Silicon Tetrachloride as innovative working fluid for high temperature rankine cycles: Thermal Stability, material compatibility, and energy analysis

Silicon Tetrachloride as innovative working fluid for high temperature rankine cycles: Thermal Stability, material compatibility, and energy analysis

Silicon Tetrachloride (SiCl4) is proposed as a new potential working fluid for high-temperature Rankine Cycles. The capability to overcome the actual thermal stability limit of fluids commercially employed in the state-of-the-art Organic Rankine Cycles (ORC) is demonstrated by static thermal stability and material compatibility tests. Experimental static test proves its thermo-chemical stability with a conventional stainless-steel alloy (AISI 316L) up to 650 °C. A preliminary material compatibility analysis performed with optical microscope on the AISI 316L cylinder, after exposure of 300 h to SiCl4 at temperature higher than 550 °C, confirms the potentiality of this fluid when coupled with high-grade heat sources. A thermodynamic analysis has been carried out accounting for the effect of operating conditions on the axial turbine efficiency. A comparison with fluids adopted in medium–high temperature ORCs is performed, evidencing that the proposed fluid could achieve more than + 10 % points as thermal efficiency gain compared to any commercial solutions when coupled with high-temperature sources such as solar, biomass, waste heat from industrial processes and prime movers. A 2 MW SiCl4 cycle operating full-electric at 550 °C reaches a thermal efficiency of 38 %, exceeding values attainable by any other working fluid under similar conditions and power size.

https://doi.org/10.1016/j.applthermaleng.2024.123239

Authors:

  • M. Doninelli, G. Di Marcoberardino, C.M Invernizzi, P. Iora, and M. Gelfi – Università degli Studi di Brescia, Dipartimento di Ingegneria Meccanica ed Industriale, via Branze, 38, 25123, Brescia, Italy
  • G. Manzolini – Politecnico di Milano, Dipartimento di Energia, Via Lambruschini 4A, 20156, Milano, Italy
Experimental investigation of the CO2+SiCl4 mixture as innovative working fluid for power cycles: Bubble points and liquid density measurementsv- Energy Journal

Experimental investigation of the CO2+SiCl4 mixture as innovative working fluid for power cycles: Bubble points and liquid density measurementsv- Energy Journal

Supercritical CO2 is recognized as a promising working fluid for next-generation of high temperature power cycles. Nevertheless, the use of CO2 mixtures with heavier dopants is emerging as a promising alternative to supercritical CO2 cycles in the recent years for air-cooled systems in hot environments. Accordingly, this work presents an experimental campaign to assess the thermodynamic behaviour of the CO2+SiCl4 mixture to be used as working fluid for high-temperature applications, conducted in the laboratories of CTP Mines Paris PSL. At first, bubble conditions of the mixture are measured in a variable volume cell (PVT technique), then liquid densities are measured with a vibrating tube densimeter, for molar composition in the range between 70 % and 90 % of CO2. The Peng Robinson EoS was fine-tuned on the bubble points obtained, resulting in a satisfactory accuracy level. Finally, a non-conventional methodology has been developed to measure bubble points with the vibrating tube densimeter, whose results are consistent with the VLE data obtained with the standard PVT technique. Thermodynamic analysis in next-generation concentrated solar power plant, at 700 °C turbine inlet, confirms the mixture overcomes 50 % thermal efficiency, providing +4.2 % net electrical output over pure supercritical CO2 at equal thermal power from the solar field.

https://doi.org/10.1016/j.energy.2024.131197

Authors:

  • M. Doninelli, G. Di Marcoberardino, C.M Invernizzi, P. Iora – Università degli Studi di Brescia, Dipartimento di Ingegneria Meccanica ed Industriale, via Branze, 38, 25123, Brescia, Italy
  • G. Manzolini, E. Morosini – Politecnico di Milano, Dipartimento di Energia, Via Lambruschini 4A, 20156, Milano, Italy
  • M. Riva, P. Stringari – Mines Paris, PSL University, Centre of Thermodynamics of Processes (CTP), 77300, Fontainebleau, France
Modified ceramic membranes for the treatment of highly saline mixtures utilized in vacuum membrane distillation

Modified ceramic membranes for the treatment of highly saline mixtures utilized in vacuum membrane distillation

Membrane Distillation processes could enable the treatment of highly saline solutions and facilitate minimal (MLD) or zero liquid discharge (ZLD) applications. Ceramic membranes can be a robust alternative to polymeric membranes if they are chemically modified to exhibit hydrophobic qualities to prevent wetting, particularly for vacuum membrane distillation (VMD). This study found that the thin top layer of asymmetrically structured ceramic membranes is robust enough for highly saline and abrasive suspensions and that TiO2 membranes outperform Al2O3 membranes in respect to the mass transport due to their larger support pore size and lower thermal conductivity. A maximum permeate flux of 35 kg/(m2 h) with exceptionally high rejections were measured in VMD using a saline brine with a concentration of 350 g NaCl per kg H2O. Furthermore, a VMD mass transfer model was successfully adopted (based on the Dusty Gas Model) to facilitate the calculation of the mass transfer through asymmetrically structured TiO2 membranes. Model deficiencies such as the underestimation of polarization effects were discussed, and correction factors integrated accordingly. This was done to establish a mass transfer modelling fundament for asymmetrical ceramic membranes used in MD that can be extended in future works and possibly serve as a tool for membrane optimization.

https://doi.org/10.1016/j.desal.2023.116943

Authors:

  • J. Schnittger, T. Hoyer, M. Weyd, I. Voigt | Fraunhofer Institute for Ceramic Technologies and Systems (IKTS), Germany
  • Jeffrey R. McCutcheon | University of Connecticut, Department of Chemical & Biomolecular Engineering, United States of America
  • A. Lerch | TUD Dresden University of Technology, Germany
Ein fortschrittliches Entsalzungssystem mit einem innovativen CO2-Stromkreislauf, der mit erneuerbaren Energiequellen integriert ist

Ein fortschrittliches Entsalzungssystem mit einem innovativen CO2-Stromkreislauf, der mit erneuerbaren Energiequellen integriert ist

Der Anstieg der CO2-Emissionen verursacht große Probleme wie das Abschmelzen der Gletscher und den Anstieg des Meeresspiegels. Um zur Lösung dieser Probleme beizutragen, stellt das Projekt DESOLINATION einen hochmodernen Energiekreislauf für Entsalzungsanlagen vor, bei dem innovative CO2-basierte Mischungen als nächste Generation von Arbeitsflüssigkeiten verwendet werden. In diesem Beitrag werden die Vorteile des Projekts und die technischen Hürden, die bei der Entwicklung der erforderlichen Maschinen überwunden wurden, vorgestellt.

Bei der Entwicklung des thermischen Kreislaufs und der Wahl des Arbeitsmittels wurden wichtige Faktoren berücksichtigt, darunter Sicherheit, Umweltverträglichkeit, Materialverträglichkeit und Effizienz.

Das System stützt sich auf eine Turbomaschine, insbesondere eine Pumpe und einen Expander, um Wärme aus einem primären Solarkreislauf zu gewinnen. Dieser Aufbau ermöglicht eine flexible Wärmeerzeugung bei gleichzeitiger Simulation unterschiedlicher Sonnenverhältnisse.

Eine große Herausforderung war die Wahl der richtigen CO2-Mischung, um ein Gleichgewicht zwischen Effizienz und Zweckmäßigkeit zu finden. Durch die Zugabe eines “Dotierstoffs” zum CO2 konnten die Eigenschaften der Flüssigkeit angepasst werden, so dass das System eine Pumpe statt eines Kompressors verwenden kann. Dadurch wird der Wärmeaustausch effizienter, da die Flüssigkeit auf einer für die Solarwärmequelle geeigneten Temperatur gehalten wird. Es wurden mehrere Dotierstoffe getestet, um den besten für Effizienz und Kompatibilität zu finden.

Eine weitere Herausforderung war die Materialkompatibilität, da die Geräte Temperaturen von bis zu 550 °C standhalten müssen, die für die solarthermische Energietechnik typisch sind. Die endgültige Wahl des Dotierstoffs war ein Kompromiss zwischen der Verringerung der Korrosion und der Maximierung der Leistung.

Im Rahmen des DESOLINATION-Projekts soll 2025 die erste Pilotanlage in Betrieb genommen werden, die wettbewerbsfähige Lösungen mit einem solarthermischen Wirkungsgrad von über 42%, einer effizienten Süßwasserproduktion und bis zu 70% geringeren CO2-Emissionen pro Kubikmeter entsalztem Wasser im Vergleich zu den derzeitigen Systemen bietet.
Characterization of the physical properties of the thermoresponsiveblock-copolymer PAGB2000 and numerical assessment of its potentialities in Forward Osmosis desalination

Characterization of the physical properties of the thermoresponsiveblock-copolymer PAGB2000 and numerical assessment of its potentialities in Forward Osmosis desalination

Forward Osmosis is a promising strategy for desalination processes, however some aspects have to be better characterized to make it competitive with other affirmed technologies. One of these aspects is the selection of the draw agent, i.e., a polymeric solution that has to fulfill different requirements to guarantee both high membrane performances and good regeneration process. Previous studies have identified a thermoresponsive copolymer known as PAGB2000 as potential draw agent. However, in the open literature there is no information on the thermo-physical properties required for a fully characterization of the polymer itself, hence, different experimental campaigns have been conducted to quantify: phase behavior, osmotic pressure, density, dynamic viscosity, thermal conductivity, thermal diffusivity and isobaric specific heat capacity. These properties were then used in a computational model to simulate the whole desalination process. Recovery ratio, specific electric consumption and specific thermal consumption were compared with the ones obtained in a previous work, showing that a detailed characterization of the thermo-physical properties is required to get accurate and realistic predictions of the system performance.

Keywords: Polymer, Draw agent, Forward osmosis, Desalination.

Authors:

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Study on the Operation of the LUTsCO2 Test Loop with Pure CO2 and CO2 + SO2 Mixture Through Dynamic Modeling

Study on the Operation of the LUTsCO2 Test Loop with Pure CO2 and CO2 + SO2 Mixture Through Dynamic Modeling

Within the framework of the Horizon 2020 DESOLINATION (DEmonstration of concentrated SOLar power coupled wIth advaNced desAlinaTion system in the gulf regION) project, CO2-based mixtures will be used as the working fluid of the power cycle coupled with the desalination plant. Desalination technologies require temperatures above 50℃, therefore a fluid with a critical temperature above 70 ℃ is required to perform the compression step in the liquid phase, minimizing compression work and increasing cycle efficiency. Blending CO2 with other fluids, such as SO2, leads to an increase in the critical temperature of the mixture and makes it suitable for transcritical cycles in concentrated solar power applications, while preserving the advantages of pure CO2 over steam cycles. Throughout the DESOLINATION project, CO2 blends will be tested in the LUTsCO2 test loop to provide validation data for the design of heat exchangers. In this work, the adaptation of the test loop to the CO2 blend is investigated. A dynamic model of the test loop is built in MATLAB-Simulink, which allows each component to be modeled independently and to realize a closed-loop cycle model coupled with a controller and real gas property tables. Steady-state simulations of the system are performed and the dynamic model of each component is verified with the design values. As a result, the study highlights the key performance and fluid dynamic differences which arise from the use of a CO2 blend instead of pure CO2.

Keywords:

  • CO2 mixtures
  • Transcritical refrigeration cycle
  • Dynamic model
  • Simulink
Authors:

Giuseppe Petruccelli Lappeenranta-Lahti University of Technology LUT, Lappeenranta, Finland

Teemu Turunen-Saaresti Lappeenranta-Lahti University of Technology LUT, Lappeenranta, Finland

Aki Grönman Lappeenranta-Lahti University of Technology LUT, Lappeenranta, Finland

Afonso Lugo Lappeenranta-Lahti University of Technology LUT, Lappeenranta, Finland