Multiscale modeling of dimerization thermodynamics of formic acid

Journal Article (2025)
Author(s)

Dominika O. Wasik (Eindhoven University of Technology)

Silvia Lasala (Lorraine University)

Olivier Herbinet (Lorraine University)

Konstantin Samukov (Lorraine University)

Sofía Calero (Eindhoven University of Technology)

T. J.H. Vlugt (TU Delft - Process and Energy)

Department
Process and Energy
DOI related publication
https://doi.org/10.1016/j.fluid.2025.114356
More Info
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Publication Year
2025
Language
English
Department
Process and Energy
Volume number
594
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Abstract

Heat pumps, which recycle waste heat, are a promising technology for reducing CO2 emissions. Efficiently using low-grade waste heat remains challenging due to the limitations of standard heat exchangers and the need for more effective working fluids. This work introduces a multi-scale methodology that combines force field-based Monte Carlo simulations, quantum mechanics, and equations of state to explore the potential of formic acid as a new reactive fluid in thermodynamic cycles. Formic acid exhibits dimerization behavior, forming cyclic dimers in the gas phase, which can enhance the thermodynamic efficiency of heat recovery systems. The dimerization reaction of formic acid is crucial because it integrates chemical energy into thermodynamic processes, potentially improving the performance of heat pumps and other energy systems. The study implements umbrella sampling in Monte Carlo simulations to compute the thermodynamic properties of HCOOH dimerization, including equilibrium constants, enthalpy, and entropy. Results from two different methods to study dimer formation, namely the dimer counter method and the potential of mean force method, show strong agreement with the enthalpy of dimerization of −60.46 kJ mol−1 and −62.91 kJ mol−1, and entropy of −137.36 J mol−1K−1 and −146.98 J mol−1K−1, respectively. A very good agreement of the Monte Carlo results with Quantum Mechanics and experimental data validates the accuracy of the simulations. For phase equilibrium properties, the Peng–Robinson equation of state, coupled with advanced mixing rules, was applied and compared to Monte Carlo simulations in the Gibbs ensemble. This approach enabled the determination of the Global Phase Equilibrium of the system, vaporization enthalpy, phase composition, vapor and liquid densities of the coexisting phases, and entropy as a function of temperature. The agreement between the thermodynamic model and Monte Carlo simulations confirms the reliability of the methodology in capturing the phase behavior of the system. The findings demonstrate a promising approach for discovering and characterizing new reactive fluids, contributing to more efficient and sustainable energy technologies.