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Machine learning to predict plasma-based CO2 conversion in dielectric barrier discharge reactors

Jiayin Liab, Xinpei Luc, Pranav Arund, Jing Xue, Fausto Galluccid, Sirui Li*d and Annemie Bogaerts*ab
aResearch Group PLASMANT and Center of Excellence PLASMA, University of Antwerp, Department of Chemistry, Antwerp, 2610, Belgium. E-mail: annemie.bogaerts@uantwerpen.be
bElectrification Institute, University of Antwerp, Olieweg 97, 2020 Antwerp, Belgium
cSchool of Electrical and Electronic Engineering, Huazhong University of Science and Technology, Wuhan, Hubei 430074, China
dDepartment of Chemical Engineering and Chemistry, Eindhoven University of Technology, Eindhoven 5612, AZ, the Netherlands. E-mail: S.Li1@tue.nl
eSchool of Electronic Information and Communications, Huazhong University of Science and Technology, Wuhan, Hubei 430074, People's Republic of China

Received 19th February 2026 , Accepted 11th May 2026

First published on 14th May 2026


Abstract

Plasma-based CO2 conversion is an emerging defossilization technology that converts a potent greenhouse gas into valuable chemical feedstocks, yet its optimization is hampered by complex nonlinear behavior and resource-intensive experimentation. In this work, we collected a comprehensive database, comprising 358 data points with six key operational and geometric parameters, published in literature between 2010 and 2025. Leveraging this dataset, we developed a hybrid machine learning (ML) model integrating physics-informed neural network (PINN), random forest (RF) and extreme gradient boost (XGB) algorithms to predict CO2 conversion and energy efficiency (EE) in dielectric barrier discharge (DBD) reactors. Under a rigorous group 5-fold cross-validation (CV) protocol, the ensemble consistently outperformed all individual models, with the best-fold model achieving an R2 of 0.791. Error-correlation analysis revealed that the ensemble weights adapt to the pairwise error correlation structure: PINN consistently provides complementary information, while RF and XGB, being largely interchangeable, are selected according to their individual performance. When applied to prospective experimental validation, the hybrid model achieves an R2 of 0.92 on unseen data within the explored domain, and it eliminates unphysical predictions in data-sparse regimes, yielding strictly non-negative CO2 conversion estimates. SHapley Additive exPlanations (SHAP) analysis further identified flow rate and power as the dominant input features, collectively accounting for 61%–71% of the model's predictions. This work establishes a robust and interpretable framework while quantifying the generalizability of ML models in heterogeneous data environments, offering a practical tool to accelerate plasma-based gas conversion optimization.



Green foundation

1. This work presents a robust and interpretable machine learning (ML) model to predict plasma-based CO2 splitting performance from a diverse literature dataset comprising 358 data points, quantitatively assessing model generalizability across heterogeneous experimental sources.

2. Our hybrid model integrating physics informed neural network, random forest and extreme gradient boost algorithms achieves an R2 of 0.92 on prospective experimental validation while eliminates unphysical predictions on CO2 conversion in data sparse regimes.

3. Future studies may focus on advanced ML models development through standardized databases with descriptors including discharge characteristics and when relevant, catalyst properties as well as integration of physics informed architectures to enhance predictive power in plasma-based gas conversion, thereby reducing reliance on extensive experimental campaigns and improving resource efficiency.


1. Introduction

Carbon dioxide (CO2), a major greenhouse gas driving global climate change, necessitates the urgent development of strategies for its mitigation and valorization. Converting CO2 into valuable products is a cornerstone of this effort, yet it is fundamentally challenged by the molecule's high thermodynamic stability, which demands significant energy input for activation. Plasma technology has emerged as a compelling solution to this problem.1 By generating a partially ionized gas rich in high-energy electrons, reactive radicals, and excited species, plasma can cleave the stable C[double bond, length as m-dash]O bond under mild conditions. Notably, non-thermal plasma (NTP) systems, powered by electricity, offer rapid dynamic control and excellent compatibility with intermittent renewable power sources.2,3 These advantages position NTP as a key enabling technology for power-to-X (P2X) applications, providing a promising and sustainable pathway for CO2 conversion within future energy systems.4,5

Various plasma types have been studied for plasma-based CO2 conversion.6,7 Dielectric barrier discharge (DBD) reactors have attracted particular attention due to their simple design, user-friendly nature, compatibility with catalysts, and potential scalability.1 Reported CO2 conversion and energy efficiency (EE) values vary widely across studies, even under nominally similar operating conditions, because reactor performance emerges from the coupled effects of discharge power, gas flow rate, electric-field distribution, and reactor geometry.8,9 Importantly, these relationships are highly nonlinear and often non-monotonic, with improvements in conversion frequently accompanied by losses in EE. Traditional process optimization approaches in this field rely heavily on computationally expensive physics-based simulations or resource-intensive experiments. Mechanistic modelling, while providing valuable insights,10,11 is sometimes constrained by uncertain kinetic parameters or high computational costs for systematic parameter screening. Conversely, purely experimental optimization faces the curse of high dimensionality: the vast parameter space renders exhaustive exploration impractical, possibly leading to suboptimal processes and inefficient resource utilization.12,13 This optimization bottleneck constitutes a major barrier, preventing plasma technology from achieving the sustainability performance required for industrial adoption.

Recent advances in machine learning (ML) offer a transformative tool for addressing this challenge.14–16 Data-driven algorithms can learn complex input–output relationships directly from experimental observations, enabling rapid performance prediction and rational process optimization without requiring explicit mechanistic knowledge.17,18 ML methodologies are typically categorized by their learning model. The most established are supervised learning (SL), which maps known input parameters to target outputs, and unsupervised learning (UL), which identifies latent structures, such as clusters or reduced dimensions, within unlabeled data.19 Building on these, more advanced frameworks have emerged: reinforcement learning (RL), where an agent learns optimal actions through environmental feedback and reward signals,20 and active learning (AL), designed to maximize model accuracy while minimizing the cost of data annotation.21 These powerful data-driven approaches are being increasingly deployed to solve complex problems across scientific domains, including plasma medicine,22–25 large-scale screening26,27 and synthesis of novel chemicals,28–30 self-driving laboratory systems,31–33 and emissions control.34

ML has also started to be applied in plasma-based gas conversion, specifically in DBD plasmas.35–38 Successful applications of several ML models have demonstrated the predictive capability of single-algorithm models, such as artificial neural networks (ANNs). For instance, Wang et al. elucidated a relationship between process parameters and performance targets in plasma-based dry reforming of methane (DRM) to oxygenates by well-trained ANN models.35 Similarly, Shen et al. simulated CO2 conversion in a DBD-photocatalytic system using a back-propagation (BP) ANN model, reporting high coefficients of determination (R2) on both the training set and testing set.36 Recently, the field has been rapidly evolving toward more sophisticated frameworks, where pioneering work successfully integrated SL with RL, to not only predict but also autonomously optimize plasma-based or plasma-catalytic CO2 and CH4 conversion, demonstrating the potential of ML as an active optimization tool.37,38 Besides, AL strategies are being employed to automatically and efficiently navigate high-dimensional parameter spaces. For instance, Shao et al. used AL via Bayesian optimization (BO) to maximize the energy efficiency of NOx generation in a glow discharge within a fixed experimental budget,21 while our prior work demonstrated a framework where an ANN, pre-trained on literature data and refined via AL with minimal local experiments, achieved R2 > 0.95 for the prediction performance of the plasma-based CO2 splitting.39

Despite these promising developments, the research landscape remains nascent and faces significant challenges. Many existing studies rely on small, homogeneous datasets (typically less than 100 data points, which is far from big data and meta-analysis) derived from individual laboratory setups, which limit generalizability. This reliance on group-specific data, coupled with a frequent lack of comprehensive evaluation metrics and model interpretability, creates a “generalizability gap” where high performance reported on one system may not translate reliably to others. To address these limitations, a compelling strategy is to leverage the expanding corpus of published literature to construct larger, more diverse training datasets, fostering the development of widely applicable ML models and enabling robust cross-study comparisons. Recent meta-analysis of CO2 conversion data, notably within the PIONEER database framework,40 highlights that specific energy input (SEI), i.e., the ratio of power over flow rate, remains the predominant metric for cross-study performance comparison. While practical, this parameter sometimes offers an oversimplified representation, failing to capture the intrinsic and varied plasma properties (e.g., reduced electric field and electron density) within the reaction zone that fundamentally govern the process efficiency. To develop a robust, generalizable ML model capable of accurate cross-experimental prediction, it is therefore essential to move beyond SEI and identify a more comprehensive set of physically grounded descriptors. Moreover, because purely data-driven models lack any inherent awareness of thermodynamic law, they risk producing physically implausible outputs when queried in sparsely sampled operating regimes; incorporating thermodynamic constraints directly into the learning objective offers a paradigm shift from purely empirical fitting toward physically consistent extrapolation.

Furthermore, robust ensemble modelling strategies combined with transparent interpretability frameworks are required. Hybrid ensemble models, which integrate multiple base learners (e.g., neural networks, support vector regression, decision trees or ensemble-tree models), can leverage complementary strengths to enhance predictive robustness and mitigate overfitting, as evidenced in studies on plasma tar reforming and DRM.41,42 At the same time, explainable artificial intelligence (XAI) tools are essential for making ML models transparent and interpretable, and help elucidate how a model arrives at its predictions by quantifying the contribution of each input feature to an individual output.43 To date, the development of a fully interpretable, physics-informed hybrid ML model, trained exclusively on a comprehensive, multi-source literature dataset for plasma-based CO2 conversion has not, to our knowledge, been reported yet.

In this work, we develop a broadly applicable ML framework built on a consolidated literature dataset of 358 experimental conditions for plasma-based CO2 splitting in DBD reactors. We systematically evaluate inter-laboratory generalizability through a publication-wise group 5-fold cross-validation strategy, and introduce a physics-informed neural network (PINN) whose loss function is augmented with thermodynamic constraints to prevent unphysical predictions in sparsely sampled operating regimes. The resulting model integrates the PINN with random forest (RF) and extreme gradient boosting (XGB) into a hybrid ensemble, and SHapley Additive exPlanations (SHAP) analysis is employed to quantify feature contributions. This work establishes a robust, interpretable, and thermodynamically consistent ML framework that reduces the reliance on trial-and-error experimentation and provides actionable guidance for process optimization in plasma-based CO2 conversion.

2. Methods

The framework overview is presented in Fig. 1, with detailed explanations provided in the following sections. A complete list of abbreviations related to these methods is available in the SI (SI, Section S1, Table S1).
image file: d6gc01077f-f1.tif
Fig. 1 Scheme of the workflow to develop our hybrid ML model.

2.1 Dataset collection and processing

A fundamental challenge in constructing ML models from published literature is the inherent heterogeneity of experimental data, stemming from variations in reactor design, diagnostic methods, and reporting standards. To build a consistent dataset, we executed a rigorous, multi-phase harmonization protocol.

First, a systematic literature screening was conducted, focusing on peer-reviewed studies of CO2 splitting in geometrically similar coaxial DBD reactors. The selection of input parameters was guided by the dual principles of widespread data availability and fundamental physical significance. Six key parameters, i.e., discharge power, frequency, gas flow rate, discharge gap, dielectric constant and discharge length, were chosen because they are the most consistently reported descriptors across studies and collectively represent the first-order governing factors of the plasma process: energy input, micro-discharge formation, reactant residence time, electric field strength, charge accumulation and reaction volume, respectively. Consequently, only studies reporting all six inputs alongside measurable CO2 conversion and energy efficiency (EE) (or sufficient data for their calculation) were included.

Second, to ensure direct comparability, all performance data were recalculated using unified definitions. CO2 conversion was standardized as the molar amount of converted CO2 relative to the inlet amount, with corrections for gas expansion where necessary. EE was consistently derived from the discharge power and the enthalpy change of CO2 splitting, thereby normalizing values originally reported as SEI or other equivalent metrics (detailed in SI, Section S2). The CO2 conversion (χCO2) and EE were defined as follows:44

 
image file: d6gc01077f-t1.tif(1)
 
image file: d6gc01077f-t2.tif(2)
where image file: d6gc01077f-t3.tif is the output fraction of CO2, ΔH is the reaction enthalpy (282.96 kJ mol−1) of pure CO2 decomposition, and the CO2 molar volume is 24.24 L mol−1, at around 295 K and 1 atm under ideal gas assumptions.

Finally, this process yielded a compiled dataset of 358 distinct experimental records across 27 published papers,8,9,39,45–68 spanning a broad operational range (see Table S2). We explicitly acknowledge that residual, unquantifiable heterogeneity from systematic inter-study differences (e.g., analytical techniques such as GC and FTIR analysis) remains. However, by aggregating data from numerous independent sources, the influence of any single experimental bias is mitigated, allowing the SL model to identify the underlying cross-system trends from a large, diversified dataset. Prior to model training, all features were normalized to a [0, 1] range using the Min–Max scaling technique.

2.2 Pearson correlation coefficient

The linear relationship between input parameters and output targets was initially assessed using the Pearson correlation coefficient (PCC). The PCC, which quantifies the strength and direction of a linear relationship, ranges from −1 (a perfect negative correlation) to +1 (a perfect positive correlation).69,70 It is calculated as follows:
 
image file: d6gc01077f-t4.tif(3)
where ρxy represents the PCC value between the input feature and output target, xmean and ymean indicate the average of the input feature x and the output target y, respectively. For our analysis, the absolute value of the PCC was used to gauge the strength of the linear association between each of the four input parameters and the two target performance metrics (CO2 conversion and EE).

2.3 Training and validation of ML models

In this study, neural networks (NN) and two tree-based ensemble learning algorithms, namely Random Forest (RF) and Xtreme Gradient Boost (XGB) were first evaluated for their prediction performance. An artificial neural network (ANN) was first constructed as a fully connected, feed-forward architecture with six input neurons (corresponding to discharge power, frequency, gas flow rate, discharge gap, dielectric constant and discharge length) and two output neurons (for CO2 conversion and EE). Model training was conducted using the BP algorithm optimized via the gradient descent method.71 The ReLU activation function was employed in hidden layers to introduce nonlinearity while mitigating the vanishing gradient problem. The mean squared error (MSE) between predictions and experimental values was minimized during training.

Although the standard ANN can accurately capture the complex nonlinear mapping within the training distribution, it lacks any inherent awareness of thermodynamic law. To prevent unphysical predictions when the model is queried outside dense training regions, the ANN was further developed into a physics-informed neural network (PINN) by augmenting the loss function with a penalty term that enforces fundamental thermodynamic constraints on the predicted CO2 conversion (Xpred, in %) and EE (EEpred, in %):

 
image file: d6gc01077f-t5.tif(4)
with
 
image file: d6gc01077f-t6.tif(5)
where the penalty factor λ was set to 10−3. The three terms enforce non-negative conversion, non-negative EE, and EE not exceeding 100%, respectively. The first two terms enforce non-negativity of the predicted conversion and energy efficiency. The last constraint, EEpred ≤ 100%, is equivalent to the thermodynamic upper bound imposed by the minimum enthalpy of CO2 dissociation. This equivalence follows directly from the definition of EE in eqn (2): since EE ∝ χCO2/(P/F), a predicted EE exceeding 100% would imply a conversion greater than the theoretical maximum attainable for the given power and flow rate, thereby requiring less than the reaction enthalpy of 282.96 kJ per mole of CO2 split. Apart from the modified loss function, all other training settings remained identical to the standard ANN.

RF is an ensemble method that operates on the principle of bootstrap aggregation, or bagging.72 It constructs a large collection of decorrelated decision trees, each trained on a random subset of the data and features. For regression, the final prediction is formed by averaging the output of all individual trees in the forest. This methodology effectively reduces model variance, mitigates overfitting, and enhances generalization performance compared to a single decision tree, yielding a robust predictive model.

XGB is a highly efficient and scalable implementation of the gradient boosting framework.70 It builds decision trees sequentially, with each new tree trained to correct the residual errors of the current ensemble. The algorithm incorporates advanced regularization techniques to control model complexity and prevent overfitting. Key computational innovations, such as a weighted quantile sketch for efficient candidate split finding, enable faster training and often superior accuracy compared to other tree-based models like RF.

To obtain a realistic estimate of model generalizability across different published studies and to avoid data leakage, we adopted a group 5-fold cross-validation (CV) strategy with the source publication as the grouping variable. The 27 source publications were partitioned into five folds such that each fold was held out for testing exactly once across the five folds and used for training in the remaining four folds, thereby providing an unbiased assessment of the inter-laboratory and inter-publication predictive performance. Because the number of data points varies among source publications, the group assignment was designed to keep the validation set size in each fold at approximately 20%–25% of the total dataset, balancing the evaluation across folds while strictly preserving group integrity.

Hyperparameter optimization for all algorithms was conducted using the BO method (see Section S3, SI),36 which efficiently explores high-dimensional parameter spaces by constructing probabilistic surrogate models (Gaussian processes) that guide the search toward optimal configurations with minimal computational cost. In principle, a single set of hyperparameters could be selected to maximize the average performance across the five folds. However, the considerable heterogeneous dataset employed in this study comprises multiple literature sources with widely varying value ranges in each fold, a fixed hyperparameter configuration that performs well on one fold frequently performs poorly on another, occasionally driving the overall five-fold average into a negative coefficient of determination (R2) regime. We therefore performed independent hyperparameter optimization within each of the five mutually exclusive splits, yielding five separate model instances.

2.4 Hybrid model development and evaluation

To integrate the complementary strengths of the individual base learners, a hybrid ensemble model was constructed. This model generates its final prediction through a linear combination of the predictions from the three evaluated algorithms, namely, PINN, RF, and XGB, as defined by the following eqn (6):
 
image file: d6gc01077f-t7.tif(6)

Following the independent hyperparameter optimization of the base learners within each fold, the optimal ensemble weights were determined via an exhaustive grid search over the interval [0, 1] with a step size of 0.01. For each candidate weight combination, the ensemble prediction was constructed as a linear combination of the three base model outputs, and R2 on the corresponding validation set was computed. The weights that simultaneously maximized R2 were selected for that fold. This procedure was repeated independently for each of the five folds, yielding five-fold-specific ensembles. The reported CV metrics represent the average performance of these five independently optimized ensembles on their respective validation folds.

To comprehensively evaluate the model's performance, several metrics, including R2, MSE, mean-absolute error (MAE), and root mean square error (RMSE), were computed to test the datasets and validate the robustness and generalizability, as shown in Table 1.

Table 1 Metrics used for evaluating the performance of the ML models
Metric Definition Equation
yi and ŷi represent the actual value and the predicted value, respectively, and ȳ denotes the average of the actual value. In general, model accuracy was optimized by maximizing R2 and minimizing MSE.
Coefficient of determination (R2) image file: d6gc01077f-t9.tif (7)
Mean-squared error (MSE) image file: d6gc01077f-t10.tif (8)
Mean-absolute error (MAE) image file: d6gc01077f-t11.tif (9)
Root mean square error (RMSE) image file: d6gc01077f-t12.tif (10)


2.5 SHapley Additive exPlanations (SHAP) methodology

SHAP provides a model-agnostic framework for interpreting ML predictions, grounded in concepts from cooperative game theory. At its core, SHAP quantifies the contribution of each input feature to a model's output by calculating its Shapley value. This value represents the average marginal contribution of the feature to the prediction, considering all possible combinations of other input features. The Shapley value for a feature is given by:73
 
image file: d6gc01077f-t8.tif(11)
where p is the total number of input features, N\{j} is the set of all features excluding Xj, and S denotes a specific subset from N\{j}. The terms f(S) and f(S∪{j}) correspond to the model's predictions using the feature subset S and when feature Xj is added to S, respectively.

A key strength of the SHAP framework is its dual capacity for interpretation. It offers local interpretability by assigning a precise contribution value to each feature for every individual prediction. Simultaneously, global interpretability is achieved by aggregating absolute Shapley values across the entire dataset, which reveals the overall average influence of each feature on the model's outputs.74,75 A higher absolute mean SHAP value indicates a feature with greater overall influence on the model's predictions. It is essential to emphasize a critical distinction: SHAP analysis explains the model's behavior, not the underlying physical system. The method identifies which input features the trained model found most statistically influential for its predictions. It does not establish causal relationships, nor does it elucidate the fundamental mechanistic role of parameters within the plasma-chemical process. Therefore, SHAP values indicate “what the model relies on”, providing essential insight into its decision-making process, which must then be reconciled with domain knowledge.

3. Results

3.1 Characterization of the training dataset

The statistical summary of the compiled and harmonized dataset, presented in Table 2, provides a clear overview of the operational landscape captured from the literature. The parameter ranges are extensive, reflecting the broad exploration conducted by the research community. Discharge power varies over three orders of magnitude, from 0.5 W to 1000 W. Gas flow rate spans an even wider range, from 10 to 3000 mL min−1. Discharge gap and length also cover significant ranges, from sub-millimeter scales to several centimeters. Additionally, the frequency ranges from 0.05 kHz to 120 kHz, and the dielectric constant spans from 3.7 to 10. This breadth is beneficial for model training, as it exposes the algorithms to a wide spectrum of reactor behaviors and provides leverage to learn non-linear trends.
Table 2 Statistical summary of the compiled literature dataset
Parameter Minimum Maximum Mean Std. deviation
Power (W) 0.5 1000 42.25 68.84
Flow rate (mL min−1) 10 3000 86.96 210.35
Frequency (kHz) 0.05 120 23.87 19.67
Discharge gap (mm) 0.25 8.00 2.09 1.66
Length (cm) 1.0 40 11.73 7.25
Dielectric constant 3.7 10 6.76 2.85
CO2 conversion (%) 1.06 54.49 17.08 10.55
Energy efficiency (%) 0.55 23.34 5.11 4.06


At the same time, the data density is not uniform across these ranges; conditions around moderate flow rates (25–100 mL min−1) and mid-range powers (20–50 W) are more densely sampled, reflecting common laboratory practice. This non-uniform coverage is an important consideration when interpreting model uncertainty and generalization performance. The output variables (CO2 conversion and EE) exhibit correspondingly wide distributions, ranging from below 2% to over 50% for conversion and from under 1% to over 20% for efficiency, capturing the diversity of performance outcomes across different reactor configurations and operating conditions. This non-uniform coverage is an important consideration when interpreting model uncertainty and generalization performance.

3.2 Relative importance analysis

The relative importance of each input parameter, as quantified by Pearson correlation coefficient (PCC) analysis, is demonstrated in Fig. 2. Flow rate emerged as the most important input parameter for both CO2 conversion (34.2%) and energy efficiency (45.4%). Frequency and power are the second- and third-most important parameters for EE (22.7% and 19.6%, respectively), while being the least important parameters for CO2 conversion (6.3% and 8.4%, respectively). In contrast, discharge length and gap are the second and third most important parameters for CO2 conversion (25.9% and 16.1%, respectively) while ranking among the least important for EE (3.4% and 7.4%, respectively). Dielectric constant exhibits moderate importance for CO2 conversion (9.2%, fourth) but negligible influence on EE (1.4%).
image file: d6gc01077f-f2.tif
Fig. 2 Relative significance of operating parameters on the performance of plasma-based CO2 splitting.

3.3 Performance of individual ML models

To construct an efficient ML model, benchmark tests were first conducted on individual ML models, namely PINN, RF, and XGB. Hyperparameters and training curves of these models are shown in Table S3 and Fig. S1 in the SI, respectively. The predictive performance of the three base learners under the group 5-fold CV framework is summarized in Table 3. The XGB model achieved the highest five-fold average R2 of 0.362 and the lowest error metrics overall, followed by the RF model. PINN exhibited the weakest overall performance, with an average R2 of 0.038 and the highest error metrics. However, the best individual model varied across folds. RF outperformed the XGB model in Folds 1 and 5, while the XGB model was the strongest learner in Folds 2, 3, and 4, as shown in Fig. 3.
image file: d6gc01077f-f3.tif
Fig. 3 Predicted data versus experimental results on the dataset (R2 plot) for the single optimal model for CO2 conversion and energy efficiency within the (a, b) Fold 1, (c, d) Fold 2, (e, f) Fold 3, (g, h) Fold 4, and (i, j) Fold 5.
Table 3 Overall performance of individual ML models within the group 5-fold cross-validation framework
Fold Model R2 MSE RMSE MAE
Fold 1 PINN 0.055 28.704 4.152 3.659
RF 0.549 12.116 2.735 2.306
XGB 0.417 10.669 2.670 2.257
Fold 2 PINN 0.660 24.162 4.419 3.488
RF 0.740 17.766 3.843 2.992
XGB 0.780 14.590 3.518 2.739
Fold 3 PINN −1.077 29.387 5.127 4.009
RF −0.658 47.864 5.948 4.803
XGB 0.017 42.336 5.193 3.645
Fold 4 PINN 0.288 34.843 5.618 4.433
RF 0.325 31.293 5.555 4.502
XGB 0.375 29.106 5.348 4.088
Fold 5 PINN 0.267 89.789 7.586 5.871
RF 0.273 64.598 6.635 5.085
XGB 0.220 77.236 7.181 5.587
Group 5-fold average PINN 0.038 41.377 5.380 4.292
RF 0.246 34.727 4.943 3.938
XGB 0.362 34.787 4.782 3.663


Substantial inter-fold variability was observed across all models, reflecting the heterogeneous nature of the multi-source dataset and the strict source-holdout partitioning. In Fold 2, all three models performed well, with the XGB model reaching an R2 of 0.780, RF attaining 0.740, and PINN achieving 0.660. In Fold 3, however, performance collapsed across the board: PINN and RF returned sharply negative R2 values of −1.077 and −0.658, respectively, while XGB was only marginally positive (R2 = 0.017). Folds 1 and 4 showed intermediate performance, with the best model achieving R2 values of 0.549 and 0.375, respectively. PINN displayed the widest performance swing, underscoring its sensitivity to the composition of the training and test sources. These results demonstrate that while XGB provides the most consistent baseline overall, no single model is immune to the distribution shifts inherent in strict group-wise validation.

3.4 Performance of hybrid ML models

The hybrid ensemble model was then evaluated under the same group 5-fold CV framework, and its performance in each fold is summarized in Table 4 and Fig. 4. The ensemble consistently surpassed the best individual model in every fold, achieving a five-fold average R2 of 0.441, a 21.8% improvement over the strongest single learner (XGB, average R2 of 0.362), alongside corresponding reductions in all error metrics.
image file: d6gc01077f-f4.tif
Fig. 4 Predicted data versus experimental results on the dataset (R2 plot) for the hybrid model for CO2 conversion and energy efficiency within the (a, b) Fold 1, (c, d) Fold 2, (e, f) Fold 3, (g, h) Fold 4, and (i, j) Fold 5.
Table 4 Overall performance of the hybrid ML models within the group 5-fold cross-validation framework
Models Weights (PINN/RF/XGB) R2 MSE MAE RMSE
Fold 1 0.13/0.87/0.00 0.562 12.172 2.238 2.731
Fold 2 0.21/0.06/0.73 0.791 14.441 2.618 3.449
Fold 3 0.07/0.00/0.93 0.024 40.162 3.581 5.110
Fold 4 0.36/0.02/0.62 0.417 27.665 4.077 5.161
Fold 5 0.47/0.25/0.28 0.412 59.065 4.803 6.271
5-Fold average 0.441 30.701 3.463 4.544


The optimized weights varied considerably across folds, reflecting the adaptive nature of the fusion strategy that responded to the characteristics of each held-out source, as shown in Fig. 5. In most folds, the ensemble converged to a two-model configuration: either RF was excluded entirely (Folds 2 and 4) or dominated the combination (Fold 1), while XGB received the largest share in three of the five partitions. A notable exception occurred in Fold 5, where all three base learners contributed meaningfully (0.47, 0.25, and 0.28 for PINN, RF, and XGB, respectively), which also delivered the largest gain over the best single model in that fold. In the most challenging partition (Fold 3), the ensemble concentrated 0.93 of the weight on XGB, the only model with a positive individual R2, yielding a marginally positive ensemble R2 of 0.024. The broad dispersion of optimal weights across folds confirms that no fixed weighting scheme is universally effective, and that the ensemble's strength lies precisely in its ability to rebalance model contributions according to the difficulty and composition of each held-out source.


image file: d6gc01077f-f5.tif
Fig. 5 R2 of the training and optimization process for the hybrid model within (a) Fold 1, (b) Fold 2, (c) Fold 3, (d) Fold 4 and (e) Fold 5.

The pairwise error correlations among the three base learners were examined in each fold to characterize the diversity of their prediction errors. We computed the PCC of their prediction residuals on the different validation fold sets, as shown in Fig. 6. Across all folds, the error correlation between RF and XGB almost consistently exceeds 0.8, indicating that the two tree-based models tend to make similar mistakes. The correlation between PINN and the tree-based models showed greater variation across folds. In Folds 1, 3, and 4, PINN-RF and PINN-XGB correlations were broadly comparable, generally ranging from 0.51 to 0.82. In Fold 2, a notable asymmetry appeared for EE, where PINN-RF and PINN-XGB correlations were considerably lower (0.26 and 0.12, respectively). Fold 5 displayed a distinct structure, with PINN maintaining moderate correlations with RF (0.69 and 0.76) and noticeably lower correlations with the XGB model for CO2 conversion (0.46), representing the lowest pairwise correlation with the XGB model observed across all folds.


image file: d6gc01077f-f6.tif
Fig. 6 Error complementarity of the PINN, RF and XGB models for CO2 conversion and energy efficiency for CO2 conversion and energy efficiency within the (a, b) Fold 1, (c, d) Fold 2, (e, f) Fold 3, (g, h) Fold 4, and (i, j) Fold 5.

Overall, while the RF and XGB models consistently produced highly correlated errors, PINN exhibited a systematically lower, albeit variable, degree of correlation with both, reflecting its architectural distinctness. This error correlation structure provides the basis for the weight optimization to selectively engage complementary models in each partition (see Discussion 4.2).

To assess the generalizability of the hybrid model, we conducted validation experiments at operating conditions within the training parameter ranges but absent from the literature database. Fig. S2 in the SI shows the experimental setup of the DBD reactor used for the CO2 splitting experiments, described in detail in ref. 76. The predictions of the hybrid model for the unseen data exhibit excellent agreement with the experimental results, as presented in Fig. 7. The model predictions closely track the experimental trends for both CO2 conversion and EE, as a function of either flow rate or frequency, achieving an R2 of 0.924. This strong performance on truly independent, prospective experimental data confirms the model's reliability and practical utility for guiding reactor design and operational optimization.


image file: d6gc01077f-f7.tif
Fig. 7 Predicted performance (in terms of CO2 conversion and EE) by the hybrid model for unseen experimental datasets, compared with the actual data, as a function of (a) flow rate (power = 27.93 W, frequency = 45 kHz and discharge gap = 1.05 mm) and (b) frequency (flow rate = 20 mL min−1 and discharge gap = 0.8 mm). Discharge power, plasma length and dielectric constant are fixed at 27.93 W, 7.5 mm and 9.6, respectively.

3.5 Extrapolation capability of the PINN model

To evaluate the impact of physics-informed training, the PINN was compared against a purely data-driven ANN with an identical training procedure but without the thermodynamic penalty on Fold 2, the most favorable partition. Its architecture was independently optimized via BO under the standard MSE loss, yielding a different hidden-layer configuration. Despite this architectural freedom, the standard ANN achieved a markedly lower individual R2 than the PINN, and when integrated into the ensemble, it received zero weight and was thus entirely excluded. The PINN, by contrast, retained a meaningful complementary role within the ensemble (Table 5).
Table 5 Comparison of the performance of the PINN and ANN models on Fold 2
Key feature PINN ANN
Penalty factor λ = 10−3, loss_phys = ReLU(−Xpred)2 + ReLU(−EEpred)2 + ReLU(EEpred − 100)2; and hyperparameter optimization on ANN was conducted by the BO method.
Neurons in hidden layers (45, 38, 20) (45, 13, 13)
Loss function MSE + λ × loss_phys MSE
Weights (NN, RF, XGB) (0.21, 0.06, 0.73) (0.00, 0.23, 0.77)
NN R2 0.660 0.403
Hybrid R2 0.791 0.783


To delineate the predictive envelope of the ensemble models, we examined relatively extreme operating conditions (e.g., high flow rate of 1000 mL min−1, power between 18 and 38 W) that lie near the boundary of the training distribution but are sparsely represented in the collected literature. In the entire dataset, high-flow conditions appear almost exclusively at power levels above 50 W, leaving the low-power, high-flow quadrant virtually unexplored. Table 6 compares the predictions of the individual ANN and the hybrid PINN model on five extrapolated conditions.

Table 6 Comparisons of the predictions of the two model variants on extrapolated conditions
Flow rate (mL min−1) Power (W) Actual CO2 conversion (%) Actual EE (%) ANN prediction Hybrid PINN prediction
Conversion (%) EE (%) Conversion (%) EE (%)
1000 18.68 0.41 4.27 −1.06 33.89 0.66 11.70
1000 24.74 0.68 5.35 −1.16 33.79 0.71 11.78
1000 27.93 0.61 4.25 −1.20 33.73 0.74 11.70
1000 31.83 0.75 4.58 −1.26 33.67 0.77 11.59
1000 37.89 0.94 4.82 −1.35 33.56 0.81 11.62


The standard ANN produces negative CO2 conversion values across all five test points, while simultaneously overestimating energy efficiency by roughly a factor of seven. This failure occurs because the network extrapolates a decreasing conversion trend linearly across zero when confronted with the unseen combination of high flow and low power. The hybrid PINN model, however, eliminates all negative predictions entirely, returning strictly positive conversion values that approach the measured range, and reduces the EE overestimation to approximately a factor of two to three. While the quantitative accuracy of the PINN-based hybrid in this extreme extrapolation regime remains imperfect, the principal achievement is the complete removal of the catastrophic unphysical predictions that characterized the unconstrained model.

3.6 Model interpretability: SHAP analysis

SHAP analysis was performed on the best XGB model component of the hybrid model across Fold 2, 3 and 4 to interrogate the contribution of individual input features and to assess the stability of the derived interpretability metrics, as shown in Fig. 8. The six input descriptors encompass two distinct category domains: reaction conditions (flow rate, power, and frequency) and reactor dimensions (discharge gap, dielectric constant, and length). At the level of individual features, a clear and reproducible hierarchy emerged. Flow rate consistently ranked as the most influential descriptor across all three folds, followed by power, with discharge gap occupying the third position. The relative ordering of these top three features remained invariant across folds, while the lower-ranked features, i.e., dielectric constant, frequency, and length, exhibited minor positional fluctuations that did not alter the overall importance structure.
image file: d6gc01077f-f8.tif
Fig. 8 Feature importance analysis represented in the form of horizontal bar plots for normalized SHAP values, and a pie chart visualizing the cumulative contribution of the reaction conditions and reactor dimensions by the model prediction in (a, b) Fold 2, (c, d) Fold 3 and (e, f) Fold 4.

In global interpretability analysis, the reaction conditions dominated the reactor dimensions by a factor of approximately two across all folds examined: the share of reaction conditions ranged from 69.7% (Fold 4) to 76.8% (Fold 3), while reactor dimensions accounted for the complementary fraction. The constancy of this categorical imbalance across different ensemble weight configurations confirms that the feature importance ranking reflects genuine data structure rather than model-specific artifacts. It is important to emphasize that ensemble weights and SHAP values address fundamentally different questions. Ensemble weights reflect the optimal proportion for combining predictions from different algorithms to minimize overall error. In contrast, SHAP values decompose the prediction of the already-weighted hybrid model to attribute credit to each input feature. Thus, ensemble weights pertain to the model combination strategy, while SHAP values explain feature contributions within the combined model. These two types of “importance” are not directly comparable and should not be conflated.

4. Discussion

4.1 Relative significance and model interpretability

The PCC identifies gas flow rate as the most statistically significant parameter for both CO2 conversion and EE. Flow rate governs critical process variables, such as reactant residence time, species concentration within the discharge zone, and the resulting thermal and chemical history of the gas mixture.77 The dominant role of flow rate stems from its direct control over two competing physical factors: residence time and SEI. A lower flow rate increases residence time, enhancing conversion, but also raises the SEI, which is detrimental to EE. Conversely, a higher flow rate typically benefits EE by lowering SEI, but limits conversion due to reduced residence time. Input power shows a strong correlation with EE as it is the numerator in the SEI. Its relatively weak correlation with conversion indicates that in the studied regime, increasing power primarily leads to gas heating and acceleration of recombination reactions rather than to net conversion gains. Therefore, optimizing for high efficiency requires carefully balancing a sufficiently high flow rate to maintain a low optimal SEI with just enough power to achieve the desired conversion level, avoiding the diminishing returns associated with excessive power input.78

The reactor geometry, specifically a smaller discharge gap and a longer discharge length, is statistically significant for enhancing CO2 conversion but shows limited correlation with EE. This can be explained by the underlying plasma physics: a smaller gap increases the reduced electric field strength, promoting more efficient electron-impact dissociation of CO2,55,79 while a longer discharge length increases reactant residence time within the plasma zone.55 However, these geometric improvements do not directly address the fundamental limitation of the back-reaction between CO and O2, which wastes input energy and creates a known trade-off between conversion and EE.46 Therefore, while geometry is a key lever for conversion, breaking the conversion-efficiency trade-off likely requires advanced strategies such as in situ product separation or plasma-catalyst synergy.46,80

Regarding model interpretability, it is critical to recognize that SHAP values reflect conditional associations learned from the training data distribution and do not provide direct evidence of independent physical causality by which these parameters affect plasma chemistry. Two statistical properties of the dataset govern the observed feature rankings: differential variance and multivariate collinearity. First, the high SHAP magnitudes assigned to flow rate and power (collectively 61%–71%) are partially attributable to their broader sampling ranges relative to other descriptors. Tree-based models preferentially split on high-variance features; thus, importance rankings are shaped by experimental design rather than intrinsic physical dominance alone. Second, plasma process variables are inherently collinear. Flow rate and power are coupled through the derived quantity SEI, a central parameter governing EE in plasma processes. In typical experimental designs, power and flow rate are adjusted in tandem to systematically explore the SEI space, creating a structured correlation between these two input features. At constant SEI, the power and flow rate vary proportionally; across the dataset, their variations are linked through this ratio. Consequently, the model cannot independently resolve the distinct physical roles of flow rate and power because their effects are statistically entangled via SEI. SHAP attribution under such collinearity is conditional on the covariance structure of the training data and cannot isolate independent mechanistic effects.

Therefore, the SHAP-derived rankings should be interpreted strictly as a descriptive summary of the model's internal association structure within the sampled parameter space. They do not validate that the model has learned physically meaningful parameters, nor are they transferable to regimes with different covariance structures. Disentangling the independent contributions of collinear variables would require causally informed experimental designs that deliberately decorrelate power and flow rate.

4.2 Impact of validation strategy on performance assessment

To evaluate the influence of the validation strategy, we compared the XGB and hybrid models under group 5-fold CV and standard randomized 5-fold CV, as presented in Fig. 9. The hyperparameters of the randomized 5-fold CV model are shown in Table S4 in the SI. Under randomized splitting, both the XGB and hybrid model achieved average R2 values above 0.91, more than double the corresponding Group CV results (R2 = 0.441), and even exceeded the performance observed in the most favorable Group CV fold (R2 = 0.791). This pronounced disparity quantifies the severe inflation introduced by data leakage when interdependent points from the same published study are permitted to span both training and validation sets. The contrast reveals that conventional random splitting can yield deceptively optimistic assessments that collapse under genuine cross-study deployment, underscoring the necessity of group-aware validation for any ML model trained on aggregated literature data.
image file: d6gc01077f-f9.tif
Fig. 9 Predicted data versus experimental results on the dataset (R2 plot) within the random 5-fold cross-validation framework for the XGB model for (a) CO2 conversion and (b) energy efficiency, and hybrid model for (c) CO2 conversion and (d) energy efficiency.

The performance gap between these two frameworks exemplifies a fundamental tension in applying ML to plasma-based CO2 conversion: the conflict between model expressiveness, dataset heterogeneity, and evaluation authenticity. The modest R2 obtained under Group CV is not a failure of the modelling approach, but an honest quantification of how much predictive power can be transferred across laboratories with distinct reactor designs, diagnostic methods, and measurement protocols. The inflated metrics under randomized splitting, by contrast, reveal only that the model can interpolate effectively within a consistent data distribution between training and testing, a capability that is of limited practical value when the goal is to predict performance in an unseen experimental setup.

In summary, these findings highlight a key principle for sustainable process development: systematic investment in standardized, high-quality data collection yields compounding returns in model reliability and transferability. As consistent data accumulate, generalization performance can progressively approach the idealized accuracy, ultimately reducing the collective experimental burden for plasma process optimization across the research community.

4.3 Performance and applicability of the weighted ensemble models

Table 7 summarizes the error correlation for reaction performance, weight assignment and corresponding model performance. The ensemble weight distributions observed across the five Group CV folds fall into three archetypal modes, jointly governed by the pairwise error correlations among the base models and their individual predictive power. Across all folds, RF and XGB exhibit high error correlation, making the two tree-based models largely interchangeable, whereas PINN maintains low to moderate correlations with both, providing a persistent source of complementary information. Consequently, when one tree-based model substantially outperforms the other, the weaker one is suppressed to near-zero weight to form a two-active-model configuration, as seen in Fold 2 and 4, where XGB dominated, and RF was excluded, and in Fold 1, where the reverse occurred. PINN is almost always retained with a non-zero weight because its distinct architecture supplies error patterns not captured by the tree-based models. The only extreme case is Fold 3, where PINN joined RF in returning a negative R2 far below that of XGB, and the ensemble degenerated to XGB alone. A genuine three-model configuration emerged only in Fold 5, where all three learners performed comparably, and PINN maintains only moderate error correlation, with both tree-based models allowed to contribute meaningful complementary information.
Table 7 Error correlation for reaction performance, weight assignment and corresponding model performance
Fold Error correlation for CO2 conversion Error correlation for EE Weights (PINN/RF/XGB) Optimal single model_R2 Hybrid model_R2 ΔR2
PINN-RF PINN-XGB RF-XGB PINN-RF PINN-XGB RF-XGB
1 0.74 0.75 0.98 0.51 0.58 0.88 0.13/0.87/0.00 0.549 (RF) 0.562 0.013
2 0.80 0.69 0.87 0.26 0.12 0.81 0.21/0.06/0.73 0.780 (XGB) 0.791 0.011
3 0.66 0.74 0.86 0.69 0.70 0.82 0.07/0.00/0.93 0.017 (XGB) 0.024 0.007
4 0.81 0.77 0.91 0.82 0.77 0.96 0.36/0.02/0.62 0.375 (XGB) 0.417 0.042
5 0.69 0.46 0.91 0.76 0.74 0.81 0.47/0.25/0.28 0.273 (RF/PINN) 0.412 0.139


However, the improvement in R2 over the best single model depends not only on whether a complementary model is engaged, but also on how much of the dominant model's error is amenable to cancellation. When the ensemble degenerates to a single model, no cancellation is possible, and the gain is negligible, as shown in Fold 3. With two active models, a single pair of decorrelated error streams yields a modest improvement (Fold 1 and Fold 2), which can be somewhat larger when the dominant model itself leaves considerable room for improvement (Fold 4). The most substantial gain arises only when all three learners receive meaningful weights, enabling multiple pairwise cancellation channels simultaneously (Fold 5). The ensemble thus functions by adaptively canceling the portion of prediction error that arises from domain shift and is unevenly expressed across different architectures. Its value is greatest where the single best model struggles and multiple models provide diverse, mutually decorrelated errors.

These distinct modes of ensemble behavior are inextricably linked to the substantial inter-fold variability discussed in Section 3.3: performance fluctuates dramatically because training literature sources containing unique experimental signatures may not be well represented by others in test sources. The ensemble compensates for this variability by adaptively rebalancing model contributions: it simplifies to a single-model configuration when the domain shift is severe, and expands to a multi-model configuration by exploiting multiple decorrelated error streams when the training data maintain at least partial representativeness.

4.4 Comparison with other ML models

Before comparing with external benchmarks, it is instructive to examine how the hybrid ensemble was benchmarked against a basic linear regression using only SEI as the predictor. As shown in Table 8, the linear model fails decisively, returning a negative five-fold average R2 and underperforming the hybrid ensemble in every single fold. This outcome demonstrates that SEI alone, despite its widespread use as a cross-study comparison metric, cannot capture the nonlinear relationships between operating conditions and reaction performance when data are aggregated from multiple independent sources. In contrast, the hybrid ensemble delivers positive R2 values in five folds and a near-zero value in the most challenging split. This internal comparison demonstrates that the hybrid ensemble achieves both substantially higher accuracy and markedly better stability. The moderate increase in model complexity is therefore a necessary investment to attain meaningful predictive performance on this multi-source dataset.
Table 8 Comparison of the hybrid model and linear regression model
R2 Hybrid model Linear regression
Fold 1 0.562 −0.851
Fold 2 0.791 0.289
Fold 3 0.024 −0.887
Fold 4 0.417 −0.138
Fold 5 0.412 −4.231
Group 5-fold average 0.441 −1.164


Table 9 presents the hybrid ensemble within the landscape of recent ML modeling efforts on plasma-catalytic and related systems. Cai et al. applied a hybrid combination of ANN, RT, and SVR to a homogeneous dataset of approximately 100 in-house experiments on plasma-catalytic DRM, reporting an R2 above 0.98 under a 10-fold CV framework and an R2 of 0.92 on five new data points.42 However, the training data originated from a single experimental setup, which likely limits the model's transferability to different reactor configurations. Wang et al. developed a single-algorithm ANN model for catalytic tar reforming using 584 literature data points, achieving an R2 of 0.96 under a 5-fold CV framework but a markedly lower R2 of 0.72 on 193 unseen data, a drop the authors attributed to catalyst diversity insufficiently represented in the training set.81 Lan et al. evaluated eight regressors on 224 literature data points from 21 discharge configurations for nitrogen fixation;82 the best stacking ensemble, led by XGB as a meta-learner, achieved a test R2 of 0.966 but was validated on only two new cases (R2 = 0.98).

Table 9 Comparison of the developed ML method with existing ML methods
Dataset System ML models Performance Generalizability Ref.
Abbreviations: literature data (Lit_data), experimental data (Exp_data), artificial neural networks (ANN), random forest (RF), extreme gradient boost (XGB), and regression trees (RT). Literature data = published experimental data.
358 Lit_data Plasma-based CO2 splitting (DBD) ANN + RF + XGB R2 = 0.791 (best-fold); 0.441 (Group 5-fold CV) R2 = 0.92 (10 new data) This work
100 Exp_data Plasma-catalytic DRM (DBD) ANN + RT + SVR R2 > 0.98 (10-fold CV) R2 = 0.92 (5 new data) 42
584 Lit_data Catalytic tar reforming Only ANN model R2 = 0.96 (5-fold CV) R2 = 0.72 (193 new data) 81
224 Lit_data Plasma-based nitrogen fixation (multi-reactors) XGB (best model) R2 = 0.966 (5-fold CV) R2 = 0.98 (2 new data) 82


Compared with prior efforts, the present work is distinguished by several methodological refinements that strengthen the reliability and interpretability of the modeling. The model is developed on a larger and explicitly multi-source compilation (358 data points) that covers a substantially wider range of reactor configurations and operating conditions, with a rigorous source-holdout CV framework that treats entire experimental studies as unseen domains, offering a structurally honest estimate of generalization. It further integrates thermodynamic constraints via a PINN to prevent unphysical predictions in sparsely sampled regimes; an important safeguard incorporated in ML models applied to plasma-based CO2 conversion. The resulting ensemble, while achieving competitive predictive accuracy, additionally provides a more structurally honest estimate of cross-laboratory transferability and an explicit analysis of the conditions under which performance gains from complementary base learners are realized or bounded by irreducible inter-source heterogeneity.

4.5 Critical view of the ML model applied in plasma-based gas conversion

Despite growing interest in applying ML to plasma-based gas conversion, the practical benefit of these models for guiding process optimization beyond reported datasets remains limited. A critical examination reveals that the most fundamental bottleneck is not algorithmic but infrastructural.83 The plasma-chemical community currently lacks standardized, machine-readable databases that include the physical descriptors essential for capturing discharge mechanisms (e.g., mean electron energy, electron density) and, when relevant, catalyst properties (e.g., surface area and metal dispersion).12 Without such information, models are forced to rely on indirect operational parameters whose variations often reflect experimental design choices rather than independent physical drivers. The adoption of FAIR (Findable, Accessible, Interoperable, and Reusable) data principles is therefore an essential first step toward building the comprehensive, richly characterized datasets that robust and transferable models require.84 Until such infrastructure exists, even the most sophisticated algorithms face a hard ceiling imposed by the information content of their inputs.

Within this data-limited regime, most current purely data-driven ML models function, by construction, as high-fidelity interpolators: they learn complex functions that faithfully reproduce known experimental trends within the parameter range covered by their training data. While this capability is valuable for screening and optimization within familiar territory, it does not constitute prediction in a mechanistic sense, and offers limited capacity for extrapolation or for uncovering physical mechanisms not already implicit in the data. In such cases, the primary role of the ML model is to find an empirical mapping that accurately reproduces known results, rather than to provide insights into the underlying chemical and physical processes. The resulting models are thus best regarded as powerful interpolative tools, not as predictive frameworks that generate knowledge beyond the information content of their training data.

Precisely because its predictive reliability is confined to the explored domain, the model can produce physically inadmissible outputs when extrapolating to underrepresented regimes. Our initial effort to incorporate physical knowledge through PINN directly addresses this limitation by embedding thermodynamic constraints and thus provides a feasibility guarantee that purely data-driven models lack. While this does not yet yield accurate pointwise predictions on EE in the extrapolation regime, it demonstrates that even simple physical guardrails can extend the trustworthiness of model outputs beyond the strict interpolation envelope. More ambitious integrations of physics and data are emerging in adjacent fields, such as the neural master equation framework for plasma-surface interactions, which retains the structure of governing kinetic equations while using neural networks to represent unknown state transitions.85 Such approaches suggest a path forward in the transition of ML from a powerful interpolative tool into a genuine partner in scientific discovery for plasma-based gas conversion.86

5. Conclusions

We developed a robust and interpretable ML framework for predicting CO2 conversion and EE in DBD reactors, trained on a comprehensive database of 357 literature observations spanning 2010 to 2025. A hybrid ensemble model integrating PINN, RF, and XGB algorithms consistently outperformed the best individual model under a source-holdout group 5-fold cross-validation framework, achieving a 21.8% relative improvement in average R2. Error correlation analysis established that ensemble weights are determined by the pairwise error correlation structure of the base models and their individual predictive accuracy, while the magnitude of improvement over individual models is governed by the degree of error decorrelation and the amount of cancellable error. The ensemble model further achieved an R2 of 0.92 on unseen data within the explored domain, while the physics-informed loss eliminated unphysical predictions in data-sparse regimes, yielding strictly non-negative CO2 conversion estimates. SHAP analysis identified flow rate and power as the dominant features, collectively accounting for 61%–71% of the model's predictions, subject to the statistical associations conditioned on the training data distribution. Overall, this work provides a transparent, rigorously validated baseline and highlights that further progress toward genuinely predictive ML in plasma-based gas conversion processes will benefit from community-wide adoption of FAIR data standards and the development of physics-informed architectures that embed mechanistic constraints directly into the advanced learning framework.

Author contributions

Conceptualization, J. L. and S. L.; methodology & investigation, J. L., J. X. and P. A.; writing – original draft, J. L. and S. L.; writing – review & editing, J. L., X. L. and A. B.; funding acquisition, F. G., S. L. and A. B.; and supervision, A. B.

Conflicts of interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

Data availability

All data that support the findings of this study are included within the article and its supplementary information (SI). Supplementary information is available. See DOI: https://doi.org/10.1039/d6gc01077f.

Acknowledgements

This project received funding from the European Research Council (ERC), under the European Union's Horizon 2020 research and innovation programme (grant agreement no. 810182-SCOPE ERC Synergy project), and the GICO project (grant agreement ID: 101006656).

References

  1. R. Snoeckx and A. Bogaerts, Chem. Soc. Rev., 2017, 46, 5805–5863 Search PubMed.
  2. Y. Xu, Y. Gao, L. Dou, D. Xi, C. Qi, B. Lu and T. Shao, Green Chem., 2025, 27, 9332–9356 RSC.
  3. A. Bogaerts and E. C. Neyts, ACS Energy Lett., 2018, 3, 1013–1027 CrossRef CAS.
  4. A. Bogaerts, Nat. Chem. Eng., 2025, 2, 336–340 CrossRef CAS.
  5. J. Sun, Z. Qu, Y. Gao, T. Li, J. Hong, T. Zhang, R. Zhou, D. Liu, X. Tu, G. Chen, V. Brüser, K.-D. Weltmann, D. Mei, Z. Fang, A. Borras, A. Barranco, S. Xu, C. Ma, L. Dou, S. Zhang, T. Shao, G. Chen, D. Liu, X. Lu, Z. Bo, W.-H. Chiang, K. Vasilev, M. Keidar, A. Nikiforov, A. R. Jalili, P. J. Cullen, L. Dai, V. Hessel, A. Bogaerts, A. B. Murphy, R. Zhou and K. Ostrikov, J. Phys. D: Appl. Phys., 2024, 57, 503002 CrossRef CAS.
  6. A. George, B. Shen, M. Craven, Y. Wang, D. Kang, C. Wu and X. Tu, Renewable Sustainable Energy Rev., 2021, 135, 109702 CrossRef CAS.
  7. S. Li, P. Arun, H. van den Bogaard, T. van Raak, C. Liu and F. Gallucci, Front. Chem. Sci. Eng., 2025, 19, 96 CrossRef.
  8. A. Ozkan, A. Bogaerts and F. Reniers, J. Phys. D: Appl. Phys., 2017, 50, 084004 CrossRef.
  9. Q. Yu, M. Kong, T. Liu, J. Fei and X. Zheng, Plasma Chem. Plasma Process., 2012, 32, 153–163 CrossRef CAS.
  10. V. Laitl, I. Tsonev, O. Biondo, E. Carbone, M. C. K. Albrechts and A. Bogaerts, Chem. Eng. J., 2025, 526, 171039 CrossRef CAS.
  11. H. M. S. Van Poyer, I. Tsonev, S. J. R. Maerivoet, M. C. K. Albrechts and A. Bogaerts, Chem. Eng. J., 2025, 507, 160688 CrossRef CAS.
  12. Z. Li, X. Teng, E. Wu, X. Pei, L. Nie, A. Mesbah and X. Lu, J. Environ. Chem. Eng., 2025, 13, 118605 CrossRef CAS.
  13. X. Teng, Z. Li, X. Pei, L. Nie, A. Mesbah and X. Lu, Plasma Processes Polym., 2025, 22, e70057 CrossRef.
  14. S. Kumar, G. Ignacz and G. Szekely, Green Chem., 2021, 23, 8932–8939 RSC.
  15. Y. Kim, J. Cho, H. Jung, L. E. Meyer, G. M. Fioroni, C. D. Stubbs, K. Jeong, R. L. McCormick, P. C. S. John and S. Kim, Green Chem., 2024, 26, 10247–10264 RSC.
  16. S. Ahmat Ibrahim, S. Meng, C. Milhans, M. H. Barecka, Y. Liu, Q. Li, J. Yang, Y. Sha, Y. Yi and F. Che, Nat. Chem. Eng., 2025, 1–12 Search PubMed.
  17. S. E. Jerng, Y. J. Park and J. Li, Energy and AI, 2024, 16, 100361 CrossRef.
  18. T. Toyao, Z. Maeno, S. Takakusagi, T. Kamachi, I. Takigawa and K. Shimizu, ACS Catal., 2020, 10, 2260–2297 CrossRef CAS.
  19. A. D. Bonzanini, K. Shao, D. B. Graves, S. Hamaguchi and A. Mesbah, Plasma Sources Sci. Technol., 2023, 32, 024003 Search PubMed.
  20. A. Mesbah and D. B. Graves, J. Phys. D: Appl. Phys., 2019, 52, 30LT02 CrossRef CAS.
  21. K. Shao, X. Pei, D. B. Graves and A. Mesbah, Plasma Sources Sci. Technol., 2022, 31, 055018 CrossRef CAS.
  22. M. He, R. Bai, S. Tan, D. Liu and Y. Zhang, Plasma Processes Polym., 2024, 21, 2400020 CrossRef CAS.
  23. M.-C. Chen, Y.-C. Lee, J.-H. Tee, M.-T. Lee, C.-K. Ting and J.-Y. Juang, Plasma Sources Sci. Technol., 2024, 33, 105015 CrossRef CAS.
  24. E. Wu, K. Song, X. Pei, L. Nie, D. Liu and X. Lu, Appl. Phys. Lett., 2024, 125, 203703 CrossRef CAS.
  25. E. Wu, K. Song, X. Pei, L. Nie, A. Mesbah and X. Lu, Appl. Phys. Lett., 2025, 127, 053701 CrossRef CAS.
  26. B. Zhao, Z. Chen, K. Xie, Y. Qiu, Z. Qi, L. Lei and Z. Song, Green Chem., 2026, 28, 5429–5436 Search PubMed.
  27. M. Mohan, M. K. Kidder and J. C. Smith, Green Chem., 2025, 27, 15106–15123 RSC.
  28. M. Suvarna, T. Zou, S. H. Chong, Y. Ge, A. J. Martín and J. Pérez-Ramírez, Nat. Commun., 2024, 15, 5844 CrossRef CAS PubMed.
  29. X. Yuan, M. Suvarna, J. Y. Lim, J. Pérez-Ramírez, X. Wang and Y. S. Ok, Environ. Sci. Technol., 2024, 58, 6628–6636 CrossRef CAS PubMed.
  30. A. Ramirez, E. Lam, D. P. Gutierrez, Y. Hou, H. Tribukait, L. M. Roch, C. Copéret and P. Laveille, Chem Catal., 2024, 4, 100888 CAS.
  31. G. Wang, S. Mine, D. Chen, Y. Jing, K. W. Ting, T. Yamaguchi, M. Takao, Z. Maeno, I. Takigawa, K. Matsushita, K. Shimizu and T. Toyao, Nat. Commun., 2023, 14, 5861 CrossRef CAS PubMed.
  32. A. Slattery, Z. Wen, P. Tenblad, J. Sanjosé-Orduna, D. Pintossi, T. den Hartog and T. Noël, Science, 2024, 383, eadj1817 CrossRef CAS.
  33. B. P. MacLeod, F. G. L. Parlane, T. D. Morrissey, F. Häse, L. M. Roch, K. E. Dettelbach, R. Moreira, L. P. E. Yunker, M. B. Rooney, J. R. Deeth, V. Lai, G. J. Ng, H. Situ, R. H. Zhang, M. S. Elliott, T. H. Haley, D. J. Dvorak, A. Aspuru-Guzik, J. E. Hein and C. P. Berlinguette, Sci. Adv., 2020, 6, eaaz8867 CrossRef CAS PubMed.
  34. G. Ignacz, A. K. Beke, V. Toth and G. Szekely, Nat. Energy, 2025, 10, 308–317 CrossRef CAS.
  35. Y. Wang, Y. Chen, J. Harding, H. He, A. Bogaerts and X. Tu, Chem. Eng. J., 2022, 450, 137860 CrossRef CAS.
  36. Y. Shen, C. Fu, W. Luo, Z. Liang, Z.-R. Wang and Q. Huang, Green Chem., 2023, 25, 7605–7611 RSC.
  37. J. Li, J. Xu, E. Rebrov, B. Wanten and A. Bogaerts, Green Chem., 2025, 27, 3916–3931 Search PubMed.
  38. J. Li, J. Xu, E. Rebrov and A. Bogaerts, Chem. Eng. J., 2025, 507, 159897 CrossRef CAS.
  39. J. Li, G. Palma, J. Xu, F. Gallucci, A. Bogaerts and S. Li, Energy Convers. Manage., 2026, 356, 121210 CrossRef CAS.
  40. A. Salden, M. Budde, C. A. Garcia-Soto, O. Biondo, J. Barauna, M. Faedda, B. Musig, C. Fromentin, M. Nguyen-Quang, H. Philpott, G. Hasrack, D. Aceto, Y. Cai, F. A. Jury, A. Bogaerts, P. Da Costa, R. Engeln, M. E. Gálvez, T. Gans, T. Garcia, V. Guerra, C. Henriques, M. Motak, M. V. Navarro, V. I. Parvulescu, G. Van Rooij, B. Samojeden, A. Sobota, P. Tosi, X. Tu and O. Guaitella, J. Energy Chem., 2023, 86, 318–342 CrossRef CAS.
  41. Y. Wang, Z. Liao, S. Mathieu, F. Bin and X. Tu, J. Hazard. Mater., 2021, 404, 123965 CrossRef CAS PubMed.
  42. Y. Cai, D. Mei, Y. Chen, A. Bogaerts and X. Tu, J. Energy Chem., 2024, 96, 153–163 CrossRef CAS.
  43. J. Du, Y. Ding, C. Zhang, M. Chen and J. Pan, ACS Sustainable Chem. Eng., 2025, 13, 16845–16859 CrossRef CAS.
  44. B. Wanten, R. Vertongen, R. De Meyer and A. Bogaerts, J. Energy Chem., 2023, 86, 180–196 CrossRef CAS.
  45. S. Paulussen, B. Verheyde, X. Tu, C. De Bie, T. Martens, D. Petrovic, A. Bogaerts and B. Sels, Plasma Sources Sci. Technol., 2010, 19, 034015 CrossRef.
  46. N. Lisi, U. Pasqual Laverdura, R. Chierchia, I. Luisetto and S. Stendardo, Sci. Rep., 2023, 13, 7394 CrossRef CAS PubMed.
  47. D. Mei, Y.-L. He, S. Liu, J. Yan and X. Tu, Plasma Processes Polym., 2016, 13, 544–556 CrossRef CAS.
  48. P. Wu, X. Li, N. Ullah and Z. Li, Mol. Catal., 2021, 499, 111304 CAS.
  49. A. Ozkan, T. Dufour, T. Silva, N. Britun, R. Snyders, A. Bogaerts and F. Reniers, Plasma Sources Sci. Technol., 2016, 25, 025013 CrossRef.
  50. M. Alliati, D. Mei and X. Tu, J. CO2 Util., 2018, 27, 308–319 CrossRef CAS.
  51. N. Lu, C. Zhang, K. Shang, N. Jiang, J. Li and Y. Wu, J. Phys. D: Appl. Phys., 2019, 52, 224003 CrossRef CAS.
  52. G. Niu, Y. Qin, W. Li and Y. Duan, Plasma Chem. Plasma Process., 2019, 39, 809–824 CrossRef CAS.
  53. D. Mei, X. Zhu, Y.-L. He, J. D. Yan and X. Tu, Plasma Sources Sci. Technol., 2014, 24, 015011 CrossRef.
  54. B. Wang, X. Wang and B. Zhang, Front. Chem. Sci. Eng., 2021, 15, 687–697 CrossRef CAS.
  55. D. Mei and X. Tu, J. CO2 Util., 2017, 19, 68–78 CrossRef CAS.
  56. R. Aerts, W. Somers and A. Bogaerts, ChemSusChem, 2015, 8, 702–716 CrossRef CAS PubMed.
  57. A. Zhou, D. Chen, C. Ma, F. Yu and B. Dai, Catalysts, 2018, 8, 256 CrossRef.
  58. J. Li, S. Zhu, K. Lu, C. Ma, D. Yang and F. Yu, J. Environ. Chem. Eng., 2021, 9, 104654 CrossRef CAS.
  59. L. He, X. Yue, X. Liu and Z. Wu, J. Phys. D: Appl. Phys., 2025, 58, 105204 CrossRef.
  60. H. Yukio, P. Emeraldi, T. Imai and S. Kambara, Int. J. Plasma Environ. Sci. Technol., 2023, 17, e01007 Search PubMed.
  61. I. Michielsen, Y. Uytdenhouwen, J. Pype, B. Michielsen, J. Mertens, F. Reniers, V. Meynen and A. Bogaerts, Chem. Eng. J., 2017, 326, 477–488 CrossRef CAS.
  62. D. Ray, P. Chawdhury, K. V. S. S. Bhargavi, S. Thatikonda, N. Lingaiah and Ch. Subrahmanyam, J. CO2 Util., 2021, 44, 101400 CrossRef CAS.
  63. M. Umamaheswara Rao, K. Bhargavi, G. Madras and Ch. Subrahmanyam, Chem. Eng. J., 2023, 468, 143671 CrossRef CAS.
  64. X. Duan, Z. Hu, Y. Li and B. Wang, AIChE J., 2015, 61, 898–903 CrossRef CAS.
  65. M. Xia, W. Ding, C. Shen, Z. Zhang and C. Liu, Ind. Eng. Chem. Res., 2022, 61, 10455–10460 CrossRef CAS.
  66. D. Mei, X. Zhu, C. Wu, B. Ashford, P. T. Williams and X. Tu, Appl. Catal., B, 2016, 182, 525–532 CrossRef CAS.
  67. Y. Gao, R. Zhou, B. Chen, L. Xiao, X. Zhao, J. Sun, R. Zhou, J. Zhang and Z. Liu, ACS Sustainable Chem. Eng., 2024, 12, 10993–11005 Search PubMed.
  68. Y. Uytdenhouwen, S. Van Alphen, I. Michielsen, V. Meynen, P. Cool and A. Bogaerts, Chem. Eng. J., 2018, 348, 557–568 CrossRef CAS.
  69. M. Suvarna, T. P. Araújo and J. Pérez-Ramírez, Appl. Catal., B, 2022, 315, 121530 Search PubMed.
  70. X. Yuan, M. Suvarna, S. Low, P. D. Dissanayake, K. B. Lee, J. Li, X. Wang and Y. S. Ok, Environ. Sci. Technol., 2021, 55, 11925–11936 Search PubMed.
  71. X. Wang, X. Du, K. Chen, Z. Zheng, Y. Liu, X. Shen and C. Hu, ACS Sustainable Chem. Eng., 2023, 11, 4543–4554 CrossRef CAS.
  72. T. N. Nguyen, T. T. P. Nhat, K. Takimoto, A. Thakur, S. Nishimura, J. Ohyama, I. Miyazato, L. Takahashi, J. Fujima, K. Takahashi and T. Taniike, ACS Catal., 2020, 10, 921–932 CrossRef CAS.
  73. G. A. Lyngdoh, M. Zaki, N. M. A. Krishnan and S. Das, Cem. Concr. Compos., 2022, 128, 104414 CrossRef CAS.
  74. R. Kumar and A. K. Singh, NPJ Comput. Mater., 2021, 7, 197 CrossRef.
  75. J. Li, L. Pan, M. Suvarna and X. Wang, Chem. Eng. J., 2021, 426, 131285 CrossRef CAS.
  76. R. Vertongen, G. De Felice, H. van den Bogaard, F. Gallucci, A. Bogaerts and S. Li, ACS Sustainable Chem. Eng., 2024, 12, 10841–10853 CrossRef CAS PubMed.
  77. J. Sun, Q. Chen, Y. Guo, Z. Zhou and Y. Song, J. Energy Chem., 2020, 46, 133–143 CrossRef.
  78. J. Osorio-Tejada, M. Escriba-Gelonch, R. Vertongen, A. Bogaerts and V. Hessel, Energy Environ. Sci., 2024, 17, 5833–5853 RSC.
  79. R. Brandenburg, M. Schiorlin, M. Schmidt, H. Höft, A. V. Pipa and V. Brüser, Plasma, 2023, 6, 162–180 CrossRef CAS.
  80. H. Hatami, M. Khani, S. A. Razavi Rad and B. Shokri, Heliyon, 2024, 10, e26280 CrossRef CAS PubMed.
  81. N. Wang, H. He, Y. Wang, B. Xu, J. Harding, X. Yin and X. Tu, Energy Convers. Manage., 2024, 300, 117879 CrossRef CAS.
  82. C. Lan, H. Zhu, D. Liu and S. Zhang, Environ. Sci. Technol. Lett., 2026, 13, 34–40 CrossRef CAS.
  83. R. Anirudh, R. Archibald, M. S. Asif, M. M. Becker, S. Benkadda, P.-T. Bremer, R. H. S. Budé, C. S. Chang, L. Chen, R. M. Churchill, J. Citrin, J. A. Gaffney, A. Gainaru, W. Gekelman, T. Gibbs, S. Hamaguchi, C. Hill, K. Humbird, S. Jalas, S. Kawaguchi, G.-H. Kim, M. Kirchen, S. Klasky, J. L. Kline, K. Krushelnick, B. Kustowski, G. Lapenta, W. Li, T. Ma, N. J. Mason, A. Mesbah, C. Michoski, T. Munson, I. Murakami, H. N. Najm, K. E. J. Olofsson, S. Park, J. L. Peterson, M. Probst, D. Pugmire, B. Sammuli, K. Sawlani, A. Scheinker, D. P. Schissel, R. J. Shalloo, J. Shinagawa, J. Seong, B. K. Spears, J. Tennyson, J. Thiagarajan, C. M. Ticoş, J. Trieschmann, J. van Dijk, B. V. Essen, P. Ventzek, H. Wang, J. T. L. Wang, Z. Wang, K. Wende, X. Xu, H. Yamada, T. Yokoyama and X. Zhang, IEEE Trans. Plasma Sci., 2023, 51, 1750–1838 CAS.
  84. M. D. Wilkinson, M. Dumontier, Ij. J. Aalbersberg, G. Appleton, M. Axton, A. Baak, N. Blomberg, J.-W. Boiten, L. B. da Silva Santos, P. E. Bourne, J. Bouwman, A. J. Brookes, T. Clark, M. Crosas, I. Dillo, O. Dumon, S. Edmunds, C. T. Evelo, R. Finkers, A. Gonzalez-Beltran, A. J. G. Gray, P. Groth, C. Goble, J. S. Grethe, J. Heringa, P. A. C. ‘t Hoen, R. Hooft, T. Kuhn, R. Kok, J. Kok, S. J. Lusher, M. E. Martone, A. Mons, A. L. Packer, B. Persson, P. Rocca-Serra, M. Roos, R. van Schaik, S.-A. Sansone, E. Schultes, T. Sengstag, T. Slater, G. Strawn, M. A. Swertz, M. Thompson, J. van der Lei, E. van Mulligen, J. Velterop, A. Waagmeester, P. Wittenburg, K. Wolstencroft, J. Zhao and B. Mons, Sci. Data, 2016, 3, 160018 CrossRef PubMed.
  85. S. Nath, J. R. Vella, D. B. Graves and A. Mesbah, NPJ Comput. Mater., 2025, 11, 231 CrossRef.
  86. J. Li, X. Lu, S. Li and A. Bogaerts, ENG. Chem Eng., 2026, 20, 62 Search PubMed.

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