Abstract
Ligands play a crucial role in enabling challenging chemical transformations with transition metal-mediated homogeneous catalysts. Despite their undisputed role in homogeneous catalysis, discovery and development of ligands have proven to be a challenging and resource-intensive undertaking. Here, in response, we present a self-driving catalysis laboratory, Fast-Cat, for autonomous and resource-efficient parameter space navigation and Pareto-front mapping of high-temperature, high-pressure, gas–liquid reactions. Fast-Cat enables autonomous ligand benchmarking and multi-objective catalyst performance evaluation with minimal human intervention. Specifically, we utilize Fast-Cat to perform rapid Pareto-front identification of the hydroformylation reaction between syngas (CO and H2) and olefin (1-octene) in the presence of rhodium and various classes of phosphorus-based ligands. By reactor benchmarking, we demonstrate Fast-Cat’s knowledge scalability, essential to fine/specialty chemical industries. We report the details of the modular flow chemistry platform of Fast-Cat and its autonomous experiment-selection strategy for the rapid generation of optimized experimental conditions and in-house data required for supplying machine-learning approaches to reaction and ligand investigations.

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Data availability
The authors declare that all data supporting the findings of this study are available within the main text and Supplementary Information.
Code availability
The source code for the Pareto-front mapping and digital twin models have been deposited in the repository ‘Fast-Cat’ (https://github.com/AbolhasaniLab).
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Acknowledgements
J.A.B., N.O., M.K., S.S. and M.A. gratefully acknowledge the financial support from Eastman Chemical Company.
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Contributions
M.A. and J.A.B. conceived the project. J.A.B., N.O., S.S. and M.A. designed the algorithms. J.A.B. programmed the Pareto-mapping algorithm and built the flow platform with M.K. N.O. programmed the digital twin models and performed Shapley analysis under advisement of J.R. and M.A. M.K. conducted the reactor benchmarking experiments. J.A.B. conducted the investigations and data anlayses under advisement of J.R. and M.A. M.A. acquired funding and directed the project. J.A.B., N.O. and M.A. drafted the paper. All authors provided feedback on the paper.
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Extended data
Extended Data Fig. 1 Different experimental strategies for fundamental and applied studies of homogeneous catalysis.
(a) Manual vs. (b) automated, vs. (c) autonomous experimental catalysis. Autonomous experimentation utilizes intelligent experiment-selection to fast-track unveiling the full performance map (red pins) of each catalyst/ligand system with minimum human intervention and experimental cost. The red flask represents a reactor for homogeneous catalysis.
Extended Data Fig. 2 Fast-Cat’s hardware validation and benchmarking to quantify the inherent experimental noise.
a) Reaction stabilization time for a given experimental condition in multiples of the reactor residence time. b) Reaction stability across multiple automatic refills of the syringe pumps from the reagent reservoirs (mean of 3 replicates +/− standard deviation). c) Consecutive in-line GC sampling of a single hydroformylation reaction condition. d) Fast-Cat’s experimental noise via random sampling; starting in-flow hydroformylation reaction with condition 1 followed by 5 randomly selected reaction conditions before returning to condition 1 (labelled as condition 7) (mean of 3 samples at each reaction condition +/− standard deviation). Detailed reaction conditions available in the Supplementary Information section Benchmarking and Validation Conditions.
Extended Data Fig. 3 The hydroformylation reaction space exploration of 1-octene with ligand L1 using the digital twin built by the in-house experimental data of Fast-Cat.
a) Surface plots of predicted aldehyde yield with L1 as a function of (i) pressure and temperature, (ii) pressure and olefin to Rh fraction, and (iii) temperature and olefin to Rh fraction. b) Surface plots of predicted aldehyde regioselectivity with L1 as a function of (i) temperature and H2 flowrate, (ii) temperature and ligand to Rh fraction, and (iii) ligand to Rh fraction and H2 flowrate. For all surface plots shown in panels A) and B), the process parameters other than the two variable parameters used for each surface plot were maintained at a constant value (Xi = 0.25, 0.5 and 0.75) for each surface.
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Source Data Extended Data Fig./Table 2
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Bennett, J.A., Orouji, N., Khan, M. et al. Autonomous reaction Pareto-front mapping with a self-driving catalysis laboratory. Nat Chem Eng 1, 240–250 (2024). https://doi.org/10.1038/s44286-024-00033-5
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DOI: https://doi.org/10.1038/s44286-024-00033-5
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