Regarding the characterization of the materials, optical microscopy is used to observe droplet size distributions of emulsions. Nitrogen adsorption–desorption (BET) measurements provide specific surface area data. X-ray diffraction (XRD) assesses the crystallinity of MIL-96(Al) after incorporation into the polymer matrix. Infrared spectroscopy confirms the retention of functional groups. Mechanical properties are evaluated by applying increasing loads to monoliths until deformation is observed. Hydrodynamic properties are assessed through Darcy flow experiments, measuring pressure drop as a function of flow rate.
The obtained MOF material from battery waste dissolution is based on Aluminum from the contactors of the batteries. Even in the presence of various metals after battery dissolution, selective precipitation (MIL-96(Al)) is obtained by adding the precipitating agent to the solution.
Pickering emulsion is a type of emulsion stabilized by solid particles adsorbed at liquid–liquid interfaces. In this case, MOF particles, thanks to their amphiphilic nature and interfacial activity, can efficiently adsorb at oil–water interfaces and form stable water-in-oil (W/O) or oil-in-water (O/W) emulsions.
The emulsions are formulated by first dispersing MIL-96(Al) particles in an aqueous phase of ultrapure water. The amount of MOF dissolved in the solution heavily depends on the volume of the liquid phases used in the emulsion. The amount of MOF used for the Pickering Emulsion is specifically given in %w, which is defined as the ratio of the total mass of MOF and the total mass of liquid used in the emulsion. The amount of MOF (WMOF) is thus defined by the following formula:

where:
Voil = volume of the organic phase (paraffin)
Vwater = volume of aqueous phase
ρoil = density of the organic phase (paraffin)
ρwater = density of aqueous phase
mMOF = masse of MIL-96(Al)
Originally, 375 mg of MIL-96(Al) was used for the preparation of the polyHIPE. Subsequent experiments show that scalability is possible. The amount of MOF added can be increased 10-fold and still produce stable monoliths.
Pickering emulsions formed with MIL-96(Al) display characteristics consistent with previous observations. They produced stable Oil/Water emulsions where droplets are densely packed due to the high internal phase fraction. In formulations containing PVA and polymer precursors, droplet sizes are substantially reduced, with average diameters near 20 µm compared to 55–75 µm for simpler emulsions lacking PVA (Figure 1).
This reduction is attributed to the increased viscosity of the aqueous phase and the adsorption of PVA at the oil–water interface. Rheological measurements reveal pseudoplastic behavior across all samples. The presence of polymer precursors increases viscosity and introduces a higher yield stress, consistent with the formation of a dense droplet network18. These rheological signatures indicate that emulsions behave as gels and would retain their structure during polymerization. Increasing PVA concentration from 0–0.5 wt.% results in smaller pores but greater pore interconnectivity. Pore sizes decrease by a factor of 5 across this range, while window density increases significantly19. The concentration of MOF particles had minimal effect on pore size but influenced the deposition of MOFs at pore surfaces. Higher MOF content results in more MOF particles becoming embedded in the polyacrylamide walls or exposed at the surface, thereby affecting the composite’s specific surface area (Figure 2).
Surface area values range from low m2.g-1 for materials lacking PVA to higher m2.g-1 for samples containing 0.5 wt.% PVA. Increasing the amount of PVA enhances network openness, improving access to MOF surfaces. However, incorporation into a polymer matrix inherently reduces microporosity compared to the pristine MOF (650 m2.g-1). Losses of 74%–94% are observed depending on formulation. These results are consistent with the literature, where shaping MOFs into monoliths commonly yields substantial surface losses due to occlusion within polymeric frameworks20.
XRD diffractograms retain the characteristic peaks of MIL-96(Al), demonstrating that neither emulsification nor polymerization compromises framework integrity. Lower-intensity peaks for low-MOF-content samples are attributed to the reduced MOF accessibility rather than structural degradation. FTIR spectra confirm the presence of MIL-96 functional groups, especially carboxylate stretches indicative of intact metal–ligand coordination.
Hydrodynamic behavior is strongly influenced by PVA content. Darcy flow experiments demonstrate that pressure drop increases with flow rate for all samples, consistent with tortuous pore geometries21,22. The monolith lacking PVA exhibits significantly higher pressure drops due to poor interconnectivity.
In contrast, PVA-containing monoliths display a plateau in pressure drop at low flow rates, indicating unobstructed flow through interconnected pores23. A critical Darcy velocity is identified for each formulation, marking the transition between low-pressure and pressure-increasing regimes24. Higher PVA content correlates with higher critical velocities due to enhanced pore openness (Figure 3).
Another strategy to make the accessibility of MOFs more efficient during the process of shaping is also presented. This research proposes a novel method based on stabilizing a paraffin-in-water Pickering emulsion using a fluorinated Zr MOF combined with the polyHIPEs strategy. After polymerization and paraffin removal, a hierarchically structured monolith is obtained with the MOF particles typically embedded in the polymer wall, potentially blocking pores. The key innovation to prevent this pore blocking is modifying the MOFs' hydrophilic/hydrophobic balance by controlled adsorption of hydrophobic molecules (Fluorinated molecules). This modification induces a displacement of the MOF position at the paraffin–water interface during emulsification. This results in particles being less embedded in the polymer wall. This process successfully yields hierarchically structured monoliths integrating highly accessible MOF particles suitable for fixed-bed processes (Figure 4).

Figure 1: Images and optical microscopic images of different Pickering emulsions. (A) Pickering emulsions with 2.5wt.% MIL-96(Al) and different paraffin volume ratios: from left to right, φv = 0.5, 0.6, 0.7, and 0.8. (B) Pickering emulsions with φv = 0.8 and different concentrations of MIL-96(Al): from left to right, wMOF = 1, 2, 3.5, and 5wt.%. Optical micrographs of emulsions with 5wt.% MIL-96(Al) and paraffin volume ratios of (C) 0.5, (D) 0.6, (E) 0.7, and (F) 0.8. This figure is reproduced with permission from Lorignon et al.17. Please click here to view a larger version of this figure.

Figure 2: Nitrogen isotherm adsorption/desorption of the corresponding MIL-96(Al) powder, M100/10/0.5, M100/10/0 and M25/10/0.5. This figure is reproduced with permission from Lorignon et al.15. Please click here to view a larger version of this figure.

Figure 3: Photograph of the M100/10/0.5 monolith seen from the front and from below. (A) and SEM images of the M100/10/0.5 monolith at different magnifications (B–E). This figure is reproduced with permission from Lorignon et al.15. Please click here to view a larger version of this figure.

Figure 4: Strategy to make MOFs particles more accessible after the shaping process. This figure is reproduced with permission from Lorignon et al.18. Please click here to view a larger version of this figure.