Project area C: Components of Carnot batteries: Fluids (2nd funding period)

Monitoring and prediction of variable load conditions for Carnot Battery components based on heat transfer and non-intrusive measurements

Heat exchangers are key components within Rankine-based Carnot Batteries. One approach to improve the efficiency of these thermodynamic cycles involves the utilization of zeotropic refrigerant mixtures instead of pure working fluids. The prediction of heat transfer characteristics for boiling and condensation as well as monitoring of part load conditions, are of particular interest for system design and control. Non-intrusive sensors, combined with machine learning (ML) methods, offer promising opportunities for condition monitoring and optimisation of heat exchangers in application-oriented systems. Within this project, a tube bundle test rig is employed to measure boiling heat transfer. These experimental investigations determine heat transfer coefficients under varying pressure, heat flux and vapor quality. Furthermore, an existing condensation test section is expanded with a second test tube. By this measure, data at higher mass flux densities and corresponding annular flow regimes are collected. The heat transfer measurements are conducted simultaneously using non-intrusive sensors. Suitable instrumentation includes a fiber-optic temperature measurement system, an infrared thermography camera, a passive acoustic sensor, and active ultrasonic transducers. The measurement data enables conclusions regarding circumferential temperature distribution, boiling regime, flow conditions, and heat transfer coefficients. Moreover, these datasets are used to develop a model for monitoring and prediction of part load operation. The experimental data undergo in a first step an exploratory analysis, Data are cleaned concerning missing values and outliers, and statistical metrics are computed. The objective is to identify correlations between the signals from the non-invasive sensors and the heat transfer measurements. Subsequently, a modeling approach focusses ML techniques. These supervised learning methods enable the generalization of patterns from the measurement data and the characterization of component behavior under variable operating conditions. The data are subsequently splitted into training, validation, and test sets. The model training process consists of setting up the network structure through hyperparameter tuning. The optimised models are integrated into the experimental facility to evaluate and monitor system performance during a second measurement phase. Based on this, selected models undergo further refinement within an iterative process involving training and validation. Additionally, the developed models are intended to be tested at both the component and system levels in collaboration with cooperation partners of the priority programme.

Professor Dr.-Ing. Dieter Brüggemann
Dr.- Ing. Florian Heberle
Universität Bayreuth
Fakultät für Ingenieurwissenschaften
Lehrstuhl für Technische Thermodynamik und Transportprozesse

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 

Impact of the Improvement of the Evaporator on the Efficiency of Carnot Batteries by reducing the minimal Driving Temperature Differences

The Carnot battery serves as sustainable storage for electrical energy of fluctuating renewable energy sources and consists of different energy conversion processes, the electrical energy is converted in heat by a heat pump, to transfer the heat into a storage converted to inner energy. In the case of requirement of electrical energy, the heat is transferred from the thermal storage to a heat engine to receive the electrical energy by a turbine. In consequence, the Carnot battery itself is a time-varying system and all components are exposed to a strongly transient behaviour. This is particularly important for the heat exchangers, because they are more or less "inertial" depending of various influence parameters. According to the hypothesis of the priority programme – starting from the target variable (energy market, Subject area A) via the Carnot battery (Subject area B) to their component as machines, apparatus, storage and fluid (Subject area C) – the heat exchanger as main coupling component between heat pump, storage and heat engine has to be investigated to the specification of the demands of Subject area B and at least A. The most efficient heat exchangers are those with phase change of the heat pump and the heat engine with the largest potential for improvement in the evaporator. The thermal storage concept and material (sensible heat or latent heat) leads to strongly time-dependent heat flows which affect the design of the heat exchanger. The theoretical total efficiency for an ideal Carnot Battery is 100 %, if there are no exergy losses at all. The efficiency of the heat exchanger depends strongly from the driving temperature difference as function of the heat transfer mechanisms. Therefore, the knowledge of the real boiling mechanisms in heat transfer are essential for the design of the evaporator. For low superheat, convective boiling is expected, as well as for high superheat nucleate boiling. Nucleate boiling results in significantly smaller size and lower operating costs as well as procurement costs (material and fluids) than convective boiling. Low operating as well as procurement costs of the heat exchangers are essential to achieve the project goals of efficient Carnot battery (Subject area B and A). Consistent experimental and theoretical analysis of the charging and discharging of the Carnot Battery, the influence of the transient behaviour of the thermal storages and the boiling mechanisms within the evaporator will be investigated. Their effect on convective and nucleate boiling, the activation criteria of nucleation and bubble formation and finally in heat transfer during boiling is analysed. The deeper understanding of the complex transport processes in the evaporator lead to establish correlations for the design of evaporator at one side (Subject area C) and for the thermodynamic and thermo-economic modelling of the Carnot battery on the other side (Subject area B).

Professorin Dr.-Ing. Andrea Luke
Institut für Thermische Energietechnik
Fachgebiet Technische Thermodynamik
Universität Kassel