Testing the self-cleaning properties of a coordination polymer surface

A Zn(Cys)₂ CP was obtained using the procedure reported by Ferrer et al. (2014). The structure was confirmed by the XRD, FTIR thermal and elemental analysis. This CP is nonporous (the BET surface area is equal to 96 m²/g). The crystallographic data and the structure of this CP were reported previously (Ferrer et al. 2014).

The chromatographic investigations were carried out using a Chrom 4 gas chromatograph with a flame ionization detector (FID). A computer was connected to the gas chromatograph to control, acquire and process the chromatographic data. The adsorbent was placed in glass column (30 cm × 2 mm I.D.) with an absorbent bed length of 22 cm, which corresponded to 0.37 g of Zn(Cys)₂ used. Before adsorption experiments, the column with the adsorbent was conditioned at 403 K for 8 h under a flow of helium.

Methanol and n-octane (A.R. grade) were used as adsorbates. The adsorbates were injected into the column by means of a Hamilton microsyringe. The size of the injected samples was 0.5 µl. The temperature of the injection device was set at 373 K and 433 K for methanol and n-octane, respectively. Additionally in some experiments, to investigated the effect of water on n-octane adsorption, dosed different amounts of water (1, 2, 4 µl) before as well after n-octane injection.

Adsorption isotherms were determined in the range of 313–343 K in 10 K steps at carrier gas flow-rates 30 and 60 cm³/min (measured by means of a bubble gauge). The measured flow-rates at room temperature and atmospheric pressure were corrected for temperature and pressure drop (Paryjczak 1987). Adsorption isotherms were determined using the peak profile method (Paryjczak 1987; Słomkiewicz 2006). The obtained peaks were unsymmetrical for all adsorption systems. This points to the effect of diffusion on the rate of establishment of adsorption equilibrium. Therefore, in calculation of the adsorption isotherms account was taken of the diffusion effect in accordance with the postulates of Dollimore et al. (1970). The isosteric enthalpy of adsorption (q^st) was calculated using isosteres obtained from adsorption data (i.e. using plots of partial pressures (ln p) versus temperatures (1/T) at constant coverages θ) according to the Clausius–Clapeyron equation (Paryjczak 1987; Grob 1995):where R is the gas constant.

The change in the entropy of adsorption (\(\Delta S\)) was calculated with respect to the liquid state using:where \(\Delta G\) and \(\Delta H\) are the change in free enthalpy, and the so-called “pure” enthalpy of adsorption, respectively, p and p_s are the equilibrium and saturated vapour pressures. The values of the saturated vapour pressures (Yaws 2003) and the enthalpy of condensation (Majer and Svoboda 1985) applied during calculations are provided in the Electronic Supplementary Material.

All molecular dynamics (MD) simulations were performed using the OpenMM molecular simulation toolkit (Eastman et al. 2013). As in our previous studies (Włoch et al. 2017a, b, 2018) the TIP4P/2005 (Abascal and Vega 2005) water model was applied. The OPLSAA force field parameters were taken from the TINKER package (Robertson et al. 2015; Lagardère et al. 2018), while the parameters for Zn were taken from the study of Li et al. (2013). First the wetting of the bare CP surface was determined. Next, to study the self-cleaning effect, the monolayer adsorption of hydrocarbons was simulated (C₁₀H₂₂, C₂₄H₅₀ and C₅₅H₁₁₂). Lastly, the water drop was placed on top of the equilibrated alkane monolayer, and the wetting properties were determined again. The hydrocarbon molecules could freely move on a surface (see Electronic Supplementary Material for further simulation details and results).

To check the dynamics of wetting six Zn(Cys)₂ samples were prepared following the procedure described in Electronic Supplementary Material. Three of them were thermally desorbed (T = 393 K) and the remaining three were equilibrated with the saturated C₁₀H₂₂ vapour at the T = 300 K. Next the wetting process was performed using the system described in the Electronic Supplementary Material, and the movies were recorded.

From the data collected in Figures S1 and S2 (Electronic Supplementary Material) one can observe that the carrier gas flow-rate (V_He = 30 and 60 cm³/min) has small influence on the n-octane adsorption isotherms determined in the range of T = 313–343 K. In contrast, we observe the influence of this gas flow-rate on methanol adsorption. This is why for our calculations we used the data determined at the flow 30 cm³/min. As it can be seen from the data collected in Figures S2c and S2d the reproducibility of measurements is very good.

Figure 1 shows the comparison of methanol and n-octane adsorption isotherms on Zn(Cys)₂ determined for the studied temperatures. In the case of both adsorbates one can observe the linear parts of adsorption isotherms at low coverages, and the decrease of adsorption with the rise in temperature (due to the exothermic nature of the process).

Moreover, for all studied temperatures the adsorption of n-octane is smaller than the adsorption of the methyl alcohol (the same sequence of adsorption isotherms is observed at the flow-rate of 60 cm³/min—see Figure S3 in the Electronic Supplementary Material).

Figure 2 shows the comparison of the isosteric enthalpy of adsorption (calculated using Eq. 1) and the change in the entropy of the process (Eq. 2). One can conclude that the q^st values are more negative for n-octane than for methanol. Moreover, the absolute value of methanol adsorption enthalpy progressively decreases due to heterogeneity of the studied CP surface. The rise in the absolute enthalpy value (starting at adsorption ca. 20 µmole/g) is caused by adsorption of subsequent methanol molecule forming surface associates, because it is well known that the adsorption mechanism of polar molecules is usually dominated by clustering around the adsorption sites (Furmaniak et al. 2008). It has been well established that the metal nodes serve as the CP adsorption centers for hydrogen and polar molecules (Rosi et al. 2003). Thus one can expect, that in the case of methanol we observe donor–acceptor interactions with exposed zinc surface cations. As it can be observed in Fig. 2b the absolute value of the n-octane adsorption enthalpy slightly increases at small coverages and next remains almost constant. The enthalpy steadiness is caused by the decrease of the solid–fluid interactions with the concomitant increase of the fluid–fluid interactions, upon rising the surface coverage (Vernov and Steele 1991). It is well proved that the non-polar molecules (like alkanes) during adsorption may form different ordered structures due to adsorbate–adsorbate interactions (Gilbert et al. 1998). Since the n-octane molecule does not possess the dipole moment, the adsorption in this case is not very sensitive to the presence of the surface polar sites. Thus, the observed in Fig. 1 (and Figure S3) better methanol than n-octane adsorption causes more positive entropy change, in comparison to the liquid state (Fig. 2c, d). We conclude that the n-octane molecules due to the strong affinity for the CP surface, as well as due to the fluid–fluid interactions are less mobile than the adsorbed methanol molecules.

The fact that the adsorption of methanol is stronger than the adsorption of n-octane has been also corroborated by the results collected in Fig. 3. In this figure we show the chromatograms of dosed n-octane followed by injection of different volumes of methanol (Fig. 3a) and water (Fig. 3b) into the column. We note that the addition of polar molecules decreases the n-octane retention time. Thus it can be concluded that n-octane is expelled from the adsorbed phase by polar methanol and/or water molecules.

Figure 4 collects the results of MD simulation for water nanodroplet sitting on the considered CP surface. One can observe that the complete wetting occurs, and the resulting water contact angle is equal to zero. It means, that the studied CP surface is strongly hydrophilic, and completely wetted by water at the room temperature. However, more interesting are the results showing the behavior of water nanodroplet on the studied CP surface covered by an n-alkane monolayer. Collected in Fig. 5 results for n-decane show that the equilibrated hydrocarbon monolayer (see Fig. 5 for t = 0.5 ns) is completely expelled by water molecules forming the nanodroplet (see Fig. 5 for t = 2.5, 5 and 10.5 ns). The same situation is observed for other n-alkane molecules (see Figure S4 in the Electronic Supplementary Material), leading to conclusion about the self-cleaning properties of the studied CP surface. It is interesting to note, that even C₅₅H₁₁₂ molecules (being solid at the normal conditions) are successfully expelled by the nanodroplet of water sitting on the studied CP surface (Figure S4). This indicates that the self-cleaning behaviour is robust.

Figure 6 collects the results of wetting dynamics measurements. As one can observe, macroscopic water droplet wets the dry Zn(Cys)₂ surface very fast (around 1 s) however, the wetting of Zn(Cys)₂ equilibrated with C₁₀H₂₂ vapour is around 5 times longer. This is the confirmation of the chromatography and simulation results presented above.