Project area C: Components of Carnot batteries: Fluids (2nd funding period)
Linking dynamics and equilibrium thermodynamics: entropy scaling and density scaling of siloxane mixtures and other working fluids for Carnot batteries
The top-down methodology worked within the SPP 2403 requires accurate data on thermodynamic equilibrium and transport properties to achieve a high efficiency of Carnot batteries. In inverse design, theoretically sound equations describing these properties are necessary to identify optimal working fluids and operating conditions. The development of predictive equations for transport properties has remained well behind that of equilibrium properties, such that it is the objective of the proposed project. In fact, the better availability of equilibrium property data and predictive equations makes exploring the link between transport and equilibrium thermodynamics compelling. Entropy scaling and density scaling, having isomorph theory as a background, are addressed for modeling the shear viscosity and thermal conductivity of pure fluids and mixtures. One of the goals of this project is the elaboration of a trustworthy methodology and recommendations for the application of entropy scaling and density scaling to transport property modeling. Next to systematic investigations on the influence of repulsion, anisotropy and dipolarity on entropy scaling and density scaling, a fully predictive model for the transport properties of the mixture CO2 + butane and its constituent components was developed. This binary system was identified by other groups within SPP2403 as a promising working fluid candidate. It will be applied in Carnot battery process design, although practically no experimental transport property data exist. Moreover, the class of siloxanes was studied in detail, where different scaling approaches were considered in a comparative manner. In the second funding period, the present project will carry out systematic studies with model mixtures of nonpolar, dipolar and quadrupolar components that are directly, but also in a more general sense, related to real working fluid mixtures. The generated understanding will be used to predict the transport properties of the ternary mixture CO2 + ethane + propane, together with its unary and binary subsystems. This system was selected in close cooperation with other groups in SPP2403 because of its presumed suitability for Carnot batteries. In addition, entropy scaling and density scaling will be applied to fluids with hydrogen bonding interactions, which are considered to be particularly difficult cases. The goal is to evaluate the limits of these scaling approaches. This project, as a part of SPP 2403, includes a high level of collaboration with other partners. It is thus not limited to the development of transport property scaling schemes but also includes the supply of equilibrium properties and the study of other fluids according to the specific needs of other SPP 2403 project partners.
Professor Dr.-Ing. Jadran Vrabec
Technische Universität Berlin
Institut für Prozess- und Verfahrenstechnik
Development of Helmholtz-Energy based Multi-Parameter Property-Models for New Binary and Multinary Working-Fluid Mixtures
This project aims to improve the modelling of thermodynamic and transport properties of mixtures of carbon dioxide (CO₂) and alkanes and to establish a reliable data base for the optimization of Carnot-battery energy storage. Such mixtures are promising working fluids because their thermophysical properties can be tuned by changing the composition, enabling more efficient heat exchange and better adaptation to specific temperature profiles. However, reliable experimental data for these mixtures are scarce, and existing models are often not accurate enough for the demanding energetic and exergetic optimization of Carnot batteries. The project therefore focuses on developing new, physically consistent and highly-accurate equations of state and transport property models for CO₂–alkane and alkane–alkane mixtures. A reference model for the CO₂ + propane system will be established using advanced fitting methods and additional constraints that ensure realistic behaviour outside well-measured regions. This approach will then be extended to a wider range of mixtures, including systems with heavier alkanes and multicomponent mixtures – progress made in the first funding period forms the basis for this work. In parallel, a software tool will be developed to analyse how uncertainties in individual thermophysical properties (such as density or enthalpy) influence the results of process simulations while maintaining thermodynamic consistency. This will allow users to assess which properties require high accuracy for a given application and to select appropriate models accordingly. For mixtures containing long-chain alkanes, alternative modelling approaches and coupling strategies between different equation-of-state classes will be explored to overcome the lack of accurate reference models. Furthermore, an optimisation framework will be created to determine mixture compositions that lead to favourable temperature profiles in heat exchangers, supporting efficient Carnot-battery design. For selected binary and ternary CO₂/ethane/propane mixtures, highly accurate viscosity measurements will be performed to provide reliable experimental data for model development and validation. Overall, the project will deliver improved mixture property models, new experimental data, and practical tools for process simulation and optimisation, thereby supporting the development of efficient and economically viable Carnot-battery systems based on natural working fluids.
Professor Dr.-Ing. Roland Span
Ruhr-Universität Bochum
Fakultät für Maschinenbau
Lehrstuhl für Thermodynamik
Dr.-Ing. Monika Thol, Ph.D.
Ruhr-Universität Bochum
Fakultät für Maschinenbau
Lehrstuhl für Thermodynamik
Prediction and surrogate modelling of thermodynamics properties of mixtures with application to the inverse design under uncertainty
The identification of suitable working fluids for Carnot batteries (CB) is a key challenge in meeting their complex performance requirements. Mixtures are becoming increasingly important as working fluids, but their description via multiparameter Helmholtz equations of state incurs enormous computational costs in process optimization. At the same time, reference data for calibrating mixture models in equations of state are often lacking. The same holds true for the prediction of transport properties, which are indispensable for optimizing real processes. This proposal aims to model relevant mixtures with systematic uncertainty quantification. In addition to thermodynamic properties, we focus on viscosities, modelled by Residual Entropy Scaling (RES) approaches. Uncertainties in both the model parameters and the residual entropy as input into the RES approach will be quantified via novel variants of generalized Bayesian inference. To enable the generation of mixture data required for calibration by molecular simulation, we will advance the Bayesian parametrization of force‐field parameters. Thereby we focus on the sequential strategy to minimise the number of expensive molecular simulations and on enabling the simultaneous determination of numerous transferable parameters for an entire component family. Further challenges arise from incorporating both equilibrium data and transport properties into the parametrization. Using viscosity data from molecular simulations, both as targets in force‐field fitting and as reference in the Bayesian inference of RES models, also requires methods to reduce the statistical uncertainty of the simulation results. Building on our achievement from the first funding period, we will construct Gaussian process surrogates for thermodynamic properties, facilitating the embedding of our mixture models into process simulations and the inverse design workflows of our project partners. Together with robust viscosity models and comprehensive uncertainty quantification, these tools will enable the reliable selection of the optimal working‐fluid mixture and determination of its ideal composition from a CB process perspective.
Prof. Dr.-Ing. Gabriele Raabe
Technische Universität Braunschweig
Fakultät für Maschinenbau
Institut für Thermodynamik
Professor Dr.-Ing. Ulrich Römer
Technische Universität Braunschweig
Fakultät für Maschinenbau
Institut für Dynamik und Schwingungen