Davide
Ceriotti
a,
Piergiorgio
Marziani
a,
Federico Maria
Scesa
a,
Arianna
Collorà
a,
Claudia L.
Bianchi
bc,
Luca
Magagnin
ad and
Maurizio
Sansotera
*ad
aDipartimento di Chimica, Materiali e Ingegneria Chimica, Politecnico di Milano, via Mancinelli 7, 20131 Milano, Italy
bDipartimento di Chimica, Università degli Studi di Milano, via Golgi 19, I-20133 Milano, Italy
cConsorzio Interuniversitario Nazionale per la Scienza e Tecnologia dei Materiali (UdR – UniMi), via G. Giusti, 9, 50121 Firenze, Italy
dConsorzio Interuniversitario Nazionale per la Scienza e Tecnologia dei Materiali (UdR– PoliMi), via G. Giusti, 9, 50121 Firenze, Italy. E-mail: maurizio.sansotera@polimi.it; Fax: +39 2 2399 3280; Tel: +39 2 2399 4770
First published on 28th August 2024
A solvent-free mechanochemical synthesis of two fluorinated perovskites, KCuF3 and KNiF3, including the optimization of milling time at constant rotational speed, was studied as a practical and green alternative to the classical solvothermal synthesis. The presence of KCuF3 and KNiF3 in the desired crystalline phase as the main product was observed after 6 h of milling. At higher milling times K2CuF4 and K2NiF4 were detected as additional crystalline phases for the Cu- and Ni- based perovskites, respectively. The fluorinated perovskites were characterized by using X-Ray Powder Diffraction (XRD), X-Ray Photoelectron Spectroscopy (XPS) and Scanning Electron Microscopy (SEM), confirming the selective formation of the fluorinated perovskites. The mechanochemical route was also compared to a new mild solvothermal method. An evaluation of the environmental impact and the energy efficiency was performed; moreover, the effectiveness of the mechanochemical process was compared to that of the solvothermal method. The promising results obtained from this innovative method opened the door to the use of solvent-free mechanochemical syntheses as a suitable approach in the field of crystal engineering also.
The physical and electrical properties of fluorinated perovskites are largely dependent on their synthesis because it significantly affects their dimension and shape; thus, several methods were developed: the conventional solid state reaction at high temperature,18 hydrothermal processes,19,20 and microemulsion-based methods.21 Mechanochemical synthesis of perovskites has emerged in recent years as a viable alternative to traditional chemical syntheses, spanning applications from organic–inorganic hybrid materials to fully inorganic perovskite-type electro-ceramics.22 This method has rapidly gained recognition as an environmentally friendly route for chemical modification in materials science, particularly in electronics, optoelectronics,23 and electrochemical fields.24,25 Utilizing mechanical forces in a one-step process,26 typically through high-energy ball milling, this approach facilitates reactions without hazardous, expensive, or polluting solvents. It offers a sustainable alternative to high-temperature, solution-based synthesis, and the potential of this technique is demonstrated in tailoring the properties of final products by manipulating reaction conditions such as milling energy, reaction time, stoichiometry, or additive insertion.27,28
In this work, the mechanochemical syntheses of KNiF3 and KCuF3 were described and compared to a mild solvothermal synthesis performed at mild temperature in a relatively fast process. A planetary instrument was employed for the mechanochemical reactions: in a planetary ball mill, the collisions between the milling media and the treated materials were generated by the simultaneous rotation of the base plate and the jar; these impacts were responsible for producing the necessary kinetic energy for the reaction, allowing the conversion of the starting materials.29 The yield of the reaction was strictly dependent on the selected milling parameters, which included the rotational speed, media filling ratio, powder filling ratio and milling time. The first three parameters directly influenced the kinetic energy of the spheres, modifying their speed, directly in the case of the rotational speed, or indirectly in the case of media filling ratio and powder filling ratio influencing the free space available inside the jar that the spheres required to gain velocity and, thus, kinetic energy, before the impact. The milling time enhanced the probability that the kinetic energy released by the impacts was exploited for the reaction rather than being dissipated as heat or against the walls of the jar. The parameters employed in the mechanochemical syntheses were discussed and the properties of the perovskites, such as their crystalline phases, compositions, and morphologies, were also reported.
This work also evaluates whether the mechanochemical process is actually more environmentally friendly than the solvothermal process from both a chemical and energetic point of view. Some green metrics commonly used in these cases were examined:30 the theoretical atom economy of the process (AE) and the theoretical process mass intensity (PMI).
The atom economy evaluates a synthetic process a priori and it reveals a low environmental impact when the maximum number of reactant atoms are found in the products. Therefore, the fewer by-products created in a process, the more efficient it is. Process mass intensity is defined as the total mass (including reagents, solvents, catalysts, etc.), expressed in grams, of raw materials used to synthesize 1 gram of the product. It is a parameter that must be determined a priori, similar to the atom economy. When comparing two processes, a lower PMI value usually indicates a lower environmental impact.31
These metrics emphasise the importance of avoiding the use of unnecessary solvents, or the huge amounts of waste produced in some syntheses. When designing a mechanochemical process, these parameters must be taken into account in order to achieve the desired result with the least possible waste of resources.
Furthermore, the energy consumption required for perovskite synthesis by mechanochemical and solvothermal methods was evaluated, using as a reference the maximum theoretical quantity that can be synthesized with the corresponding equipment. In this way, it is possible to observe whether the use of mechanical energy can be a valid alternative to thermal energy also from an energy point of view, as it has been demonstrated in numerous studies for other chemical syntheses.32
The actual yields of the reactions were not considered for these evaluations as they depend on the optimization of the process, which, in the solvothermal case, was not performed.
In the literature, optimal values are reported between 0.3 and 0.5 for the media filling ratio and between 0.5 and 1.0 for the powder filling ratio.34
The visual representation of the media filling ratio and powder filling ratio is shown in Fig. 1.33
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Fig. 1 Graphical representation of the media filling ratio (on the left) and the powder filling ratio (on the right). |
Every sample was synthetized in a 50 mL zirconia jar with a defined number of zirconia grinding balls: 39 balls of 8 mm diameter. An equimolar amount of KF and CuF2 or NiF2 were weighted according to Table 1 and placed inside the zirconia jar.
Sample | KF | CuF2 | NiF2 |
---|---|---|---|
KCuF3 | 0.730 g (12.5 mmol) | 1.27 g (12.5 mmol) | — |
KNiF3 | 0.750 g (12.9 mmol) | — | 1.25 g (12.9 mmol) |
The two-steps milling procedure included 15 minutes clockwise and 15 minutes anti-clockwise rotation with 1 minute of resting time between the two steps. The rest was performed in order to avoid temperature increases that can affect the results and could potentially damage the instrument. Three different grinding times were defined: 3 h, 6 h and 12 h (including the rest).
The solvothermal method was performed for both KNiF3 and KCuF3, following the same procedure: KF was dissolved in a minimal amount of distilled water (4/5 mL) while nickel or copper chloride were dissolved in 40 mL of ethanol according to the data present in Table 2. The two solutions were then mixed together in a Teflon® reactor and placed inside a stainless steel (AISI 316) autoclave. The reaction was performed at 185 °C for 16 h. At the end of the thermal step, the resulting precipitate was filtered and washed first with pure ethanol and then with a mixture 80/20 (v/v) of ethanol and water three times. The final product was dried under vacuum at 90 °C for 12 h.
Sample | KF | CuCl2 | NiCl2·6H2O |
---|---|---|---|
KCuF3 | 0.261 g (4.5 mmol) | 0.201 g (1.5 mmol) | — |
KNiF3 | 0.174 g (3.0 mmol) | — | 0.236 g (1.0 mmol) |
Scanning Electron Microscopy (SEM) and quantitative Energy Dispersive X-ray Spectroscopy (EDS) were also performed to evaluate the shape and the morphology of the particles and the possible content of other chemical species as impurities.
X-Ray Photoelectron Spectroscopy (XPS) was performed to confirm the XRD results. XPS was conducted using an M-probe apparatus (Surface Science Instruments). The source was a monochromatic Al Kα radiation (1486.6 eV). A spot size of 200 × 750 μm and a pass energy of 25 V were used. Fits were performed using pure Gaussian peaks and Shirley's baseline, without any constraints. Survey and high-resolution spectra have been obtained to determine the compositions of the samples and the oxidation states of the elements. By fitting the C 1s signal, the main peak has been shifted in order to set the adventitious carbon peak at 284.6 eV. C 1s, Ni 2p, O 1s, F 1s and K 2p has been recorded for KNiF3 and C 1s, Cu 2p, O 1s, F 1s and K 2p for KCuF3. The peaks in high resolution XPS spectra were assigned according to literature data on fluorinated perovskites.15,22,24 XPS errors on the measurements were evaluated considering the atomic scaling factors (ASFs) of the elements detected.
After 12 hours of milling, the occurrence of K2MF4 side crystals as a product of subsequent KF addition to the perovskite structure was observed. Indeed, as the reaction time increases, the mechanochemical forces generated by the interactions between the milling media and the treated materials result in the build-up of more intense mechanical stresses; these higher mechanical stresses promote reactions that may not occur under conventional synthesis conditions. This phenomenon applied to the milling conditions employed lead to the minor formation of K2CuF4 and K2NiF4,36 as additional crystalline species.
The solvothermal method was performed at high temperatures (i.e., 185 °C) with ethanol in an autoclave, by following a different reaction pathway that included the production of KCl as a by-product:
The perovskites were easily separated from KCl with a final filtration step, exploiting their low solubility in water and ethanol.
In the mechanochemical syntheses of KNiF3 (Fig. 3), the precursors of the perovskite successfully reacted because the crystalline phases of KF or NiF2 were not detected in the XRD pattern of the products, although their presence as an amorphous phase cannot be excluded. The synthesis of KNiF3 was confirmed in accordance with the XRD standard card of KNiF3 (JCPDS: 21-1002), and the peaks associated with the cubic crystalline phase of KNiF3 were clearly visible.12 In the samples of KNiF3 produced by mechanochemical syntheses, an additional crystalline phase ascribable to the presence of K2NiF4 was observed: these peaks were almost negligible after 3 h, but they became more relevant by increasing the milling time to 6 h and to 12 h.
The quantification of the different crystalline phases obtained by the Rietveld refinement is presented in Table 3 and 4. The original XRD patterns with the quantification of each peak are shown in the ESI.†
Phase | Solvothermal | Milling 3 h | Milling 6 h | Milling 12 h |
---|---|---|---|---|
KCuF3 | 100% | 98.5% | 100% | 80% |
K2CuF4 | — | — | — | 20% |
CuF2 | — | 1.5% | — | — |
Phase | Solvothermal | Milling 3 h | Milling 6 h | Milling 12 h |
---|---|---|---|---|
KNiF3 | 100% | 84% | 70% | 65% |
K2NiF4 | — | 16% | 30% | 35% |
In the case of KCuF3 perovskites, after 6 h of milling a quantitative formation of the product without side-products was observed. In the case of the Ni-based samples, at 3 h of milling the highest production of KNiF3 was observed and at longer times the formation of a greater quantity of the K2NiF4 phase was detected. For both the perovskites it was confirmed that the higher the milling time, the higher the content of K2CuF4 and K2NiF4, respectively. The examination of the crystallite diameters with the Scherrer equation revealed a decrease, albeit minimal, in the average size of the crystallites as the milling hours increased (Table 5).
Sample | Solvothermal | 3 h milling | 6 h milling | 12 h milling |
---|---|---|---|---|
KCuF3 | 37 | 29 | 28 | 25 |
KNiF3 | 17 | 15 | 14 | 12 |
Sample | Potassium at% | Copper at% | Fluorine at% |
---|---|---|---|
6 h milling | 22.0 (±0.3) | 22.0 (±1.1) | 56.0 (±0.6) |
12 h milling | 23.8 (±0.3) | 15.6 (±0.7) | 60.6 (±0.6) |
Solvothermal | 20.7 (±0.3) | 13.0 (±0.6) | 64.3 (±0.7) |
In potassium high-resolution spectra, the KCuF3 2p3/2 peak was detected at 293.5 eV and 293.7 eV in the samples milled for 6 h and 12 h, respectively. These signals were in agreement with the 293.6 eV peak of the solvothermal synthesis, in which KCl formation in little amounts can be noticed due to the peak at 295.9 eV.38,39 The peak at 294.1 eV was assigned to the 2p3/2 signal of residual KF in the sample milled for 6 h.38,40 After 12 h of milling, the formation of a crystalline phase due to K2CuF4 was detected by XRD measurement and the XPS signal at 294.5 eV can be ascribed to the presence of this compound. The high resolution spectra in the Cu region showed trends which were in agreement with the deconvolutions observed for potassium signals: after 6 h of mechanochemical synthesis two Cu 2p3/2 peaks were evident at 933.9 eV and 937.2 eV and they can be assigned to KCuF3 and CuF2, respectively;41 after 12 h, KCuF3 was observed in a similar range at 933.4 eV and a signal due to K2CuF4 was observed at 939.4 eV; in the solvothermal sample the perovskite peak was at 934.0 eV and the formation of a small amount of CuF2 was confirmed by the appearance of a peak at 937.4 eV.41 The high resolution analyses in the F 1s region confirmed the presence of the chemical species detected in the other spectra: after 6 h of mechanochemical synthesis three bonds of a different nature were observed at 683.4 eV, 684.6 eV and 686.2 eV, and they were ascribable to KF, CuF2 and KCuF3, respectively;41 after 12 h, CuF2 reacted quantitatively with KF, the partial formation for K2CuF4 was detected and, therefore, only the signals at 686.2 eV of KCuF3 and at 684.1 eV due to K2CuF4 were observed;41 in the solvothermal synthesis, the peak at 686.2 eV due to KCuF3 was clearly present.
In KNiF3 samples, the contents of K, F and Ni atoms were measured by XPS survey analyses and they were mainly in agreement with the theoretical composition of a Ni-based perovskite (Table 7): F contents were 56%, 57% and 60% after 6 h and 12 h of the milling procedure and in the solvothermal sample, respectively, and, therefore, these quantities were approximately in agreement with the expected values; K contents were 26%, 29% and 20%, respectively, and it should be noticed that the mechanochemical procedures induced potassium contents slightly higher that what is theoretically expected; Ni contents were complementary to the other data and, thus, the nickel amount in the sample obtained by 12 h milling decreased to 14% while it was around 18% for both the 6 h milling and the solvothermal samples. These differences from the theoretical values can be explained by the presence of K2NiF4, especially after 12 h of the milling procedure. The chlorine content in the solvothermal sample was due to a little amount of KCl that was undissolved by the washing procedure.
Sample | Potassium at% | Nickel at% | Fluorine at% | Chlorine at% |
---|---|---|---|---|
6 h milling | 25.5 (±0.3) | 18.3 (±0.7) | 56.2 (±0.6) | — |
12 h milling | 28.8 (±0.4) | 14.1 (±0.5) | 57.1 (±0.6) | — |
Solvothermal | 19.8 (±0.3) | 18.4 (±0.7) | 59.6 (±0.6) | 2.2 (±0.02) |
The deconvolutions of the K 2p, Ni 2p and F 1s high resolution XPS spectra are shown in Fig. 5 and they confirmed the formation of KNiF3, showing slight amounts of by-products. The K 2p spectrum of the sample synthetized by 6 h milling showed a broad peak centered at 293.0 eV with a shoulder signal at around 295.9 eV which can be attributed to the KNiF3, in particular to a 2p3/2 and 2p1/2 doublet due to the spin-orbit coupling typical for K.42 The binding energy split of these two signals resulted in agreement with the typical energy difference of K of around 2.8 eV.41 In the literature, K signals of KF were reported in the range from 292.1 to 293.2 eV and these were in agreement with the peaks observed in the experimental spectra, confirming the presence of little amounts of KF in all the samples.40,43 Indeed, the peaks related to the perovskite were accompanied by a doublet at 293.2 and 296.0 eV coming from KF excess coming from the unconverted reagents. A similar K 2p spectrum was recorded for the solvothermal sample with the main peaks of KNiF3 at 293.5 (2p3/2) and 296.4 eV (2p1/2) and side peaks of KF at 292.3 (2p3/2) and 295.1 eV (2p1/2). In the XPS high resolution spectrum recorded for the sample synthesized by the 12 h mechanochemical process, in addition to the doublets of KNiF3 at 293.5 (2p3/2) and 296.4 eV (2p1/2) and of KF at 292.1 eV (2p3/2) and 294.8 eV (2p1/2), another compound was detected: similar to what was observed in the copper-based perovskite, during the 12 h milling process a different perovskite characterized by the formula K2NiF4 was formed, as shown by the XRD data, and its doublet in the K 2p region can be ascribed to the contributions of the deconvolution detectable at 294.1 (2p3/2) and 297.0 eV (2p1/2). The binding energies of Ni 2p3/2 related to the KNiF3 perovskite for all three analyzed samples were recorded at 858.1 ± 0.1 eV, corroborating the assignment of this peak to the perovskite product. Moreover, for the mechanochemical synthesis, an evident effect of milling time on the extent of reaction was observed: after 6 h, a slight amount of unreacted NiF2 was still present and its signal at 860.4 eV was present together with that of the perovskite product; after 12 h, K2NiF4 started to be formed in addition to KNiF3 and its signal was observable at 854.8 eV. In the sample produced by the solvothermal approach a peak at 856.1 eV was due to the excess of NiCl used as a reagent in the synthesis. In the F 1s high resolution spectra, sharp peaks ascribable to KNiF3 were observed at 686.7 eV (±0.3 eV) in the 6 h and 12 milled samples as well as in the solvothermal sample, in agreement with the data reported in the literature.11,42 The presence of other species, in addition to the perovskite product, detected by the analyses of the K 2p and Ni 2p signals, was also confirmed in the F 1s high resolution spectra. In particular, after 6 h two additional peaks due to an excess of KF and NiF2 as reagents were recorded at 683.7 eV and 685.2 eV, respectively. After 12 h it was also possible to notice both the presence of KF excess because of its signal at 683.3 eV and the formation of K2NiF4 due to its peak at 687.5 eV. In the F 1s spectrum of the solvothermal product, the KNiF3 perovskite was the predominantly present species (around 80%) and the residual deconvoluted peak at 683.9 eV can be attributed to KF.
![]() | ||
Fig. 7 SEM images of KCuF3 perovskite obtained by mechanochemical solid-state synthesis after 6 h of milling time (A) as well as by solvothermal method (B). |
Process | Milling time (h) | AE (%) | PMI (—) | ED (MJ g−1) |
---|---|---|---|---|
Mechanochemical | 3 | 100% | 1 | 0.58 |
6 | 100% | 1 | 1.16 | |
8 | 100% | 1 | 2.32 | |
Solvothermal | — | 51.7% | 191 | 6.1 |
Process | Milling time (h) | AE (%) | PMI (—) | ED (MJ g−1) |
---|---|---|---|---|
Mechanochemical | 3 | 100% | 1 | 0.58 |
6 | 100% | 1 | 1.16 | |
8 | 100% | 1 | 2.32 | |
Solvothermal | — | 37.6% | 294 | 9.5 |
The mechanochemical approach allowed the synthesis of the perovskites starting directly from fluoride salts, avoiding the use of chemicals which, even stoichiometrically, can produce side products; indeed, all the atoms of the reagents can be transformed into products. For the aforementioned reasons, the atom economy values of the samples obtained through the mechanochemical process were 100% and the corresponding values of PMI were 1. Although this conversion can be tempered by the reaction yield, the yields of mechanochemical processes are typically comparable to or higher than that of a solvothermal processes.
The green metrics of the solvothermal process considered the wastes caused by the use of chlorides in the synthesis of fluorinated perovskites, which necessarily lead to a higher consumption of potassium fluoride and to the formation of potassium chloride as a side product. It is possible to observe that the hydration water of the nickel chloride salt further reduces the atom economy leading to a final value of 37.6% for KNiF3.
The energy demand was calculated for the mechanochemical process by considering the power of the ball miller employed and the different reaction times. The mechanochemical energy consumption was identical for both the perovskites because the optimized parameters were employed in both the syntheses and only the milling time was varied in the different samples. For the solvothermal synthesis, the heating time of the oven and the energy consumption during the synthesis and final drying step were considered.
On the basis of the energy assessment, the mechanochemical syntheses was clearly favourable from an energetic point of view because of the absence of waste of energy due to solvent heating, heat dispersion and final drying of the products. The dispersion of mechanical energy is therefore less impactful, especially for laboratory scale production. Overall, the mechanochemical process showed a clear advantage over the solvothermal process in the assessment of all the green metrics examined. All the details of the calculations are presented in the ESI.†
The absence of significant by-products and the ease of the mechanochemical process demonstrated that this kind of synthesis can be considered a valid alternative to the classic solvent-based approach. Thus, the described process can be extended to the synthesis of other fluorinated perovskites.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4mr00037d |
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