstream–downstream measurement is needed to characterize the flow response.
Figure 6 shows the temperature fields along the blood flow direction and the thermal wake that does not appear in the cross-sectional view. At low
Vf of 0.01 m/s, weak blood convection reduces heat transfer and causes high temperature near the heater region. Increasing
Vf to 0.05 and 0.10 m/s increases convective heat transfer, lowers the downstream tissue temperature, and shortens the region affected by the heater. The strongest velocity-dependent temperature change therefore occurs between the heater and
Sd, rather than at the upstream location. Increasing
ks lowers the surface maximum temperature for every velocity and conducts heat farther into the tissue. This conductivity effect changes the magnitude of the local temperature field but does not change the flow-induced directionality. The side-view fields therefore show that the velocity dependence is confined to the downstream region, while the conductivity dependence acts over the entire heated area.
Figure 7 shows the corresponding skin surface temperature profiles. At
ks = 0.20 W/(m·K), the heater region has the highest temperature and the hot spot is confined within the heater, due to weak thermal conduction. As
ks increases, the peak temperature decreases and the surface temperature gradient becomes smoother because heat spreads laterally away from the heater efficiently. The temperature change is directly measured by S
m, which is located near the center of the conductivity-dependent hot spot. Blood flow mainly changes the temperature field on the downstream side of the heater. At low
Vf, heat remains in the vessel-coupled region and produces a higher temperature near S
d. At high
Vf, the blood dilutes more heat, reducing the downstream surface temperature and the difference in
Td −
Tu. The temperature at S
u has negligible change because the thermistor is located far upstream of the heater. In summary, the temperature profiles from FEA simulations show that
ks affects the magnitude and spatial spreading of the surface heater significantly, and
Vf affects the longitudinal asymmetry greatly, forming the physical foundation to apply
Tm and
Td −
Tu for simultaneous measurements of tissue thermal conductivity and blood velocity.
The distinct dependence of the three thermistor temperatures on
ks and
Vf, as established by the above FEA results, provides the basis for data-driven parameter estimation by an ML algorithm. Each FEA case associates a temperature triplet [
Tu,
Tm,
Td] with a known parameter pair [
ks,
Vf]. Supervised regression utilizes these paired data to learn a temperature-to-parameter mapping by minimizing the error between model predictions and FEA ground truth. Once trained, this mapping enables
ks and
Vf to be estimated from thermistor temperatures measured by the thermal sensor. Seven candidate regression models were evaluated using shuffled five-fold cross-validation. Third-order polynomial ridge regression produced the lowest mean normalized root-mean-square error and was therefore selected. During model training, the three temperature inputs were standardized and transformed into third-order polynomial features containing nonlinear and interaction terms. The coefficients were estimated by ridge regression, which applies L2 regularization. L2 regularization adds a penalty based on the sum of the squared regression coefficients to the model loss, thereby discouraging excessively large coefficients, reducing overfitting, and improving model stability. For each prediction, the measured temperature triplet was standardized using the training-set mean and standard deviation, transformed into the same polynomial feature space, and passed to the fitted regression model to obtain predictions of
ks and
Vf. Candidate-model settings and cross-validation performance are summarized in
Supplementary Table S2.
The generalization performance of the selected model was further evaluated using 30 independently simulated off-grid FEA cases that were not included in model training or selection. None of these parameter combinations coincided with the original full-factorial grid, and the fitted model was kept fixed, without retraining or model reselection, throughout the validation. The selected model achieved
R2 values of 0.99976 for
ks and 0.99424 for
Vf on the 30 independent off-grid FEA cases, demonstrating high predictive accuracy for previously unseen parameter combinations within the investigated domain. Complete validation metrics and bootstrap 95% intervals are provided in
Supplementary Table S3.
Figure 8 shows the ML predictions of
ks and
Vf from
Tu,
Tm, and
Td. The predicted
ks values at various blood velocities match well with the ground-truth FEA simulations, with only slight deviations at low thermal conductivities in
Figure 8A. The ML-predicted
Vf values are also validated by FEA simulations in
Figure 8B. These results show that the third-order polynomial model is able to accurately predict the coupled
ks and
Vf from the three temperatures collected from one thermal sensor measurement rather than requiring separate measurements for each parameter. The relative prediction error maps in
Figure 8C,D show the distributions of ML prediction accuracy across various combinations of
ks and
Vf. Prediction errors in
ks are low over most combinations and are relatively high near the conductivity and velocity boundaries, where polynomial interpolation in ML algorithm is supported by fewer neighboring cases. Prediction errors in
Vf are also low through the interior of the domain but become larger at low velocity. Because relative prediction errors are normalized by
Vf, a similar absolute deviation produces a larger percentage error at
Vf = 0.01 m/s. The largest relative prediction errors of the ML model, 5.58% for
ks and 21.92% for
Vf, both occur at the same corner case of
ks = 0.20 W/(m·K) and
Vf = 0.01 m/s, where the prediction lies simultaneously at the lower bound of both parameter ranges and the percentage error is amplified by the small denominator. Excluding such isolated corner cases, the relative prediction error remains below 4% for
ks predictions and below 10% for
Vf predictions. These results demonstrate that the ML model can simultaneously predict the two coupled parameters from the three thermistor temperatures with good agreement with the FEA reference over the interior of the parameter space.
To further investigate the conjugate heat transfer mechanism in tissue and blood flow, the thermal-resistance network is built to describe heat conduction from the thermal sensor to the tissue, blood convection, and environment heat loss in
Figure 9. The three thermistor locations are represented by surface nodes u, m, and d. The heater supplies
Q = 0.05 W at node m, and lateral conductive resistances connect the heater region to the upstream and downstream regions. Each surface node also transfers heat to the ambient environment through air natural-convection loss resistance. At nodes m and d, heat is divided between two parallel paths of tissue and vessel blood. In the vessel-coupled path, heat first conducts through the tissue layer above the vessel and is then transferred by blood convection. In the bypass path, additional heat conducts around the vessel and dissipates into deeper tissue. At node m,
Rspread connects the measured heater temperature
Tm to the effective subsurface temperature
T’m. This resistance accounts for the additional temperature rise created when heat spreads from the finite heater area into a larger tissue volume. The network represents the major conductivity dependence by conductive and spreading resistances and the major flow dependence by the blood convective resistances. Increasing
ks decreases the lateral, vertical, bypass, and spreading resistances, reducing
Tm significantly. Increasing
Vf increases the Nusselt number and heat transfer coefficient, thereby changing the downstream temperature
Td. Tu is a measured reference, while
Tm and
Td reflect the conduction- and flow-dependent responses. The thermal-resistance network clearly demonstrates different heat transfer pathways in the complex thermal-fluid scenario and establishes the foundation for ROM heat transfer analysis.
Figure 10 compares the ROM-calculated temperatures with FEA simulations across full
ks and
Vf ranges. The detailed ROM formulation and calibration procedure are provided in
Supplementary Section S1.
Tm derived by ROM closely matches the FEA results in
Figure 10A, and similarly good agreement is observed for
Td in
Figure 10B.
Figure 10C shows the calibrated parameter
cd for the downstream convective resistance at node d.
cd is a function of
Vf1/2 and increases with velocity, indicating that downstream convective heat transfer strengthens as
Vf increases. This nonlinear dependence is associated with the development of the local boundary layer and blood convective transport near the downstream sensor.
Figure 10D further shows that the ROM predicts the nonlinear decrease in
Tm with
ks at
Vf = 0.01 m/s as an example.
Figure 10E shows
Td decreases with
Vf at
ks = 0.30 W/(m·K), calculated by both ROM and FEA methods.
Figure 10F summarizes the ROM calculation error of
Tm and
Td compared with FEA results. The calculation errors are narrowly distributed around 0 °C, with magnitudes within only a few hundredths of a degree Celsius.
Figure 10 demonstrates that the ROM is sufficiently accurate as a forward model, which provides the basis for using it to determine
ks and
Vf from thermistor temperature measurements.
Figure 11 shows the ROM predictions of
ks and
Vf derived from the three thermistor temperatures
Tu,
Tm, and
Td.
Figure 11A,B compare the ROM-predicted
ks and
Vf with the FEA ground-truth values. The predicted
ks values closely follow the 1:1 line throughout the investigated range, demonstrating that the ROM accurately recovers tissue thermal conductivity from the temperature measurements. The predicted
Vf values also show good overall agreement with the FEA reference, although the dispersion around the 1:1 line becomes more obvious at higher flow velocities.
Figure 11C,D show the relative prediction error distributions of the ROM predictions across the
ks − V
f parameter space. The relative prediction error in
ks remains below 1% throughout the investigated domain, indicating consistently high prediction accuracy with limited dependence on blood flow velocity. The relative prediction error in
Vf remains low over most of the parameter space but increases near the parameter boundaries and at higher flow velocities, reaching up to 8%. The increased
Vf prediction error at high flow velocities is consistent with the reduction in thermal sensitivity when convective heat transfer becomes strong and thermal convection resistance is less dominant than tissue thermal conduction. At high flow velocities, a given change in
Vf produces a smaller temperature response, making the inferred
Vf more susceptible to small temperature errors. These results demonstrate that the ROM can use the three thermistor temperatures to simultaneously predict
ks and
Vf with high accuracy. In addition to providing a computationally efficient prediction method, the physics-based ROM explicitly relates the measured thermal sensor temperatures to conductive heat spreading in the tissue and convective heat transfer by blood flow.
Figure 12 compares the prediction performance of the ROM and ML models and provides an overall evaluation of the proposed thermal sensor design to measure tissue thermal conductivity and blood velocity.
Figure 12A,B show the
ks and
Vf predicted by the two models and compare the predictions with FEA ground-truth values. Both models accurately predict
ks and
Vf over the investigated range, with the prediction points following the 1:1 line. However, differences between the two methods become more evident from the absolute prediction deviations shown in
Figure 12C,D. As shown in
Figure 12C, the ROM has smaller prediction errors in
ks than the ML model across the investigated conductivity range. The improvement is particularly significant near the lower
ks boundary, where the ML model shows greater prediction errors. This result indicates that the physical constraints incorporated into the ROM provide robust prediction of tissue thermal conductivity because the ROM is less susceptible to the data-driven boundary effects that degrade the ML predictions near the edges of the training parameter space. For
Vf prediction,
Figure 12D shows that the two models exhibit different prediction error characteristics. The ROM provides small deviations at low flow velocities, but the deviation gradually increases as
Vf increases. In contrast, the ML model generally maintains smaller deviations over the intermediate-to-high flow range, although it shows greater deviations in low flow conditions. The increasing ROM deviation at high
Vf is associated with the reduced temperature sensitivity under conduction resistance dominant conditions. The ML model more flexibly captures the nonlinear temperature–flow relationship, resulting in improved
Vf prediction at higher velocities.
More importantly, the agreement between the two fundamentally different prediction frameworks supports the feasibility of the proposed thermal sensor configuration. The ROM represents the sensor response using physically defined conductive and convective thermal resistances, whereas the ML model learns the temperature-to-parameter relationship directly from the FEA dataset. Despite these different representations, both models successfully distinguish the effects of tissue thermal conductivity and blood flow velocity from a single set of three thermistor measurements. Because the two models employ different physical representations and modeling assumptions, their agreement indicates that the simultaneous prediction capability arises from the complementary thermal information captured by the thermal sensor layout rather than from a specific prediction algorithm. The ROM provides physical interpretability and higher accuracy in predicting ks, whereas the ML model provides greater flexibility in capturing the nonlinear flow response.