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Article

NPG–TRIS Thermal Storage System. Quantification of the Limiting Processes: Sublimation and Water’s Adsorption

by
Noelia De La Pinta
1,*,
Sergio Santos-Moreno
1,2,3,
Stephania Doppiu
2,
Josu M. Igartua
1,
Elena Palomo del Barrio
2,4 and
Gabriel A. López
1
1
Physics Department, University of the Basque Country UPV/EHU, 48940 Leioa, Spain
2
Centre for Cooperative Research on Alternative Energies (CIC energiGUNE), Basque Research and Technology Alliance (BRTA), Alava Technology Park, 01510 Vitoria-Gasteiz, Spain
3
TECNALIA, Basque Research and Technology Alliance (BRTA), San Sebastián Technology Park, 20009 Donostia-San Sebastián, Spain
4
Ikerbasque, Basque Foundation for Science, 348013 Bilbao, Spain
*
Author to whom correspondence should be addressed.
Crystals 2021, 11(10), 1200; https://doi.org/10.3390/cryst11101200
Submission received: 6 July 2021 / Revised: 10 September 2021 / Accepted: 1 October 2021 / Published: 5 October 2021
(This article belongs to the Special Issue Polymer Dielectrics: Crystalline Materials as Energy Storage Systems)
Browse Figures
Versions Notes

Abstract

:
The NPG–TRIS binary system (NPG = (CH3)2C(CH2OH)2 = 2,2-dimetyl-1,3-propanodiol; TRIS = NH2C(CH2OH)3 = 2-Amino-2-(hydroxymethyl)-1,3-propanediol) was intensively investigated as a thermal energy storage system, due to the reversibility of its phase transitions and their associated energy. An adapted methodology was applied to precisely quantify its sublimation tendency. Relevant thermochemical data were revisited and evaluated using some specific experimental procedures. We also determined that the widely accepted requirement of working in an inert atmosphere to avoid deviations due to hygroscopicity is not necessary. Nevertheless, to take advantage of the energetic properties of the NPG–TRIS system, closed containers will be required to avoid NPG losses, due to its quantitatively determined high sublimation tendency.

Graphical Abstract

1. Introduction

The high level of human activity is leading to the depletion of fossil and natural energy sources. As is well-known, society is continuously looking for alternative energy solutions to overcome this issue. Different approaches have been applied to find new alternative energy sources and new methods to store energy. In this context, the use of thermal energy storage (TES) is a suitable strategy to achieve efficiency in cold energy storage [1], in solar energy storage [2,3], in textile applications [4], in electronic devices [5,6], and in the building field [7,8], among others. In fact, during the 1970s global energy crisis some publications showed how phase change thermal energy storage was applied [9].
Since the 1970s, phase change materials (PCM) [10,11] have been studied as potential thermal energy storage materials, due to the high values of the latent heat of phase transitions and their high energy density. Some of the most common systems are still being studied [12,13], and even carrying out ternary combinations between them [14]. Solid–solid and liquid–solid PCMs enable storing large amounts of thermal energy, with low associated costs, in small volumes [15,16,17,18], and nearly isothermal conditions [19]. However, liquid–gas PCMs are not attractive, because of their very large change of volume [20]. In addition, another critical parameter is the range of the temperatures in which the phase transition occurs, because this will be ultimately decisive in the choice of PCM for a potential application [21,22], Considering the mentioned criteria, Sharma et al. [23] analyzed thermal energy storage with PCMs for solar systems and spacecraft. Zhou et al. [24] reviewed thermal energy storage with PCMs in building applications, whereas Chen et al. [25] and Delgado et al. [26] focused their work on microencapsulated PCMs.
Early studies about latent heat storage suggested the use of inorganic materials. Although these materials are good candidates at high temperatures, they present some disadvantages, such as a corrosive character, incompatibility with other materials, and segregation processes during the phase transition, among others [19,27]. Conversely, not having the mentioned drawbacks, for low temperatures the use of organic materials and their mixtures as PCMs has attracted more attention in recent years [15,19]. In this case, researchers have considered several properties as important factors: high thermal storage density; small volume change during the phase transition; repeatability of the phase change; thermal stability in the course of heating and cooling cycles; high density, with the ultimate goal of achieving small-sized storage containers; chemical stability; and no toxicity or flammability, among others.
In the wake of promising organic PCMs, during recent years, several studies have been made on systems of polyalcohols and amine derivatives of neopentane. These compounds are also called “plastic crystals”, due to the plastic nature of the high-temperature phase. The orientational disorder in these plastic crystals gives rise to the reversible absorption or release of a large amount of heat upon their solid–solid phase transition to their plastic phases. In this sense, Murril et al. [28] showed that plastic crystals with large substituent groups have their solid–solid transition inhibited. Other studies about the mechanism of this transition were also reported [2,29,30]. The mechanism reported as responsible for the large energy exchange is the formation of hydrogen bonds, which break reversibly during the solid-state transformation [31,32]. In these works, the thermodynamic properties of the involved transitions (transition temperatures, energy changes, etc…) and recommendations for careful sample preparation procedures were emphasized.
The binary system NPG (2,2-dimetyl-1,3-propanodiol, (CH3)2C(CH2OH)2)-TRIS (2-Amino-2-(hydroxymethyl)-1,3-propanediol, NH2C(CH2OH)3) is one of the typical plastic crystals studied as a candidate for thermal energy storage. Although previous studies concerning neopentane derived compounds strongly recommended very controlled humidity conditions to avoid deviations from the desired composition, no quantitative data on the absorbed water content were reported, and only qualitative claims can be found [33,34,35]. With the aim of clarifying the reasons behind the claimed demanding conditions, the influence of environmental moisture in NPG, TRIS, and in a NPG–TRIS mixture were carefully investigated in a quantitative manner. In particular, samples with a peritectic composition were studied, due to their interest as a PCM (Figure S1) (see supplementary materials). To stabilize this influence two different samples were prepared, one under inert gas and the second under laboratory moisture. In addition, the effect of sublimation of NPG was studied under heating and cooling cycles in the NPG–TRIS binary system.

2. Materials and Methods

2.1. Sample Preparations

2,2-dimetyl-1,3-propanodiol (NPG, (CH3)2C(CH2OH)2, CAS number = 126-30-7) and 2,2-dimethyl-1,3-diaminopropane (TRIS, NH2C(CH2OH)3, CAS number = 77-86-1) were purchased from Aldrich with a purity of 99 and 99.8%, respectively. Samples with a peritectic composition of NPG–TRIS system were prepared (XNPG = 0.515 and XTRIS = 0.485; in molar fraction) according to the reported binary equilibrium phase diagram [36] (Figure S1, Table S1). To prepare 5 g of the peritectic composition, 2.575 g of NPG and 2.425 g of TRIS were introduced in a ball-milling container with 3 stainless steel balls (1 g each). The milling was performed for 20 min to obtain a homogeneous sample.
Two different samples with peritectic composition were investigated. One of them was prepared in a glovebox with argon atmosphere and levels of oxygen and humidity below 0.1 ppm (SAr). The other sample, SLab, was prepared and manipulated in ambient conditions (more or less with 70% of humidity). The SAr was kept under inert conditions during the whole process, while the SLab was stored at ambient conditions.

2.2. Equipments

Differential scanning calorimetry (DSC) measurements were carried out using an MDSC Q-2000 calorimeter manufactured by TA Instruments (New Castle (DE), USA) with T-zero hermetically closed aluminum pans. For the calibration, sapphire and indium were employed. All the experiments were carried out in helium atmosphere. Depending on the experiment, different heating/cooling rates (2 K·min−1 and 10 K·min−1) and temperature ranges were scheduled. Thermogravimetric measurements were performed on a TA Discovery TGA (manufactured by TA Instrument in New Castle (DE), USA) using unclosed HT-aluminum pans under N2 atmosphere (flow rate of 10 mL·min−1) at 5 K·min−1 and 2.5 K·min−1 heating rates. Depending on the experiment, different temperature ranges were set. For temperature calibration of the TG equipment, pure nickel was used. Optical micrographs were produced on a MERLIN Carl Zeiss Instrument (manufactured by Zeiss Vision GMbH in Hallbergmoos, Germany), working temperature range from 308 K up to 433 K. For sample preparation, a Mixer/Mill® High-Energy Ball Mill manufactured by SPEX sample Prep. In Metuchen, NJ, USA (2016 at 1060 cycles·min−1 was used as working conditions).

2.3. Methods

2.3.1. Study of the Water Content

The water content present in the samples prepared under laboratory conditions (SLab) and in the NPG and TRIS compounds was determined by means of DSC. All measurements were acquired using a heating/cooling rate of 10 K·min−1. To prepare DSC specimens a 2-t weight was used to press the materials into 5 mm diameter pads. In order to quantify the water content in these samples, the value of the solidification (or fusion) enthalpy of distilled water (ΔHsolid) under the same conditions was verified in advance. The obtained value (Figure S2) of ΔHsolid = 6.02 kJ/mol was in very good agreement with data reported in literature [37]. The range of temperature for the DSC measurements was selected in such a way that the melting point of water was always included; i.e., SLab was measured from 243 K up to 433 K, and NPG and TRIS were measured between 203 and 388 K and 203 and 413 K, respectively, taking into account their corresponding melting points (396 K for NPG and 445 K for TRIS) and also the temperature of the peritectic reaction (Figure S1). Considering, the dependence of the heat flow, as a function of the temperature, the water content present in the samples was determined using the solidification enthalpy change of water. The associated error was not higher than 5%. This error value is an upper conservative estimation, taking into account that the equipment was calibrated to a sapphire standard and the determination of enthalpy changes was verified for melting of an In reference at several heating/cooling rates, reaching a good agreement with literature data. Exactly the same methodology as applied for the determination of the enthalpy changes in the case of the In reference was used for the investigated samples.

2.3.2. Sublimation Measurements

Measurements of the evaporation rate (dm/dt, rate of mass loss) of compounds were performed using TGA equipment. In order to obtain the temperature dependence of the vapor pressure of the sublimated compound (p), an approximation of a Langmuir equation was used [38,39]. Since the Langmuir approach can only be applied when the compound sublimates to a vacuum, for our termogravimetric measurements a vaporization coefficient “α” had to be introduced. Therefore, the vapor pressure “p” can be expressed as:
p = − ( α A ) ( d m d t ) 2 π R T M
where dm/dt is the rate of mass loss, A is the area of the evaporating surface, M the molecular weight of the effusing substance, and R is the gas constant.
In our case, dm/dt values were measured under isothermal conditions for 20 min every 5 and at 2.5 K, maintaining the same area for each sample. A constant (α/A) value for all measurements was ensured by using powdered samples pressed (2 t) into cylindrical pellets with identical dimensions (5-mm diameter) as those of the aluminum cylindrical crucibles used for the thermogravimetric measurements [40]. According to the mentioned approach, the dependence of the vapor pressure on the temperature was consistent with the ClausiusClapeyron equation, and the sublimation enthalpy ΔHsub can be determined using the following equation:
Δ H S u b = R ⌈ ln ( ( d m d t ) T 1 · T 1 ( d m d t ) T 2 · T 2 ) ⌉ · ( 1 T 1 − 1 T 2 ) − 1
where T1 and T2 are the temperatures corresponding to two consecutive isothermal measurements.
For calibration and testing of the method, benzoic acid was used as a well-established reference material (recommended by IUPAC for sublimation enthalpy measurements for compounds with a vapor pressure of approximately 0.1 Pa at room temperature (aprox. 298 K)). The TGA isothermal curves were measured every 5 K for 20 min from 318 K up to 370 K (Figure S3). Applying the previously described method, the experimental values obtained for the ΔHSub of benzoic acid (Figure S4) were in agreement with data reported in the literature [41,42,43]. From the acquired data an error of about 5% in the determination of ΔHSub was estimated as an upper conservative limit.

3. Results

3.1. Study of the Water Content in the Samples

In order to verify the reported special handling environmental conditions when manipulating NPG and TRIS and their mixtures [35,44,45,46], the water content present in the pure compounds and in a peritectic sample was reanalyzed and quantified using the method described in Section 2.3.1. As mentioned above, DSC measurements of the samples (SLab, NPG and TRIS) were acquired in temperature ranges that include the temperature of water solidification (melting). Consistently, for all the samples, the enthalpy changes measured upon heating (ΔHFusion) were very similar to those obtained upon cooling (ΔHSolid). To skip duplication, the analysis of the water content was only performed based on ΔHFusion data obtained upon heating.
Figure 1 shows a DSC measurement acquired for SLab, from 240 K up to 433 K. Carefully analyzing these curves, the value of heat flow around 273 K shows a tiny peak, which is directly related with the fusion process of water. The analysis of this peak shows an exothermic process linked the freezing process of water during cooling. Therefore, due to this, the water present in the samples is ascribed to the adsorption process of water.
To clarify this point, the adsorption capacity of water for NPG and TRIS was investigated. One sample of NPG sample was stored under laboratory moisture for 4 months, and other was kept in a glass bottle under dry conditions. In addition to the drying agent the bottle was connected to a rotary vacuum pump to assure rigorously dry conditions. In the case of the TRIS compound, an analogous procedure was applied. Subsequently, DSC measurements were acquired for a temperature range that contained the melting point of water for both NPG and TRIS samples (Figure 2 and Figure 3, respectively).
As can be seen in Figure 2 (see the inset), a comparison of the results of heat flow for samples of NPG stored in laboratory conditions and under dry conditions shows a clear difference around the melting temperature of water. Indeed, although a tiny amount, some water is present in the NPG sample exposed to ambient humidity. However, in the case of the TRIS compound no peak around the melting temperature of water can be observed in the curves (see inset in Figure 3) of any of the samples. The values of enthalpy changes related to water fusion for the NPG and SLab samples are gathered in Table 1. Using these data, the water content in the samples was estimated.
According to these data, it is clear that the TRIS compound did not take on any detectable water, even after storing the sample under laboratory conditions, and that the NPG compound could only absorb 0.32 wt.% weight of water after exposing it to these humidity conditions for 4 months. Hence, considering this fact, it can be said that the adsorbed water in the SLab sample derives exclusively from NPG. Using the peritectic composition and the data of the heat flow (Figure 1), the amount of water in the SLab sample was determined to be just 0.003 wt.% (of the NPG mass).

3.2. Thermal Analysis of the Pure Components and of the Peritectic Compound

Further analyzing the influence of the handling (humidity) conditions on the NPG–TRIS system, the dependence of the molar heat capacity at constant pressure (Cp (J·mol−1·K−1)) for NPG and TRIS compounds handled under laboratory conditions was compared with data acquired under inert atmospheres (Figure 4 and Figure 5). Cp data are also necessary to study the sublimation, which will be addressed in the next subsection. The data obtained in this work are in excellent agreement with adiabatic calorimetry measurements [31] and with modulated differential scanning calorimetry (MDSC) measurements [29].
Following the mentioned purpose, the phase transitions for NPG and TRIS were also revisited for samples handled under laboratory conditions. As is known, NPG appears as an ordered monoclinic phase below 313.8 K. At this temperature, the compound transforms into the orientationally disordered phase (FCC). Meanwhile, this TRIS compound presents an orthorhombic (ordered) phase thermodynamically stable below 406.8 K, where the ordered phase transforms into the disordered body-centered cubic (BCC) phase. The latter phase is stable up to 442.7 K (Figure S5). In the ordered phase of NPG, the molecules are connected by two different types of hydrogen bonds. The arrangement of these molecules forms zig-zag linear chains, which are established by Van der Waals interchain bonds [47]. The orthorhombic arrangement of TRIS shows a layered structure established by strong intermolecular hydrogen bonds, whereas the layers are connected by weak hydrogen bonds. This is due to the different electronegativity between the oxygen and nitrogen atoms present in the structure [48]. The value of the enthalpy change for the solid–solid phase transition (ΔHPT) was determined by the integrals from DSC measurement (Figure S6). As can be seen in Table 2, even though in our experiments the samples of NPG and TRIS were prepared and handled under laboratory conditions (without strict handling under dry conditions in a glove box), the experimental values of the enthalpy changes and temperatures of phase transitions are in very good agreement with the literature data.
Having confirmed that the small amount of water that could be adsorbed in the pure compounds did not have influence on their transitions; the effect of the laboratory humidity on the peritectic reaction for sample SLab was studied and was compared with the results obtained for the SAr sample. Analogous DSC curves acquired in the temperature range 293–433 K for both samples are shown in Figure 6. It is worth mentioning here that the different appearance of the curves lies in the different weights of the samples (23.09 mg-SLab vs. 8.9 mg-SAr). It is evident that the small amount of water present in SLab did not lead to a deviation from the peritectic composition and did not prevent or have a deleterious effect on this reaction with energetic interest. Table 3 summarizes the characteristic data for SLab and SAr, which are in agreement with those reported in the literature [13,20,28,32,44,53,54,55]. To finish this section, peak number five in Figure 6 deserves particular comment. It appeared during the second heating process of the sample and is ascribed to the recrystallization process of the NPG compound. This process takes place starting at the temperature of the solid–solid transition of NPG up to 373 K. Above this temperature, due to the beginning of the melting of NPG, the crystallinity of the sample is lost (see the progressive evolution in the optical micrographs shown in Figure S7).

3.3. The Sublimation of NPG and Its Effect on NPG0.515TRIS0.485

Using the method described in Section 2.3.2, the change of enthalpy during the sublimation process of a commercial NPG sample was studied in the temperature range where the crystal plastic phase of NPG exists; i.e., in the temperature range 313–363 K. The reasons for investigating this process are twofold. On the one hand, if sublimation takes place, compositional changes will occur, with the risk of losing the composition of interest (in this case, the peritectic composition). On the other hand, a certain amount of energy will be lost. The dependence of the evaporation rate (dm/dt) of NPG on the temperature and the mass loss with time, measured under isothermal conditions for 20 min every 5 K, were determined by TGA measurements (Figure S8). Plotting the data of the logarithm of the volatility rate of commercial NPG samples (Figure S9) and applying Equation (2), the dependence of the sublimation enthalpy change for NPG (ΔHsub) was determined as a function of the temperature (Figure 7). It can be observed that ΔHsub shows a decreasing tendency with increasing temperature. This downward evolution is not monotonic, due to the influence of the phase transitions of the NPG upon the sublimation process. The solid–solid phase transition was observed before 320 K, and the effect of the melting process was determined at just over 358 K.
Going one step further, the sublimation of NPG was investigated more precisely, applying the same procedure in a smaller temperature range (313–363 K) to avoid the influence of these phase transitions (experimental results shown in Figures S10 and S11 were used). In this case, the measurements were acquired under isothermal conditions for 20 min every 2.5 K. For this selected temperature range, Figure 8 shows a remarkably linear dependence of ΔHsub on the temperature; i.e., only the sublimation of NPG takes place.
The marked dependence of ΔHsub on temperature was already noticed by Font et al. [56], although they did not report the temperature variation of the sublimation enthalpy for the whole plastic phase range. In this reference, the authors reported values of ΔHsub acquired using a calorimetric method with Knudsen effusion cells, and only at two different temperatures close to the solid–solid phase transformation point: i) just before the solid–solid phase transition (311.3 K, ΔHsub = 87.6 kJ·mol−1); and ii) just after the solid–solid phase transition (318.6 K, ΔHsub = 75.5 kJ·mol−1). Taking into account the assumed associated error of 5%, our experimental values of ΔHsub for these two temperatures (Figure 7) are in an agreement with these data.
Having quantified the marked sublimation of NPG in a wide temperature range, it was required to investigate its effect on the behavior of the binary peritectic NPG0.515TRIS0.485 sample. Two SLab samples with different treatments were analyzed by thermogravimetry. One of them (SLab) was only ball milled, while the other (SLab+T) was ball-milled and then heated in a hermetically closed DSC holder from room temperature (RT) up to 448 K; i.e., the fusion temperatures of NPG and TRIS were surpassed. Later, both samples (SLab and SLab+T) were placed in an open thermobalance and the mass loss of these samples was measured (Figure 9), using the experimental procedure described in Section 2.3.2. Thermogravimetric measurements were made every 5 K upon heating from 310 K up to 400 K.
Since TRIS has a low sublimation tendency in the investigated temperature range, the mass loss observed corresponds mainly to NPG sublimation. This can be deduced if the data gathered in Table 4 are taken into account. For both samples, the experimental values of the weight loss are almost the same as the nominal NPG contents of the peritectic samples, taking into account the experimental uncertainty. Therefore, sublimation of NPG in peritectic samples or other compositions will occur, in spite of previous treatments in a closed system. However, these treatments can clearly affect the sublimation process, as can be straightforwardly observed from the different trajectories of the curves.
The experimental results of evaporation rate (dm/dt) as a function of time for SLab and SLab+T are showed in Figure 10. For both samples, the experimental dm/dt curves rise sharply with increasing time, followed by an abrupt drop to zero, which is caused by the total sublimation of NPG. Furthermore, it is clearly shown that the thermal treatment of the NPG–TRIS mixture affected the sublimation tendency. Therefore, applying appropriate thermal treatments can be a method of tuning the rate of mass loss caused by NPG sublimation.

4. Conclusions

The experimental results in the current work clarify some practical aspects about the possibility of implementing NPG and its mixtures, for example peritectic NPG–TRIS, as thermal energy storage materials. In opposition to what is usually claimed in the literature, it was proven that environmental moisture does not significantly modify the peritectic composition (by water adsorption) to lead to a composition outside the reported peritectic reaction range (0.46 ≤ XTRIS ≤ 0.53; 0.54 ≤ XNPG ≤ 0.47 at T = 410.7 ± 2.0) [36]. In fact, the water content adsorbed by NPG exposed for 4 months under laboratory humidity conditions was a tiny amount (0.32% of the NPG content), which did not affect the peritectic reaction. Consequently, we consider that it is possible to handle the NPG–TRIS binary under normal environmental conditions, without using the claimed strict dry conditions in a glove box.
The presence of water in the peritectic sample handled in non-controlled conditions (SLab) and in NPG samples at the freezing temperature of pure water indicates clearly that this type of water entered the sample by physisorption, i.e., it is not crystallization water that could affect the phase transition of the compounds. Therefore, the adsorbed water only produces small compositional changes, which do not have significant effects during its handling.
In addition, it was shown that the sublimation of NPG happens during heating in open conditions for a NPG–TRIS mixture. Therefore, working a NPG–TRIS mixture with hermetically closed containers is a requirement that must be taken into account, to avoid changes in composition at invariant points. Hence, taking into account the relatively high sublimation tendency of NPG it is highly recommended to use closed systems for energy storage industrial applications where NPG will be employed.

Supplementary Materials

The following are available online at https://www.mdpi.com/article/10.3390/cryst11101200/s1, Figure S1. Phase diagram of the binary system NPG–TRIS. (x) DSC, (O) Guinier-Simon Technique, (Δ) solubility boundaries determine by s-ray powder diffraction at constant temperature, Table S1. Temperature and concentration values corresponding to the invariant points obtained by the phase diagram of the binary system NPG-TRIS, Figure S2. DSC of distiller water in MDSC Q-2000 calorimeter TA Instruments in the temperature range 203 K-313 K (heating rate was 10 K·min−1), Figure S3. Experimental dependence of evaporation rate (dm/dt) on temperature at each temperature for Benzoic Acid, Figure S4. Dependence of the enthalpies of sublimation of the benzoic acid on temperature. Blue circles show our experimental data. Values of the literature data: red circles, green squares, and black triangles, Figure S5. Thermograph obtained at 2 K·min−1 heating rate for commercial samples (a) NPG and (b) TRIS, Figure S6. Dependence of the ΔHPT with the temperature for (a) NPG and (b) TRIS compounds, Figure S7. Photographs taken with the cooling of the sample at 333 K, 353 K, and 373 K using a polarization microscope Zeiss Axioplan 2, Figure S8. Experimental results of TGA isothermal measurements for NPG commercial samples every 5 K for 20 min at temperature range 313–370 K. (a) Weight loss with the time. The different colors represent the isotherms every 5 K during 20 min; (b) Dependence of evaporation rate (dm/dt) on temperature, Figure S9. Dependence of the logarithm of evaporation rate of commercial NPG compound on reciprocal temperature. NPG sample was measured every 5 K from 313 up to 370 K, where Ln p is L n d m d t T ; t = time   and   T = Temperature , Figure S10. Dependence of evaporation rate of NPG on temperature from 333 K up to 358 K. The measurement was carried out using isothermal conditions every 2.5 K, Figure S11. Dependence of logarithm of evaporation rate of commercial NPG compound on reciprocal temperature. NPG sample was measured every 2.5 K from 333 up to 358 K, where Ln p is Ln d m d t T ; t = time   and   T = Temperature .

Author Contributions

Conceptualization, N.D.L.P. and S.S.-M.; methodology, N.D.L.P., S.S.-M. and SD; data treatment and validation, N.D.L.P. and J.M.I.; investigation, S.S.-M. and S.D.; writing—original draft preparation, N.D.L.P.; writing—review and editing, S.S.-M., S.D., J.M.I., E.P.d.B. and G.A.L.; supervision, S.D. and G.A.L.; project administration, S.D., G.A.L. and E.P.d.B.; funding acquisition, G.A.L. and E.P.d.B. All authors have read and agreed to the published version of the manuscript.

Funding

This study was financially supported by the Basque Government (IT1301-19, IT1364-19) and through the Elkartek18 R&D program, by the University of the Basque Country UPV/EHU (GIU19/019), and by the Ministry of Science and Innovation of Spain (PID2019-106644GB-I00).

Data Availability Statement

All data, models, or code that support the findings of this study are available from the corresponding author upon reasonable request.

Conflicts of Interest

The authors declare no conflict of interest.

Nomenclature and Abbreviations

NPG2,2-dimetyl-1,3-propanodiol
TRIS2-Amino-2-(hydroxymethyl
PCMPhase Change Materials
SArSample prepared in a glovebox with argon atmosphere and levels of oxygen and humidity below 0.1 ppm
SlabSample prepared and manipulated in ambient conditions
SLab+TSample prepared and manipulated in ambient conditions which was heated
DSCDifferential Scanning Calorimetry
TGAThermogravimetric analysis
TGThermogravimetric
HT-aluminum pansHigh Temperature aluminum pans
ΔHsubSublimation Enthalpy
ΔHFusionFusion Enthalpy
dm/dtrate of mass loss
CpMolar Heat Capacity at constant pressure
MDSCModulated Differential Scanning Calorimetry
TPTTemperature of Phase Transition
ΔHPTEnthalpy of Phase Transition
TmMelting Temperature
TiInitial Temperature
TFFinal Temperature
%ΔmexperimentalExperimental mass loss percentage
%ΔmtheoricalTheoretical mass loss percentage
FCCFace Centered Cubic
BCCBody Centered Cubic
XTRIS; XNPGMolar fraction of TRIS or NPG

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Crystals 11 01200 g001 550
Figure 1. DSC of the SLab (peritectic composition under laboratory humidity conditions) acquired at a 10 K·min−1 heating rate.
Figure 1. DSC of the SLab (peritectic composition under laboratory humidity conditions) acquired at a 10 K·min−1 heating rate.
Crystals 11 01200 g001
Crystals 11 01200 g002 550
Figure 2. DSC measurement for the NPG samples; one stored under laboratory moisture for 4 months (red and dash solid line) and the second kept under dry conditions (green and solid line). The heating rate used was 10 K·min−1.
Figure 2. DSC measurement for the NPG samples; one stored under laboratory moisture for 4 months (red and dash solid line) and the second kept under dry conditions (green and solid line). The heating rate used was 10 K·min−1.
Crystals 11 01200 g002
Crystals 11 01200 g003 550
Figure 3. DSC measurement for the TRIS samples; one stored under laboratory moisture for 4 months (red and dash solid line) and the second under dry conditions (green and solid line). The heating rate used was 10 K·min−1.
Figure 3. DSC measurement for the TRIS samples; one stored under laboratory moisture for 4 months (red and dash solid line) and the second under dry conditions (green and solid line). The heating rate used was 10 K·min−1.
Crystals 11 01200 g003
Crystals 11 01200 g004 550
Figure 4. Dependence of molar heat capacity of NPG on temperature from 223 K up to 385 K (heating rate 2 K·min−1). Blue circles are the experimental results for NPG samples handled under non-controlled environmental conditions. Red circles [31], green triangle, and black crosses [29] represent literature data for samples prepared under dry conditions in a glove box.
Figure 4. Dependence of molar heat capacity of NPG on temperature from 223 K up to 385 K (heating rate 2 K·min−1). Blue circles are the experimental results for NPG samples handled under non-controlled environmental conditions. Red circles [31], green triangle, and black crosses [29] represent literature data for samples prepared under dry conditions in a glove box.
Crystals 11 01200 g004
Crystals 11 01200 g005 550
Figure 5. Dependence of molar heat capacity of TRIS on temperature from 223 K up to 433 K (heating rate 2 K·min−1). Blue circles are the experimental results for the TRIS handled under laboratory conditions. Red circles [31], green squares, purple rhombus, pink triangles, and black crosses [29] are literature data acquired using different methods for samples prepared under dry conditions in a glove box.
Figure 5. Dependence of molar heat capacity of TRIS on temperature from 223 K up to 433 K (heating rate 2 K·min−1). Blue circles are the experimental results for the TRIS handled under laboratory conditions. Red circles [31], green squares, purple rhombus, pink triangles, and black crosses [29] are literature data acquired using different methods for samples prepared under dry conditions in a glove box.
Crystals 11 01200 g005
Crystals 11 01200 g006 550
Figure 6. DSC measurements of NPG0.515TRIS0.485 peritectic samples in the temperature range 293–433 K. Blue lines correspond to the sample SAr (prepared and handled under dry conditions). Red lines correspond to the sample SLab (prepared and handled under laboratory conditions). The heating/cooling rate used in this experiment was 1 K·min−1. Peak labels: (1) Eutectoid reaction 1; (2) Eutectoid reaction 2; (3) Peritectic melting; (4) Peritectic solidification and (5) Recrystallization process.
Figure 6. DSC measurements of NPG0.515TRIS0.485 peritectic samples in the temperature range 293–433 K. Blue lines correspond to the sample SAr (prepared and handled under dry conditions). Red lines correspond to the sample SLab (prepared and handled under laboratory conditions). The heating/cooling rate used in this experiment was 1 K·min−1. Peak labels: (1) Eutectoid reaction 1; (2) Eutectoid reaction 2; (3) Peritectic melting; (4) Peritectic solidification and (5) Recrystallization process.
Crystals 11 01200 g006
Crystals 11 01200 g007 550
Figure 7. ΔHsub of NPG as a function of the temperature in the range 313–363 K.
Figure 7. ΔHsub of NPG as a function of the temperature in the range 313–363 K.
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Crystals 11 01200 g008 550
Figure 8. ΔHsub of NPG as a function of temperature (between 333 K and 358 K).
Figure 8. ΔHsub of NPG as a function of temperature (between 333 K and 358 K).
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Crystals 11 01200 g009 550
Figure 9. TGA measurement of SLab and SLab+T samples, from 310 K up to 400 K.
Figure 9. TGA measurement of SLab and SLab+T samples, from 310 K up to 400 K.
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Crystals 11 01200 g010 550
Figure 10. Evaporation rate (dm/dt) for SLab (blue circles) and SLab+T (red squares) over time. The measurements were carried out using an isothermal treatment for 20 min every 5 K.
Figure 10. Evaporation rate (dm/dt) for SLab (blue circles) and SLab+T (red squares) over time. The measurements were carried out using an isothermal treatment for 20 min every 5 K.
Crystals 11 01200 g010
Table
Table 1. Thermoanalytic data obtained by DSC for sample of water, SLab, and NPG compound.
Table 1. Thermoanalytic data obtained by DSC for sample of water, SLab, and NPG compound.
CompoundEnthalpy Change Related Adsorbed Water
(J/g)		Figures in the Article Connected to Enthalpy Changes
Distilled H2O334.20Figure S2
NPG-adsorbed water1.07Figure 2
SLab-adsorbed water4.20 × 10−3Figure 1
The experimental values have an associated error of 5%, as a conservative upper limit.
Table
Table 2. Thermal properties and phase transitions of commercial NPG and TRIS samples handled under laboratory conditions. Literature data are also included in this table.
Table 2. Thermal properties and phase transitions of commercial NPG and TRIS samples handled under laboratory conditions. Literature data are also included in this table.
CompoundLow Temperature PhaseTPT (K)ΔHPT (kJ/mol)High Temperature PhaseTm (K)ΔHF (kJ/mol)Ref.
NPGMonoclinic315.013.6FCC399.04.6[13]
315.012.1403.24.4[49]
314.612.8401.34.4[36]
313.813.0402.44.7[50]
315.213.0402.23.9our study
TRISOrthorhombic408.032.7BCC445.03.3.[13]
407.332.9446.03.0[51]
406.834.0442.73.7[52]
407.234.50445.43.4[50]
411.933.2443.93.3our study
TPT = temperature of phase transition; ΔHPT = enthalpy of transition; Tm = melting temperature; ΔHF = latent heat of fusion; FCC = face centered cubic; BCC = body centered cubic; low phase = phase at low temperature; high phase = phase at high temperature.
Table
Table 3. Temperature and enthalpy values associated with each identified transition for the peritectic samples NPG0.515TRIS0.485; SLab (without special handling, preparation, and storage) and SAr (with special handling, preparation, and storage).
Table 3. Temperature and enthalpy values associated with each identified transition for the peritectic samples NPG0.515TRIS0.485; SLab (without special handling, preparation, and storage) and SAr (with special handling, preparation, and storage).
SLabSAr
PeakTemperature(K)ΔH (J/g)Temperature(K)ΔH (J/g)Assignation
1314.660.9314.357.4Eutectoid temperature 1; [M] + [O] → [CF] + [O]
2391.2102.1393.2106.6Eutectoid temperature 2; [CF] + [O] → [CF] + [CI]
3411.824.2413.726.1Peritectic invariant (melting) [CF] + [CI] → [L] + [CI]
4410.030.4407.528.9Peritectic invariant (solidification); [L] + [CI] → [CF] + [CI]
5*314.098.1309.794.1Recrystallization process, solid-solid transformation
(*) 2nd cycle of thermal treatment. [M] = monoclinic; [O] = orthorhombic; [CF] = face-centered cubic; [CI] = body-centered cubic; [L] = liquid. The experimental values have associated error of 5%, as a conservative upper limit.
Table
Table 4. Thermoanalytic data for SLab and SLab+T samples.
Table 4. Thermoanalytic data for SLab and SLab+T samples.
SampleStepTi(K)TF(K)%Δmexperimental%ΔmtheoricalAssignation
SLab130836850.351.5Sublimation of NPG
SLab+T130837852.051.5Sublimation of NPG
Ti = initial temperature; TF = final temperature, %Δmexperimental = experimental mass loss percentage; %Δmtheorical = theoretical mass loss percentage. The experimental values have an associated error of 5%, as a conservative upper limit.
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De La Pinta, N.; Santos-Moreno, S.; Doppiu, S.; Igartua, J.M.; Palomo del Barrio, E.; López, G.A. NPG–TRIS Thermal Storage System. Quantification of the Limiting Processes: Sublimation and Water’s Adsorption. Crystals 2021, 11, 1200. https://doi.org/10.3390/cryst11101200

AMA Style

De La Pinta N, Santos-Moreno S, Doppiu S, Igartua JM, Palomo del Barrio E, López GA. NPG–TRIS Thermal Storage System. Quantification of the Limiting Processes: Sublimation and Water’s Adsorption. Crystals. 2021; 11(10):1200. https://doi.org/10.3390/cryst11101200

Chicago/Turabian Style

De La Pinta, Noelia, Sergio Santos-Moreno, Stephania Doppiu, Josu M. Igartua, Elena Palomo del Barrio, and Gabriel A. López. 2021. "NPG–TRIS Thermal Storage System. Quantification of the Limiting Processes: Sublimation and Water’s Adsorption" Crystals 11, no. 10: 1200. https://doi.org/10.3390/cryst11101200

APA Style

De La Pinta, N., Santos-Moreno, S., Doppiu, S., Igartua, J. M., Palomo del Barrio, E., & López, G. A. (2021). NPG–TRIS Thermal Storage System. Quantification of the Limiting Processes: Sublimation and Water’s Adsorption. Crystals, 11(10), 1200. https://doi.org/10.3390/cryst11101200

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