1. Introduction
Thermal energy storages are one of many energy storage possibilities that need to be assessed in order to implement a sustainable energy provision. One type of thermal energy storage is latent heat storage, which makes use of the latent energy released with the phase change of a material. Commonly, phase change materials (PCM) that transition from solid to liquid and vice versa are used.
The widespread use of PCM applications is often hindered by the negative impact of supercooling. The supercooling effect can be lowered or even prevented by the use of a suitable crystallization triggering method. Next to triggering by a mechanical shock or electric nucleation, nucleation agents (NA) are investigated [
1]. A NA can be an additional material mixed into the PCM typically in a light by weight percentage to not alter the phase change properties significantly. In order to act sufficiently as a NA, the material properties must somehow create a local environment, which facilitates the crystallization of the surrounding PCM. The successful search for NA is still often an empirical process.
The complexity of the NA effect was shown within the work of the joint project LWSNet [
2]. The supercooling behavior of salt hydrates was studied extensively. The role of the epitaxy relation between the crystal surfaces of the NA and the PCM could be identified, yet this property alone is not enough for identifying a suitable NA. Nevertheless, within this work the understanding of the NA effect on salt hydrates was improved. In large compartments or storages, paraffinic PCM commonly do not show a supercooling behavior. This changes significantly once small compartments like microcapsules or emulsions are used. Huang et al. prepared emulsions containing Tetradecane, Hexadecane as well as RT20, a commercial paraffin blend from Rubitherm Technologies GmbH, which all show a large supercooling in the range of 9–15 K [
3]. Gschwander et al., give a detailed analysis on influences on the storage capacity of a range of emulsions consisting of alkanes with an even- and odd-numbered carbon chain. The supercooling of emulsions with Hexadecane and Octadecane was 6.34 K and 4.48 K, respectively, whereas for Heptadecane and Nonadecane it was 3.87 K and 3.22 K, respectively, all with the same purity and from the same supplier. These results indicate that alkanes with an even number of carbon atoms (16 and 18) show a higher degree of supercooling (6.34 K and 4.48 K, respectively) than odd-numbered ones, as well as that shorter alkanes tend to have a higher degree of supercooling. Further measurement showed that emulsions consisting of purer material led to a higher supercooling [
4].
An interpretation on the arising supercooling in micro capsulated and emulsified alkanes can be found in the nucleation theory. A nucleation barrier has to be overcome in order to spontaneously transition from liquid phase to solid. This barrier is described by the bulk free energy and the interface free energy. The interface area refers to the surface area between the two phases, here liquid and solid. Both terms depend on the radius
r, hence the volume, of the nucleus. The two terms depend inversely on
r, resulting in a critical value
r* for which the free energy has a minimum. Once a nucleus with
r* is formed, with addition of molecules, the free energy reduces and the nucleus is more probable [
5]. The nucleation barrier, and hence the formation of nuclei, can be overcome by thermal fluctuations. Therefore, the process is a probabilistic phenomenon. The number of nucleation formation events per time and volume is called the nucleation rate. The nucleation rate depends on the temperature as well, giving a temperature interval from which the rate changes from few nuclei in the long term to many events in the short term. Once the latter state is reached, nucleation can be expected. The corresponding temperature of this specific system is called the nucleation temperature. By applying this theory on the emulsions of paraffinic PCM, Günther et al. [
6] explained the supercooling by the isolated nucleation sites given by the small compartments of PCM. This means that, in a large storage, one nucleation side, whether homogeneous or heterogeneous, can lead to the solidification of the whole system, whereas for emulsion one crystallized compartment will not lead to a phase change in another one inside the emulsion system.
As mentioned above, the use of NA can avoid the supercooling of the PCM. For the case of micro capsulated Octadecane, it was reported by Fan et al. [
7] that two NA—Sodium chloride and 1-Octadecanol—could prevent supercooling, yet lead to drawbacks such as rough capsule surfaces. The best results could be observed with 20 wt% of paraffin as NA. It should be mentioned that not only a NA but also the surfactant could help reduce the supercooling. Hagelstein and Gschwander [
8] reported that using polyvinyl alcohols as surfactants could reduce the degree of supercooling by 10 K. In order to achieve a more holistic understanding on how the NA works, a real time investigation of the crystallization process itself might provide new understandings. The possibilities to study NA-PCM-mixtures experimentally are limited. The crystallization of a material can be investigated for example by X-ray crystallography or Atomic Force Microscopy. Whereas these techniques give information about the progress of crystallization over time, it does not give detailed information about how the NA is supporting the crystallization of the PCM. This information lies on a molecular scale that might be gained by molecular dynamics (MD) simulation.
In recent years, MD simulation has been explored for different paraffin materials. Ewen et al. studied Hexadecane as a lubricant [
9]. He compared, among others, the density and viscosity computed with different force fields used in MD simulation. The results lead to the suggestion that for long-chained alkanes the all-atom OPLS force field for long hydrocarbons, L-OPLS-AA, should be used. Glova et al. [
10] gives a detailed study comparing in total 10 all-atom and united-atom force fields. They simulated an Eicosane system and computed thermal, structural and dynamic properties such as the density, viscosity and crystal structure. Regarding the density values, the united-atom force fields TraPPE, NERD and PYS represented the experimental values the best, among the all-atom force fields OPLS-AA, L-OPLS-AA, and CHARMM36. The result of the temperature-dependent density, simulated for a large temperature range from below and above the freezing point, show for PYS and L-OPLS-AA a rather smooth shift. Whereas for most of the force fields TraPPE, NERD, OPLS-UA, GAFF, GAFF2, CHARMM36 and OPLS-AA show an abrupt transition in the dependency, representing the phase change from liquid to solid. The crystal structure has been reproduced qualitatively by most of the force fields. GROMOS force field being the only exception. Wentzel et al. performed an extensive study on Tricosane, both pure and mixed with Heneicosane, with close attention on the rotator phases [
11,
12]. Using the Flexible Williams force field good results were obtained including structural and thermodynamic properties. A parametric screening of the nucleation on real and hypothetical heterogeneous NA surfaces were conducted by Bourque et al. [
11]. To do so, a variable lattice was simulated in contact with Pentacontane and the crystal growth was studied. Identifying that next to a matching lattice, also the adhesion strengths is a potential parameter to consider for the NA choice. Li et al. [
12] simulated a simplified waxy crude oil with and without ethylene-vinyl acetate EVA in contact with a copper wall using the OPLS-AA force field. The results indicate a reduced crystallization of the wax molecules (Octadecane) on the copper surface when EVA is added.
The aim of this study was to assess the usability of MD simulation as a tool for observing the crystallization process of PCM on a NA surface. The PCM of choice was Octadecane C18, due to previous work on enclosed C18 microcapsules [
13,
14,
15]. Physical properties of a C18 system such as the density, the phase change temperature and the enthalpy as well as the crystal structure were computed and compared to literature values and the authors’ own experimental data in order to verify the simulation method. As a first approach, homogeneous mixtures of solid and liquid C18 were created. This means that a solid C18 nucleus immersed into liquid C18 surroundings acted as a homogeneous NA.
The results are in line with the hypothesis demonstrating that the homogeneous NA grows, if its surface exposes the chain sides rather than the chain ends. With this work, the applicability and therefore the potential of MD simulation to help in a better understanding of the effect of a NA on PCM could be shown.
2. Materials and Methods
The MD simulation principle is based on Newton’s equations of motion solved for a system consisting of a number of atoms. The equations’ solvation is performed considering short time steps. After each time step, the coordinates of each atom are new computed, and the trajectories of the atoms are determined. During the whole simulation time, the predefined number of atoms, temperature and pressure remain in case of a NPT ensemble. Once an equilibrium state is reached, the physical properties of the system can be calculated. To perform the MD simulation the freeware Gromacs® (Version 2019.4) was used.
The solvation of the interaction between atoms is based on force fields, representing both the non-bonded and bonded interactions. The first considers the repulsion, dispersion and Coulomb terms, whereas the second is based on the bond stretching, bond angle and dihedral angle interactions. In order to estimate atom–atom interactions, the parameters to describe the specific force field functions must be available and can be determined empirically or theoretically [
16]. A number of force fields exist that may be suitable for different atomic and molecular systems. As the current study deals with the C18 alkane, the OPLS force field adapted for long hydrocarbons, L-OPLS-AA, after Siu et al. [
17], is chosen. This OPLS is an all-atom force field and uses empirical data and ab initio calculations from a range of alkanes to describe their force field parameters. Aside from the applied force fields, it is necessary to define a cut-off radius. For atoms located within the cut-off range, the non-bonded and bonded forces are calculated. The cut-off radius was chosen to be 1.0 nm (1.0 × 10
−9 m). Periodic boundary conditions in all three directions were applied.
In order to calculate a system with constant temperature and pressure, the system is coupled to a thermostat, a “pressure bath” [
18]. The chosen thermostat was the velocity rescaling temperature coupling with a time constant of 0.1 ps (1.0 × 10
−12 s). The “pressure bath” was realized by Berendsen pressure coupling and set to 1 atm. The time constant was 10.0 ps and the compressibility uniform in all directions with 8.7 × 10
−5 bar
−1. This value was obtained for C18 by taking the experimental data from Dutour [
19] determined for the range of 40 °C to 70 °C and extrapolating the linear correlation to the melting point for which the compressibility was taken. The Berendsen pressure coupling gives a robust simulation box when temperature annealing is applied and quick changes in the box shape due to phase change occur. Nevertheless, the results were validated carefully, as this coupling algorithm stands under the critique of maybe not representing the thermodynamic ensemble correctly [
18].
The validation of the selected force field and parameters was performed by computing the density and phase change enthalpy. Both are properties that can be calculated by Gromacs® for each time step. A system of 216 C18 molecules was exposed to a range of temperatures below and above the melting point. The density was calculated by averaging the density values within a 0.2 ns duration once the system was in an equilibrated state. The results were compared with literature values available for C18 and the authors’ own laboratory measurements. For liquid C18 a densimeter (device: Anton Paar DMA 4500 M; material: Parafol 18-97) was used. The density of the solid C18 was measured via the Archimedes’ Principle using a density kit with a balance (Mettler Toledo). The simulated systems enthalpy was determined in the same manner and duration as the density and was compared with experimental data obtained by DSC measurements (device: TA Instruments DSC Q2000; heating/cooling rate: 2 K min−1, material: Parafol 18-97). The onset temperature of the heating peak given in the DSC thermogram was used for the melting point.
Besides the density and phase change enthalpy, the lattice parameter was determined for a 20 × 4 × 20 C18 system at 6.85 °C. The determination of the distances and angles of the unit cell were done based on the coordinate files of the atoms in the system. The length of the lattice unit cell in the x, y and z directions were calculated by the distance of the Vector between the ninth C-atom of neighboring C18 molecules. In order to determine the angle of the unit cell, the vector between the first and last C-atom of each molecule and its orientation with respect to the x, y and z planes was calculated on the basis of its coordinates.
In order to investigate the crystallization process of liquid C18 molecules onto a solid C18 surface, different solid liquid interfaces were created. The initial system was a 20 × 4 × 20 C18 ensemble. The solid C18 molecules in the initial system are called the NA in the following. Four different cases were defined. Its properties in terms of contact area and number of molecules are given in
Table 1.
Figure 1a illustrates the system and the four NA cases. For a right perception, the NA orientation due to the periodic boundary condition is explained in the following. The NA of case 1 ranges continuously in the x and z direction. The resulting contact area is a plane parallel to the x–z-plane and consists only of chain ends. Case 2 covers a contact area parallel to the y–z direction and its interface area exposes only chain sides. The small NA of case 3 is fully surrounded by PCM (
Figure 1b) and is continuously repeated with every simulation box. The case 4 NA is like a rod infinitely ranging along the z direction (
Figure 1c).
In order to create two phases of C18 molecules next to each other, it was necessary to create two temperature groups representing liquid and solid molecules. By exposing the NA molecules to a temperature far below the freezing point and the remaining molecules to a temperature above the melting point, a system could be provided in which a solid NA exists next to liquid C18 molecules. This configuration was the initial condition, which was used for further simulations in which the temperature was the same for both temperature groups. Three different system temperatures were simulated at −3.15 °C, 6.85 °C and slightly above the melting point at 28.85 °C. A NA-free system was simulated for all three temperatures, to distinguish if the crystallization onset is due to the NA or if it would also happen spontaneously. Contrary to the cases with an already existing NA, nucleation in the NA free case would occur stochastically. For that reason, this case was simulated for each temperature three times and average values were used.
The overall simulation time at a given temperature was 7.2 ns. All simulations were performed with a time step of 0.002 ps. Next to a visual observation of the nucleation process by VMD, a quantitative analysis of the crystallized molecules per time were performed. To distinguish if a C18 molecule was liquid or solid, the length between the first and last C-atom was measured with the Gromacs
® distance function. The threshold length was chosen to be 2.1 nm, based on the results for the lattice constant given in
Section 3.1. Both the molecules of the initial NA and the crystallized molecules were counted. The rate of crystallized molecules at three points of the simulation time were determined and compared for the different NA versions and temperature settings.