Experimental characterization of the LiCl/vermiculite composite for sorption heat storage applicationsCaractérisation expérimentale du composite LiCl/vermiculite pour les applications de stockage de chaleur par sorption

https://doi.org/10.1016/j.ijrefrig.2018.08.006Get rights and content

Highlights

  • Experimental characterization of sorption composite for thermal energy storage applications.

  • Evaluation of sorption enthalpy, cycling stability and sorption kinetic.

  • Results validation by means of a lab-scale prototype operating under seasonal storage conditions.

Abstract

The present paper reports about the experimental characterization of a recently developed composite sorbent of water, LiCl/vermiculite, for thermal energy storage applications. The sorption ability as well as the thermal storage capacity (TSC) of the material itself were tested in a dedicated TG/DSC apparatus, under two relevant boundary conditions, namely, seasonal (SS) and daily (DS) storage applications. The dynamic behavior of the composite sorbent was tested by means of a G-LTJ apparatus in flat-plate adsorber configuration, under both SS and DS working conditions. Finally, preliminary tests on a lab-scale TES configuration were performed and reported. The main outcomes confirm that the composite is promising for TES applications, reaching the TSC up to 2.15 kJ/g under SS conditions. The stability of the composite was proven for 14 consecutive sorption/desorption cycles under conditions similar to those at real SS and DS cycles. The kinetic adsorption tests confirmed a slowdown of the sorption dynamics when passing from 1.7–2.0 mm to 2.36–2.80 mm of the grain size. Furthermore, the adsorption kinetic under SS mode is faster than of DS one. The preliminary testing in the lab-scale TES at SS cycle allowed getting TSC up to 1.25 kJ/g with a specific power up to 2.1 kW/kg.

Introduction

Nowadays heating and cooling demands are accounted for about 50% of the primary energy consumption. Only 18% of this energy is produced from renewable sources (solar, geothermal etc.) and 75% – from fossil fuels (European Commission, 2016). The increasing greenhouse gas emission related to the extensive exploitation of the fossil fuels, is recognized as the first cause of the temperature rise on the Earth and the global environment pollution. Furthermore, industrial activity is a source of immense amount of waste heat, which rejected to the environment by means of hot exhaust gases, cooling media, etc. (Miró et al., 2016). In order to limit these negative factors, the utilization of renewable sources, like solar thermal (Al-Alili et al., 2014) (Döll et al., 2014), as well as the increasing in energy efficiency of processes through waste heat recovery, are strongly promoted during recent years (Scapino et al., 2017). However, the broader utilization of the renewable and waste heat sources is hindered by temporary or geographical mismatch between the production of and demand for the energy they generate. To overcome this barrier, the development of advanced thermal energy storage (TES) systems is mandatory. The TES can be divided into several groups in accordance with the storage mode, namely as sensible (Navarro et al., 2012), latent (Kant et al., 2017) (Veerakumar and Sreekumar, 2016) and chemical reaction (Aydin et al., 2015) (Li et al., 2014). In thermochemical TES the heat is stored as the heat of the broken chemical bonds in reversible chemical reaction that provides some important benefits, namely large thermal storage capacity (TSC) and minor heat losses during the storage period (Cot-Gores et al., 2012). The adsorption TES, belonging to the wider class of thermochemical TES, could represent a promising solution, especially for low temperature energy sources (Frazzica and Freni, 2017). However, contrary to the sensible and latent TES, being in an advanced stage of development, and already applied at large scale in solar thermal plant applications (Kousksou et al., 2014), (Zhang et al., 2016a), the sorption TES is still being under research level with several lab-scale prototypes (Palomba et al., 2017). The researches related to sorption TES are focused substantially on the development of new low cost sorption materials, with enhanced TSC and high cycling stability (Cabeza et al., 2017). The composite sorbents, so-called CSPMs (i.e. Composites “Salt in Porous Matrix”), which contain an inorganic salt inside pores of a matrix, firstly suggested for TES in Levitskij et al. (1996), are considered promising TES materials due to large TSC and tunable sorption behavior (Aydin et al., 2015), (Gordeeva and Aristov, 2012). The inorganic salt, being the main sorbing component, reacts with water vapor and forms crystalline hydrates or/and aqueous salt solution inside pores. The porous matrix is the structural support for the salt; it promotes faster mass- and heat-transfer in the sorbent bed, and accommodates the salt swelling during the hydration. To date, a large number of CSPMs based on various salts, namely CaCl2 (Jänchen et al., 2004), (Levitskij et al., 1996), (Casey et al., 2014), (Permyakova et al., 2017), Al2(SO4)3 (Jabbari-Hichri et al., 2016), MgSO4 (Hongois et al., 2011), MgCl2 (Whiting et al., 2014), SrBr2 (Zhang et al., 2016c), (Courbon et al., 2017), LiBr (Gordeeva et al., 1998) and CaNO3 (Simonova et al., 2009), (Henninger et al., 2017), have been developed as water sorbents for TES. An innovative composite sorbent LiCl/vermiculite has been recently suggested for seasonal and daily TES cycles (Zhang et al., 2016b), (Grekova et al., 2017). LiCl successively reacts with water according to the reactionsLiCl+H2O=LiCl·H2OLiCl·H2O+H2O=LiCl·2H2O

When temperature decreases, the hydrate LiCl⋅2H2O deliquesces forming a LiCl aqueous solution inside the vermiculite pores, which further absorbs water vapor (Grekova et al., 2017). The expanded vermiculite is a cheap natural mineral with extremely large pore volume of 2.4–2.8 cm3/g. This allows a large amount of the salt to be encapsulated and promotes large sorption ability of the composite. The study of water adsorption equilibrium on the composite LiCl (59)/vermiculite with 59 wt% of the salt demonstrated that it adsorbs large amount of water up to 0.85 g/g and can be regenerated at low charging temperature 75–85 °C. That provides promising avenues for its application in TES systems. This paper addresses the characterization of TES ability of the LiCl/vermiculite composite, both at material and prototype levels, as well as the water sorption dynamics, performed under conditions of the TES cycle.

Section snippets

Composite sorbent preparation

The composite sorbent LiCl (52)/vermiculite (Fig. 1b) was synthesized through a dry impregnation method, embedding the LiCl salt inside the pores of a macroporous vermiculite matrix (Fig. 1a). The vermiculite was dried at 160°C for 16 h, impregnated with the appropriate amount of LiCl aqueous solution and dried again at 160°C for 16 h. The salt content was calculated as the weight difference before and after impregnation and drying.

The sorption ability of the CSPMs was shown to grow with the

TSC of the LiCl/vermiculite sorbent

Fig. 5a and b reports the DSC/TG curves obtained for water adsorption/desorption for the SS cycle. Similar curves were obtained for the DS one. In the diagrams the temporary evolution of the temperature (red line), weight variation (TG – blue line) and heat flow (DSC – black line), as well as the integration of DSC peak, are reported.

The two peaks on heat flow curves probably represent the sequential formation of solid hydrate LiCl⋅H2O and liquid solution inside pores.

For DS cycle, the

Conclusions

The present paper reports about the experimental characterization of the composite sorbent of water LiCl/vermiculite developed for TES applications. The analysis was performed referring to two relevant working conditions, namely, seasonal (SS) and daily (DS) storage. The TSC of the material was tested by means of a dedicated TG/DSC apparatus, demonstrating the possibility of reaching up to 2.15 kJ/g and 1.89 kJ/g for SS and DS cycle respectively. Interestingly, the achievable TSC for SS

Acknowledgment

The Russian coauthors thank budget project No. AAAA-A17-117041110045-9 of the Boreskov Institute of Catalysis.

The Italian co-authors thank the project PON “Ricerca e Competitività 2007-13” PON03PE_00206_2 S5 - Smart Small Scale Solar Systems, that has partially funded this activity.

References (39)

Cited by (44)

  • Review of salt hydrates-based thermochemical adsorption thermal storage technologies

    2022, Journal of Energy Storage
    Citation Excerpt :

    Fopah Lele, A. et al. [56] used ethylene glycol as the heating fluid to supply heat to the heat storage material, as shown in Fig. 17(b). Brancato, V. et al. [174] designed a lab-scale closed TCES system (Fig. 18) and tested the dynamic behavior of the composite adsorbent LiCl/vermiculite in a plate adsorbent. De Jong, A.-J. et al. [45] coupled solar energy with the TCES system, designed a vacuum closed thermochemical storage system containing Na2S as active material (Fig. 19).

View all citing articles on Scopus
View full text