Investigations and technical development of adsorption thermal energy storage systems with simulation and different control strategies

Abstract

Thermal energy storage (TES) has been receiving an increasing worldwide attention, especially with the growing concerns about environmental problems caused by an inefficient utilization of energy. A major part of the energy consumption is considered as low temperature thermal energy. Thus, a better management of this energy by using thermal energy storage could provide a significant contribution to improve the overall efficiency of energy utilization in industrial processes and economies. The thermal energy can be stored in different forms e.g. sensible heat, latent heat or thermo-chemical, allowing variety of choices depending on the application. While the sensible and latent heat storage technologies are standard products, the thermo-chemical energy storage is still under development. Based on the method used, thermo-chemical energy storage can be divided into absorptive and adsorptive thermal energy storage systems. The adsorptive thermal energy storage systems have a great potential in both daily (short term) and seasonal (long term) applications. However, their implementation is still limited due to their low degree of applicability caused by lack of scientific knowledge on the thermal analysis level, as well as the absence of knowledge on the level of system integration, which has prevented the heat storage systems from reaching their maximum potential and from being fully commercialized. Consequently, there is still a big necessity for research and development in this field [Salvatore Vasta, 2018]. The principle of the adsorption storage system is based on a gaseous working fluid (e.g. water resp. vapor) which gets adsorbed by a highly porous material (e.g. zeolite). This adsorption process is an exothermal one, thus heat is being released and can be transferred and used. In order to recharge the heat storage system, desorption of the working fluid is done by heating the porous material. The heat storage system consists mainly of a reactor (where the porous material is located), a condenser/evaporator and other auxiliary components (e.g. water tank, pumps, sensors…). Efforts of development of the adsorptive TES were concentrated mainly on developing the adsorptive material, as the performance of the storage material has been the priority so far [Salvatore Vasta, 2018]. Little focus was put on heat power analysis and temperature behavior in the different system components, which have an impact on the overall system efficiency. Thus, system approach is still needed in order to combine and integrate this technology into industrial applications and products [Hauer, Andreas 2020] [Michelangelo Di Palo 2020]. With the aim of improving the heat storage efficiency (recovered heat to stored heat ratio), both numerical (simulations) and experimental (technical modifications) approaches were applied, which have enabled the system to achieve an optimal operational status in terms of energy utilization and efficiency. These approaches were later on used to define a fully automated control system assisting the adsorption TES to instantly react with the continuously varying parameters in such a way to assure an optimal performance. Hence, in the first stage of this investigation, process-modeling and simulation of the whole heat storage system were carried out, so that the total performance of the heat storage system can be predicted and evaluated for any future applications, including the possibility of combining different reactors or heat storage units. In the second stage, different experiments and technical modifications of the system were conducted. This includes testing various possibilities of TES setups (e.g. storage cascades), where the different pressure and temperature behavior in the reactor were evaluated. With the help of experiments, a detailed numerical 3D-model of the packed bed was created, giving an insight into the heat and mass transfer in the reactor during both adsorption and desorption. As a result, a new heat exchanger design was developed, which has improved the temperature distribution and the heating/cooling power. Additionally, the simulation’s results suggested the separation between the evaporator and the condenser to achieve an enhanced water vapor transfer between the reactor and condenser. On a parallel stage of this investigation, comprehensive heat power analysis during both adsorption and desorption processes was carried out, which has showed that the sensible heat left in the reactor, contributes to ca. 50% of the total stored heat. Consequently, multiple reactor concept was introduced, in order to enable the sensible heat recovery. As a conclusion, process simulation enabled tests with different parameters to be performed within much shorter time than the real experimental time. Thus, it was possible to cover numerous application-scenarios and help improving the system overall efficiency. The experimental results have shown that the developed heat exchanger design has increased the maximum power of the heat exchanger about 74%. Moreover, by improving the fluid dynamics between the reactor and condenser, the efficiency of desorption ηd and overall efficiency ηo were increased by 32% and 9% respectively. Furthermore, about 36% of the sensible heat left in the reactor after desorption was recovered by using multiple reactors with sequential configuration, which has led to a reduction in the total invested heat by ca. 9%. For future work it’s recommended to investigate the possibility of controlling the amount of discharged heat from the system by regulating the water uptake during adsorption. In addition, trying a different approach to the reactor’s design (e.g. moving bed reactor) could bring significant improvements to the system.