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Reaction-network reasoning with frontier models for experimentally confirmed catalyst-selectivity hypotheses
Sutanay Choudhury, Anwesha Banerjee, Udishnu Sanyal, Jorin Dawidowicz, Chiezugolum Ijeoma Odilinye, Jesun Firoz, Liney Arnadottir, Simone Raugei, Johannes Lercher, Arnab Dutta
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Status: succeeded | Model: Gemma-4-26B-A4B | Prompt: intel-v1 | Confidence: 94%
Last extracted: 7/10/2026, 3:16:53 AM
Summary
This paper introduces CoThinker, a human-AI co-thinking framework that uses frontier large language models constrained to explicit reaction networks for mechanism-guided catalyst discovery. Applied to CO2 electroreduction, the framework identifies mechanistic hotspots and control levers (e.g., local pH, Fe incorporation, ketene desorption) to predict a Cu-Fe oxide catalyst architecture. Experimental validation confirms a threefold increase in acetate selectivity, shifting catalyst discovery from retrospective statistical prediction to forward-looking, falsifiable hypothesis generation.
Entities (8)
Relation Signals (6)
CoThinker â identifies â Control Levers
confidence 96% · isolating actionable control levers, specifically local alkalinity, controlled iron incorporation, and restricted interfacial proton-donor accessibility
Copper-Iron Oxide Catalyst â improves â Acetate Selectivity
confidence 95% · demonstrating a threefold increase in acetate selectivity over matched Cu-rich baselines
CoThinker â uses â Frontier Language Models
confidence 95% · forcing a frontier large language model (LLM) to reason exclusively over an explicit reaction network
Explicit Reaction Network â contains â Ketene Desorption
confidence 94% · ketene desorption and hydroxide capture as the acetate-forming pathway
Local pH â governs â Acetate Selectivity
confidence 93% · local alkalinity... guides the prospective synthesis... threefold increase in acetate selectivity
Iron Incorporation â modifies â Copper-Iron Oxide Catalyst
confidence 92% · Fe acts as an electronic modifier that stabilizes CHO-containing intermediates
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Abstract
Abstract:Catalysts are essential for sustainable chemical manufacturing, yet discovering novel architectures remains a bottleneck dominated by trial-and-error experimentation and computationally intensive screening. In complex reactions such as electrochemical carbon dioxide reduction, product selectivity is governed by dynamic interfacial, electrolyte, and potential factors as well as kinetic pathway competition. Conventional descriptor-based machine learning and computational potentials struggle to resolve these mechanistic branch points, primarily relying on static ground-state descriptors or bulk structural correlations rather than end-to-end topological pathway analysis. Here, we show that frontier language models, when strictly constrained to reason over explicit reaction networks, can discover novel catalysts by identifying the physical levers that govern pathway competition. We developed a human-AI co-thinking framework that enforces network invariance to extract testable hypotheses from complex chemical graphs. Applied to CO2 electroreduction, the framework identified ketene desorption and hydroxide capture as the acetate-forming pathway, and predicted a distinct adsorbed CO and CH2 coupling route to ketene. By isolating actionable control levers, specifically local alkalinity, controlled iron incorporation, and restricted interfacial proton-donor accessibility, the framework guided the prospective synthesis of a copper-iron oxide catalyst demonstrating a threefold increase in acetate selectivity over matched Cu-rich baselines. This mechanism-guided reasoning architecture shifts the computational paradigm from retrospective statistical prediction to forward-looking hypothesis generation, providing a broadly applicable blueprint for mechanism-guided materials discovery.
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- Source: https://arxiv.org/abs/2607.08003v1
- Canonical: https://arxiv.org/abs/2607.08003v1
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1 Reaction-network reasoning with frontier models for experimentally confirmed catalyst-selectivity hypotheses Sutanay Choudhury 1* , Anwesha Banerjee 2 , Udishnu Sanyal 1 , Jorin Dawidowicz 3 , Chiezugolum Ijeoma Odilinye 3 , Jesun Firoz 1 , Liney Arnadottir 1,3 , Simone Raugei 1 , Johannes Lercher 4 , Arnab Dutta 2* 1 Pacific Northwest National Laboratory, USA 2 Indian Institute of Technology, Bombay, India 3 Oregon State University, USA 4 Technical University of Munich, Germany * Corresponding authors: Sutanay Choudhury (Sutanay.Choudhury@pnnl.gov); Arnab Dutta (arnabdutta@chem.iitb.ac.in). Abstract Catalysts are essential for sustainable chemical manufacturing, yet discovering novel architectures remains a bottleneck dominated by trial-and-error experimentation and computationally intensive screening. In complex reactions like electrochemical carbon dioxide reduction, product selectivity is governed by dynamic interfacial, electrolyte, and potential factors and kinetic pathway competition. Conventional descriptor-based machine learning and computational potentials struggle to resolve these mechanistic branch points, primarily relying on static ground-state descriptors or bulk structural correlations rather than end-to-end topological pathway analysis. Here, we show that frontier language models, when strictly constrained to reason over explicit reaction networks, can discover novel catalysts by identifying the physical levers that govern pathway competition. We developed a humanâAI co-thinking framework that enforces network invariance to extract testable hypotheses from complex chemical graphs. Applied to CO2 electroreduction, the framework identified ketene desorption and hydroxide capture as the acetate-forming pathway, and predicted a distinct CO*-CH2* coupling route to ketene. By isolating actionable control levers, specifically local alkalinity, controlled iron incorporation, and restricted interfacial proton-donor accessibility, the framework guided the prospective synthesis of a copper-iron oxide catalyst demonstrating a threefold increase in acetate selectivity over matched Cu-rich baselines. This mechanism- guided reasoning architecture shifts the computational paradigm from retrospective statistical prediction to forward-looking hypothesis generation, providing a broadly applicable blueprint for mechanism-guided materials discovery. 2 Introduction From ammonia synthesis 1 to polymer production 2 , catalysts have continuously transformed human civilization. However, the critical challenge on sustainable manufacturing 3 still hinges on effective control of carbonâcarbon coupling i.e., steering the microscopic competition among divergent reaction pathways toward high selectivity. In such systems, several pathways share the same intermediates and diverge at only one or two elementary branch points 11-13 . Consequently, whether a catalyst surface produces to a valuable oxygenate (acetate) or an easier hydrocarbon (ethylene) is set by local environmental factors, such as interfacial acidity and the surrounding electrolyte 4-6 . For such systems, a useful hypothesis must be more than a plausible explanation but provide falsifiable mechanistic reasoning. It must identify a specific mechanistic branch point, the physical quantity that governs it, and an experimental observation capable of verifying the prediction. The computational tools that currently dominate catalyst discovery fail to resolve these critical branch points. First-principles theory is time consuming, in particle for branching reaction networks on complex transition-metal oxides like copper-iron 7 . Machine-learning potentials built to accelerate these calculations and descriptor-based machine learning predicts activity well where data are dense, but lacks the representation to capture the environmental descriptors that actually govern selectivity 8-10 . We overcome these computational blind spots by forcing a frontier large language model (LLM) to reason exclusively over an explicit reaction network 14 , a design principle we term network invariance. By instantiating this directed graph of species and elementary steps as a digital twin, the agent is forced to condition every proposed hypothesis on a shared topological map, ensuring its reasoning is a function of the physical chemistry rather than the model's idiosyncratic priors. Unlike standard scientific agents 15-16 that return broad propositions prone to drift across conversational threads 17-19 , this constraint ensures that the "co-thinking" between human and AI remains rigorously coherent across iterations. Rather than attempting to correlate bulk catalyst features directly to a final product yield, the model is anchored to defined chemical transitions, forcing it to identify the specific mechanistic branch points and localized descriptors such as interfacial acidity that dictate selectivity. To execute this principle, we developed CoThinker, establishing a methodological foundation for mechanistic reasoning as researchers push into novel chemical spaces. The resulting discovery of a 1:1 CuâFe oxide catalyst serves not merely as a performance milestone, but as physical proof of this design principle. The catalyst increases acetate selectivity approximately threefold relative to matched Cu-rich baselines. Although molecularly engineered systems such as dendrimer-functionalized Cu can achieve high acetate Faradaic efficiencies and partial current densities 23 , they rely on complex surface functionalization to construct the active microenvironment. In contrast, the CoThinker-derived catalyst achieves this selectivity through a minimal, earth-abundant mixed-oxide architecture, offering a potentially more scalable route for mechanism-guided catalyst discovery. Crucially, because the agent outputs physical logic rather than purely correlative predictions, we uniquely validate its hypotheses across both domains: confirming the mechanisms theoretically via first- principles computation and proving the outcomes physically through forward experimentation. Unlike established approaches that optimize design spaces via active learning without explicit 3 physical models 20 , or that validate language-model proposals strictly against retrospective computational potentials 21 , this framework shifts the computational objective from predicting a singular winning material to providing a generalizable blueprint for deriving falsifiable, per-step reaction mechanisms. Figure 1 | Reaction-network reasoning for mechanism-guided catalyst discovery. Left, conventional strategies including descriptor-based machine learning, computational screening, and autonomous optimization efficiently explore design spaces but lack explicit mechanistic reasoning. Right, the CoThinker workflow translates a catalytic objective into an explicit reaction network. By evaluating competitive branch points and enforcing end-to-end pathway coherence through a structured reflect-verify-retry loop, the framework extracts experimentally testable mechanistic hypotheses. Applied to the electrochemical reduction of í¶í ! to acetate, this hierarchical planning yields actionable control levers such as local pH, proton accessibility, and Fe incorporation to guide prospective experimental validation. Results The CoThinker framework executes a hierarchical planning workflow 34 grounded in the physical state space of the reaction (Fig. 1). The process initiates when a human expert defines the catalytic objective, which the system formally translates into a mechanistic optimization problem. To establish the topological boundaries of the reasoning task, the platform first constructs the complete reaction network of species and elementary steps. Rather than relying on unconstrained text generation, the reasoning engine navigates this network to identify competitive branch points 14 , quantify step leverage, and assign controlling 4 physical descriptors. Before generating a final hypothesis, the system employs a structured self-critique loop 32,33 for evaluating decisions that may be locally optimal but globally inconsistent 30,31 . The output of this constrained planning phase is a prioritized set of falsifiable control levers, which are subsequently passed to the users for prospective experimental execution. Crucially, every mechanistic claim reported herein is derived solely by a frontier reasoning model (OpenAI GPT-5.4 39 ) operating over its encoded literature knowledge. Present CoThinker architecture deliberately bypasses explicit computational chemistry calculations using ab-initio simulations or neural network potentials (NNPs). While foundational NNPs 24,25 offer rapid energy screening, they suffer from severe out-of-distribution errors at complex electrochemical interfaces 26,27 and are predominantly trained on ground states rather than the transition-state kinetics required to resolve pathway competition 28,29 . Although language models possess inherent inferential uncertainties, intentionally restricting the framework purely to literature-grounded logical deduction in this study prevents the compounding of errors that arises from coupling language generation with unstable numerical extrapolations. Reaction-network reasoning identifies mechanistic determinants of selectivity Figure 2 | Reaction-network analysis identifies the mechanistic determinants of acetate formation on CuâFe catalysts. a, Complete reaction network linking CO 2 activation to competing C 1 and C 2 products through interconnected elementary reaction pathways. The network consists of 32 intermediates, 41 elementary reaction steps, nine reaction pathways, and four product manifolds, enabling explicit representation of pathway competition. b, Mechanistic hotspots extracted from the reaction network. Five high-leverage control elements, including CO* coverage, CO*âCHO* coupling, ketene adsorption strength, buffer-assisted protonation, and hydroxide-assisted ketene capture, govern the distribution of reaction flux, with hydroxide-assisted ketene capture identified as the acetate-forming pathway 13 . 5 Establishing the mechanistic scope of this reasoning task requires constructing an explicit reaction network linking í¶í ! activation to the principal í¶ " and í¶ ! products (Fig. 2). The initial network of 32 chemical species and 38 elementary transformations was iteratively expanded by the reasoning engine to incorporate missing competitive pathways, such as the buffer- assisted protonation of the í»í¶í â intermediate. The resulting complete reaction graph comprises 41 elementary steps spanning the acetate, ethylene, ethanol, methane, and formate manifolds, enabling the evaluation of selectivity as a competition among complete end-to-end pathways rather than isolated reactions. Evaluating this complete network reveals that only a small subset of elementary transformations, specifically five mechanistic hotspots exerts dominant control over product selectivity (Fig. 2 and Table 1). Table 1 shows the exact reasoning summary produced from the CoThinker run. Table 1 | Ranked mechanistic hot-spots for CuâFe CO 2 -to-acetate. # Type Element Descriptors (critical in bold) Mechanistic rationale 1 edge OHâ»-assisted ketene desorption & capture (H 2 CCO* â HâCCO·OHâ») activation barrier; local OH â» activity; transition- state energy; coverage; solvation Decisive acetate-forming step: once ketene is pulled off the surface and trapped by OHâ», flux locks into acetate. Strongest handle for pH. 2 edge Buffer-assisted protonation (HCCO*·Buffer-H â HCCOH*) proton-donor pKâ; interfacial buffer concentration; steric hindrance Key electrolyte/buffer control: accelerates the competing ethylene branch from the shared HCCO* intermediate. 3 edge CHO*âCO* coupling (CHO* + CO* â COCHO*) coverage; d-band centre; coordination number Lowest-barrier CâC entry into the acetate manifold and the clearest role for Fe: Fe stabilisation of CHO* makes coupling competitive against CO loss and C1 hydrogenation. 4 node Adsorbed ketene, HâCCO*@CuâFe binding energy; d-band centre; coordination number; interfacial field Central branch-point intermediate: binding strength sets desorption to solution (acetate) versus further surface reduction (ethylene/ethanol). 5 node CO* coverage on CuâFe local OH â» activity; transition-state energy; coverage; solvation Controls downstream CâC coupling probability; Fe acts indirectly by tuning how much activated CO is supplied near Cu coupling sites. The highest-ranked hotspot was the hydroxide-assisted desorption and solution-phase capture of ketene (í» ! í¶í â ), which the framework identified as the acetate-forming pathway 13 . 6 Because this reaction irreversibly commits the reaction flux toward acetate formation, the activation barrier for ketene desorption, together with the local hydroxide activity, emerged as the strongest mechanistic handle controlling selectivity. The second hotspot corresponded to the protonation of the shared í»í¶í â intermediate by electrolyte-derived proton donors 38 . This elementary step diverts reaction flux from the acetate manifold into the competing ethylene pathway, thereby identifying buffer identity and proton accessibility as critical determinants of selectivity. Third, the framework identified í¶í»í â âí¶í â coupling as the lowest-barrier entry into the acetate-forming pathway and the most probable point at which Fe incorporation influences catalytic behaviour. Rather than acting as an independent active site, Fe was predicted to function as an electronic modifier that stabilizes CHO-containing intermediates sufficiently to promote carbon-carbon coupling while preserving the contiguous Cu ensembles required 5,37 for subsequent reduction chemistry. Fourth, adsorbed ketene emerged as the principal branch-point intermediate controlling the competition between solution-phase acetate formation and continued surface reduction toward ethylene or ethanol. Its adsorption strength, therefore, represents a key kinetic descriptor governing product selectivity. Finally, the surface coverage of í¶í â was identified as the principal descriptor 13 controlling the probability of downstream carbon-carbon coupling. Rather than directly participating in CâC bond formation, Fe was predicted to influence this variable indirectly by modifying the local availability of activated CO species adjacent to Cu-rich ensembles. Iterative reasoning eliminates locally optimal but globally inconsistent designs Because local energetic improvements to individual elementary steps frequently fail to shift macroscopic selectivity 30,31 , true catalyst optimization requires evaluating end-to-end pathway coherence. CoThinker enforces this requirement through a structured reflectâverifyâretry loop that subjects every generated hypothesis to explicit falsification against the complete reaction network (Fig. 3). Rather than accepting the first chemically plausible output, the framework systematically evaluates whether a proposed modification improves the overall reaction flux, maintains internal consistency across competing branches, and remains physically viable under realistic electrochemical conditions. Candidate architectures that fail any of these criteria are discarded and replaced. As captured in the model's raw reasoning logs (Fig. 3), initial reasoning cycles frequently generated candidate designs that seek to optimize local kinetics but failed global network constraints. For example, early proposals incorporating subsurface Fe or conformal fluoropolymer overlayers would effectively lower the activation barrier for initial carbonâcarbon coupling or improved interfacial transport. However, network-wide verification rejected these designs because they either violated scaling-relation constraints 35 , simultaneously lowering barriers for competing ethylene and ethanol pathways, or failed to resolve the unchanged í¶í â âí¶í»í â coupling bottleneck upstream 36 . After executing these structured falsification cycles, the reasoning engine finally converge to an internally consistent architecture: CuâFe oxide interfaces decorated with sparsely distributed hydrophobic ion-conducting domains. Positioned away from contiguous Cu ensembles, this accepted configuration cooperatively addresses the global network constraints by simultaneously stabilizing intermediate coupling, supporting local alkalinity for irreversible ketene capture, and selectively suppressing protonation toward competing pathways without introducing mass-transfer resistance. 7 Figure 3 | Iterative mechanistic refinement of catalyst-design hypotheses. Candidate catalyst designs generated by CoThinker are evaluated using a reflect-verify-retry workflow. The first two designs are rejected because local improvements in individual reaction steps do not translate into enhanced overall acetate selectivity across the complete reaction network. The final design resolves these mechanistic inconsistencies by combining Cu-Fe interfaces with sparse hydrophobic anion- exchange domains, promoting ketene desorption while suppressing competing protonation pathways and preserving contiguous Cu ensembles for CâC coupling. The accepted catalyst is selected on the basis of end-to-end mechanistic consistency rather than isolated energetic improvements. 8 Translating network constraints into physical control levers The outcome of the iterative refinement loop is not a single optimized catalyst composition, but a mechanistically constrained set of experimentally testable design principles (Table 2). Having survived the network-wide falsification process, the accepted architecture, âCuâFe interfaces decorated with sparse hydrophobic anion-exchange domainsâ, was further reasoned in depth to isolate its functional components. Because navigating the unknown catalyst design space carries high computational uncertainty, the framework decomposes this architecture into independent, literature-grounded control variables. By stepping into this unknown space one high-confidence, experimentally falsifiable action at a time, the framework translates a complex structural hypothesis into a directed laboratory campaign. For the Cu-Fe CO 2 reduction system, the accepted catalyst design was distilled into five mechanistic control variables governing acetate selectivity (Table 2). Three of these variables, local pH, proton-donor accessibility, and Fe incorporation, are directly tunable experimentally, whereas ketene binding strength and Cu ensemble size emerge as intrinsic constraints that define the feasible catalyst design space. Together, these variables provide a mechanistic map linking catalyst composition, reaction environment, and product selectivity. Table 2 | Selectivity control levers distilled for Cu-Fe CO 2 -to-acetate. Lever Mechanism Design implication Local pH (OHâ») Promotes concerted ketene desorption and hydroxide capture- the acetate forming pathway Operate at high local pH; choose a morphology generating local alkalinity at the surface Buffer identity & access Interfacial proton donors accelerate the protonation that diverts flux toward ethylene Minimise interfacial proton-donor availability; a sparse hydrophobic binder restricts proton-donor approach Fe role & loading Fe stabilises CHO upstream, enabling COâCHO coupling into the acetate manifold Fe as an electronic modifier near Cu ensembles; retain contiguous Cu domains Ketene binding Adsorbed-ketene binding strength controls desorption-to-solution versus surface reduction Cu-like (moderate) binding preferred; avoid over-binding from excess Fe at active sites Cu ensemble size Contiguous Cu sites are required for CâC coupling Maintain Cu-rich domains; do not atomically dilute Cu into an Fe matrix The highest-priority design principles concern the local reaction environment and electrolyte composition. CoThinker identified hydroxide-assisted desorption and solution-phase capture of ketene as the acetate forming pathway 13 , dictating that any architecture capable of generating local alkalinity should favour acetate formation. This naturally establishes local pH as the primary experimentally controllable design variable. Conversely, because protonation 38 of the shared í»í¶í â intermediate serves as the principal entry point into the competing ethylene pathway, proton-donor accessibility at the catalystâelectrolyte interface must be 9 minimized. Given these constraints and the goal of hypothesis generation, the reasoning model proposed sparse hydrophobic ion-conducting domains. This specific architecture explicitly avoids conformal overlayers that overestimate barrier modifications, instead selectively regulating interfacial proton access while maintaining adequate transport of í¶í ! , water, and escaping ketene. The third experimentally accessible control variable concerns the role of Fe incorporation. The framework consistently predicts that Fe functions as an electronic modifier operating upstream of carbon-carbon coupling, where stabilization of CHO-containing intermediates increases the probability of productive í¶í â âí¶í»í â coupling. However, because contiguous Cu ensembles emerge as a structural prerequisite for efficient carbonâcarbon coupling 37 , excessive Fe incorporation is explicitly predicted to fragment these domains and reduce overall coupling probability. The resulting design principle therefore emphasizes controlled Fe incorporation adjacent to Cu-rich domains rather than the maximization of Fe content. The remaining mechanistic variables define intrinsic structural boundary conditions rather than independently tunable parameters. Most notably, adsorbed ketene acts as the central branch- point intermediate, meaning its adsorption strength must remain sufficiently weak to permit desorption into solution while remaining strong enough to enable productive surface chemistry. Together with the strict structural requirement for contiguous Cu domains, these variables establish the mechanistic limits within which the experimentally adjustable parameters - local pH, electrolyte composition, and Fe loading can be systematically varied. Forward experimental and computational validation of predicted mechanistic control levers To prospectively test the AI-derived mechanistic hypotheses, a series of CuâFe oxide catalysts with varying stoichiometries (Cu:Fe ratios of 4:1, 3:1, 2:1, and 1:1) was synthesized and evaluated independently of the reasoning process. By fixing the mechanistic predictions prior to synthesis, the subsequent electrochemical evaluation serves as a strict forward validation of the predicted control variables rather than a post hoc rationalization of empirical performance. Consistent with the identification of hydroxide-assisted ketene capture as the acetate-forming pathway 13 , elevating the local electrolyte pH systematically shifted reaction flux toward acetate. Increasing the initial bicarbonate electrolyte pH from 6.8 to 7.5 enhanced both acetate production rates and Faradaic efficiencies across all investigated catalyst compositions. The 1:1 CuâFe catalyst exhibited the most pronounced response, directly supporting the theoretical hypothesis that local hydroxide activity fundamentally governs the final branch point independently of bulk catalyst composition. Systematic variation of the Cu:Fe ratio confirmed the framework's prediction that iron functions as a tunable electronic modifier rather than an independent acetate-producing active site. While the Cu-rich 4:1 catalyst predominantly produced formate, progressive iron incorporation smoothly redirected reaction flux into the acetate manifold, culminating in peak acetate selectivity for the 1:1 composition. Crucially, high-resolution transmission electron microscopy (TEM) and elemental mapping revealed that the Cu component maintains contiguous domains across the compositional series, while iron oxide segregates to peripheral regions. This physical architecture perfectly mirrors the network-derived structural requirement: iron 10 modifies the electronic landscape to promote upstream coupling while strictly preserving the contiguous copper ensembles required for subsequent carbonâcarbon bond formation. Modulating the interfacial proton-donor accessibility via electrolyte substitution validated the predicted kinetic competition at the shared í»í¶í â intermediate. Electrolysis performed across bicarbonate, phosphate, and chloride environments revealed stark divergences in acetate selectivity. While bicarbonate electrolytes supported sustained acetate production, phosphate-buffered systemsâwhich provide higher interfacial proton availabilityâexhibited suppressed acetate yields and progressive catalyst passivation. This confirms the system's prediction that local proton-donor accessibility explicitly diverts flux away from the target product toward competing pathways. Figure 5 | Prospective experimental validation of the mechanistic control variables governing acetate formation on CuâFe oxide catalysts. a, Effect of electrolyte pH on acetate selectivity across the CuâFe catalyst series. Increasing the electrolyte pH from 6.8 to 7.5 systematically enhances the Faradaic efficiency for acetate formation, consistent with the predicted role of hydroxide-assisted ketene capture as the acetate forming pathway. b, Product distribution as a function of Cu composition, showing the evolution of acetate, methanol, and formate selectivity. Progressive incorporation of Fe redirects reaction flux toward acetate formation, with the CuFe (1:1) catalyst exhibiting the highest acetate selectivity. c, Influence of electrolyte identity on acetate production for CuFe (4:1) and CuFe (1:1) catalysts, demonstrating the role of proton-donor accessibility and interfacial reaction environment in governing selectivity. d, Representative HAADF-STEM images and elemental 11 maps of the CuâFe catalyst series. The Cu component forms contiguous domains, whereas Fe oxide preferentially occupies peripheral regions, supporting the predicted requirement for contiguous Cu ensembles and positioning Fe as an electronic modifier rather than an isolated active site. Finally, the intrinsic structural constraint requiring weakened ketene binding to promote desorption-to-solution was validated computationally using Universal Machine-learned Potentials (UMA 24 ). Calculating the adsorption energy of isolated Fe substituted into a CuO surface demonstrated a distinct lowering of the ketene adsorption energy from -0.61 eV to - 0.48 eV. This supports the hypothesis that Fe destabilizes the bound intermediate to facilitate solution-phase capture. While comparative calculations substituting íčí ! í $ -like clusters exhibited strong ketene binding, the highly reducing potentials inherent to the cathodic operating conditions suggest the metal-terminated surface represents the physically realistic active state. Thus, targeted computational analysis confirms the final intrinsic lever. Discussion Catalyst discovery has traditionally progressed through an iterative dialogue between mechanistic intuition and experimental validation. While computational chemistry 24,25 and autonomous laboratories 22 have accelerated the execution of these cycles, they generally address either numerical prediction or objective-function optimization rather than scientific reasoning itself. CoThinker introduces a complementary paradigm: it breaks the traditional barriers of knowledge acquisition by shifting the computational objective from retrospective mechanism clarification to forward-looking, mechanism-centred reasoning. By forcing a frontier language model to evaluate the underlying chemistry, the framework helps scientists navigate complex reaction networks faster and more rigorously, extending the role of artificial intelligence from simply accelerating experimentation to defining the precise scientific questions that experiments must answer. The central architectural advance of this framework is the introduction of the explicit reaction network as the core abstraction for machine reasoning. Unconstrained language models are prone to contextual drift 17 over chat threads. CoThinker neutralizes this weakness by enforcing network invariance, anchoring every AI-generated proposition to a shared, physically coherent topological map. By translating the domain-expert mental model into a computable directed graph, the system ensures the humanâAI co-thinking remains rigorously grounded and logically consistent across iterations. This topological grounding naturally addresses the high uncertainty inherent in frontier chemical exploration. Conventional descriptor-based machine learning 10 often fails in these spaces because models trained on bulk composition or static ground-state descriptors lack the representation to capture the highly localized, dynamic environmental variables that govern selectivity 8,9 . Rather than blindly optimizing a latent space, CoThinker decomposes the complex state space into a compact set of independent, high-confidence control levers, such as local pH or proton-donor accessibility, that isolate specific mechanistic branch points. By associating each hotspot with a falsifiable physical descriptor, the framework converts a high- dimensional design space into a sequence of high-confidence, independently testable hypotheses, narrowing the space of viable designs one directed experiment at a time. 12 The experimental validation of the CuâFe catalyst serves as physical proof of this design principle, yielding a threefold increase in acetate selectivity over matched Cu-rich baselines while maintaining comparable overall conversion. The system recovers established physical truths while prioritising specific mechanistic levers. The catalyst passivation observed in chloride electrolytes, for example, is consistent with classical halide poisoning, supporting the network's kinetic constraints. The framework also identifies a distinct acetate-committing route in which CO* couples with a surface methylene (CO*âCH2*) to form ketene, in contrast to the CO-dimerization route to ketene described previously. Because these control levers were fixed prior to synthesis, the outcomes validate the predictions prospectively rather than by post hoc rationalisation, indicating that the framework directed reaction flux away from C1 pathways largely by design. The current framework deliberately isolates language-model reasoning from explicit computational chemistry calculations to strictly prevent error compounding. While neural network potentials (NNPs) offer rapid energy evaluations, they currently suffer from severe out-of-distribution extrapolation errors at complex, multi-component electrochemical interfaces. Furthermore, current foundation models lack the architecture to reliably evaluate the transition-state structures strictly required to resolve kinetic pathway competition. Future iterations must bridge this gap by integrating NNPs via active learning to manage distribution shifts, deploying advanced architectures capable of modelling transition states, and establishing rigorous uncertainty quantification to support a fully closed-loop discovery system. Acknowledgement This work was supported in part by the U.S. Department of Energy (DOE), Office of Science, Office of Basic Energy Sciences, the Division of Chemical Sciences, Geosciences, and Biosciences. Pacific Northwest National Laboratory (PNNL) is a multiprogram national laboratory operated for the DOE by Battelle Memorial Institute under Contract No. DE-AC05- 76RL01830. A.D. and A.B. acknowledge the support of Indian Institute of Technology, Bombay for providing the facilities during this research. Author Contribution S.C. designed the CoThinker framework. S.C., A.D., and U.S. designed the study. J.F., C.I.O., J.D., and L.A. performed the neural network potential-based computational modeling. A.B. performed all experimental studies. S.C., A.D., U.S., and L.A. wrote the manuscript. J.L. and S.R. provided scientific interpretation and guidance on the analysis. All authors discussed the results and commented on the manuscript. 13 Methods CoThinker framework CoThinker is a mechanistically guided reasoning framework designed to support catalyst discovery through structured humanâAI collaboration. Rather than directly predicting catalyst compositions from data, the framework constructs an explicit reaction network from a user- defined catalytic objective and reasons over competing elementary reaction pathways to identify mechanistic control variables governing catalytic selectivity. The workflow consists of four sequential stages: (i) problem formulation, in which the desired catalytic objective and competing products are translated into a structured optimization problem; (i) reaction-network construction, where intermediates and elementary reaction steps are assembled from literature-derived mechanistic knowledge; (i) iterative mechanistic reasoning, which identifies selectivity-determining branch points and experimentally controllable descriptors; and (iv) mechanistic verification, where proposed catalyst modifications are evaluated through repeated reflectâverifyâretry cycles before being advanced for experimental validation. Construction of the reaction network For electrochemical CO 2 reduction, the reaction network was initialized using established mechanistic pathways reported for Cu-based catalysts. Literature-derived elementary reaction steps, adsorbed intermediates, and competing product pathways were assembled into a directed reaction graph. The network was automatically expanded by recursively identifying missing intermediates and competing reaction branches until all experimentally relevant products were connected through complete reaction pathways. Each node represents a chemically distinct adsorbed or solution-phase intermediate, while each edge corresponds to a single elementary reaction step, including proton-coupled electron transfer (PCET), adsorption, desorption, surface coupling, hydrolysis, and solution- phase reactions. The final reaction graph contained 32 intermediates connected by 41 elementary reaction steps, spanning nine complete reaction pathways leading to four principal product manifolds. Mechanistic reasoning and iterative refinement Mechanistic reasoning was performed over the complete reaction network rather than individual catalyst descriptors. Each elementary reaction step was evaluated according to its influence on reaction flux, competition with alternative pathways, and contribution to overall product selectivity. The framework ranked mechanistic hotspots based on their influence on branching behaviour within the reaction network and identified experimentally accessible control variables. Candidate catalyst designs generated during reasoning were subjected to an iterative reflectâ verifyâretry procedure. During each iteration, proposed catalyst modifications were evaluated for (i) mechanistic consistency across the complete reaction network, (i) pathway completeness, (i) compatibility with competing reaction branches, and (iv) experimental 14 feasibility. Designs exhibiting local energetic improvements without improving end-to-end pathway selectivity were rejected and replaced through subsequent reasoning iterations. The reasoning process continued until a catalyst design satisfied all verification criteria or the predefined iteration limit was reached. The CuâFe CO 2 reduction study required three refinement iterations and twenty model calls before convergence to the final mechanistically consistent catalyst hypothesis. Catalyst synthesis A series of CuâFe oxide catalysts with Cu:Fe molar ratios of 4:1, 3:1, 2:1, and 1:1 was synthesized using a modified co-precipitation method. Appropriate amounts of copper and iron precursor salts were dissolved in deionized water and mixed under continuous stirring. Controlled addition of alkaline solution induced simultaneous precipitation of mixed hydroxide precursors, which were aged, washed thoroughly with water and ethanol, and dried under vacuum. The resulting powders were calcined under air to obtain mixed CuâFe oxide catalysts. Detailed synthesis procedures and precursor compositions are provided in the Supplementary Information. Structural characterization Powder X-ray diffraction (XRD) was used to determine crystalline phases. Surface morphology and catalyst microstructure were examined using field-emission scanning electron microscopy (FESEM) and transmission electron microscopy (TEM). High-resolution TEM and elemental mapping were employed to determine the spatial distribution of Cu and Fe within the mixed oxide catalysts. The oxidation states and surface chemical environments of Cu and Fe were analysed using X-ray photoelectron spectroscopy (XPS). The TEM analyses showed that Cu-rich regions remained as contiguous ensembles throughout the CuâFe catalyst series, whereas Fe oxide preferentially formed peripheral domains surrounding the Cu-rich regions. This structural arrangement was compared directly with the mechanistic design principles identified by the reaction-network analysis. Electrochemical CO 2 reduction Electrochemical CO 2 reduction experiments were performed in a gas-tight three-electrode electrochemical cell using a CO 2 -saturated aqueous electrolyte. Catalyst inks were prepared by dispersing catalyst powder in a mixture of solvent and binder and deposited onto carbon paper to form the working electrode. A platinum mesh and Ag/AgCl electrode served as the counter and reference electrodes, respectively. All reported potentials were converted to the reversible hydrogen electrode (RHE) scale. Electrochemical measurements were conducted using CO 2 -saturated electrolytes of varying pH and electrolyte composition to evaluate the mechanistic predictions generated by CoThinker. Current densities were corrected for solution resistance where appropriate. 15 Product analysis Gaseous products were analysed by online gas chromatography equipped with thermal conductivity and flame ionization detectors. 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