Open Access Article
Felipe H.
dos Santos
ab,
Pavlo
Ivanchenko
a,
Roger
Borges
c,
Cauê R.
de Oliveira
c,
Marcos Y.
Kamogawa
d,
Marcelo E.
Alves
*bd and
Deb P.
Jaisi
*a
aInterdisciplinary Science and Engineering Laboratory, University of Delaware, Newark, DE 19716, USA. E-mail: jaisi@udel.edu; Fax: +1 302 831 0605; Tel: +1 302 831 1376
bDepartment of Soil Science, Luiz de Queiroz College of Agriculture, University of São Paulo, Piracicaba, SP 13418-900, Brazil. E-mail: mealves.esalq@usp.br; Tel: +55 19 3429 4189
cNanotechnology National Laboratory for Agriculture, Brazilian Agricultural Research Corporation, São Carlos, SP 13560 970, Brazil
dDepartment of Exact Sciences, Luiz de Queiroz College of Agriculture, University of São Paulo, Piracicaba, SP 13418-900, Brazil
First published on 30th September 2025
Calcium phosphate nanoparticles have been increasingly propounded as an efficient phosphorus (P) fertilizer in crop production. In this study, we used sustainable sourcing of calcium phosphates by recycling bovine bones and modifying the extracted hydroxyapatite using three approaches: calcination and mechano-activation, alkaline hydrolysis, and subcritical water extraction. Hydroxyapatites derived from these treatments were analyzed for ultrastructure, particle size distribution and crystal chemistry to interpret the dissolution characteristics under a flow-through nanofiltration system. While calcination was the most effective treatment for removing organic molecules—with only 0.22 wt% of total organic carbon and 0.03 wt% nitrogen remaining on hydroxyapatite—it led to the largest growth in crystallite size (113–139 nm) compared to hydroxyapatites treated through alkaline hydrolysis (45–93 nm) or subcritical water (33–78 nm). Surprisingly, the mechano-activated hydroxyapatite following the calcination exhibited a sustained and high P release profile, driven by the presence of ultrafine (10–35 nm) amorphous particles mixed with well-ordered and structurally defective apatitic structures. Hydroxyapatites recovered by alkaline hydrolysis and subcritical water treatments exhibited slow and steady P release profiles reflecting fewer structural and surface imperfections compared to mechano-activated hydroxyapatite. These findings demonstrate that processing-induced ultrastructural and compositional changes in bone-derived hydroxyapatite exert a major role in P-release characteristics. Consequently, these products could be tuned for both sufficiency and efficiency of P fertilization, thus generating sustainably sourced nano P fertilizer for crop production.
Environmental significanceConventional phosphorus (P) fertilizers derived from limited geological reserves are excessively soluble and contribute to environmental issues such as eutrophication of water sources, algae blooms and hypoxia. Hydroxyapatite nanoparticles are a promising source for slow-P release, but are commonly synthesized from high-purity P sources. This study presents sustainable alternatives for sourcing hydroxyapatite from bovine bones, tuned for controlled P release through the processing parameters to address dual challenges in agriculture: sufficiency and efficiency. The structure–function relationships presented may be pivotal to the advancement of the new generation of P fertilizers. |
One significant strategy to mitigate the strain on P reserves is the development of innovative fertilizers that enhance P uptake by plants and attenuate P losses from soils.4 Conventional P fertilizers, such as triple superphosphate, mono-ammonium phosphate and diammonium phosphate, are highly water-soluble, leading to their premature dissolution that is not synchronized with the P uptake kinetics by crops. In contrast, calcium phosphate (CaP) nanoparticles with tunable properties—such as synthetic hydroxyapatite,5,6 modified hydroxyapatite,7,8 or amorphous calcium phosphate (ACP)9,10—have been explored for application as slow-release P fertilizers. However, the synthesis of CaP typically relies on high-grade P sources such as phosphoric acid or monohydrogen phosphate salts, which primarily come from finite geological reserves.11
The recovery of P from sustainable sources, particularly from bones of animals raised and slaughtered for meat12 offers a promising alternative to mitigate the pressure on geological reserves of P,13 and, more importantly, enhances the circularity in the fertilizer sector. Historically, bones have been applied as fertilizer materials for centuries, albeit with low P use efficiency.14 Conventional bone processing methods, including grinding, autoclaving, combustion, acidulation, or pyrolysis, often produce materials with subpar properties for fertilizers in terms of achieving high P recovery efficiency. In addition, these mentioned methods tend to overlook the bone structure assembly, which is essential for tuning materials for target applications. The highly hierarchical composite structure of mineralized collagen fibrils15 has been known for over three centuries and has recently been better resolved through advancement of 3D imaging.16 The bone mineral, also known as bioapatite, is a nano-sized CaP phase precipitated from animal body fluids17 that if properly isolated from the organic fraction, has the potential to serve as a slow-release P fertilizer.18
Bioapatite constitutes approximately 55–60% of bone weight, far exceeding collagenous proteins found at 30%, water at 10–15%, and the small fraction of non-collagenous proteins and lipids.17,19 Compared to stoichiometric hydroxyapatite, bioapatite is a calcium (Ca) and hydroxyl (OH−) deficient structure (P63/m), and can contain up to 7 wt% of carbonate (CO32−) and 3 wt% structural water.20 In addition, bioapatite surfaces contain amorphous layers enriched with protonated phosphates such as HPO42−,21 which contribute to their higher solubility compared to stoichiometric hydroxyapatite or fluorapatite.22 The extraction of bioapatite for application as a P fertilizer could be a promising route to address dual challenges in agriculture: providing a secondary source of P and offering a slow-release mechanism for P fertilization. Nonetheless, the choice of processing method is crucial for the preparation of bioapatite as a slow-release fertilizer, as different methods can lead to significant variations in composition, crystallinity, and particle size distributions.23
Among bone processing methods, calcination is usually the standard method for recovering bioapatite, which leads to a notable increase in P concentration compared to raw bone. However, processing temperatures exceeding 700 °C may promote significant recrystallization of bioapatite.25 To enhance the dissolution of calcinated apatite, the mechanical activation method is preferred over acidulation. This is because the conventional acidulation method generates phosphogypsum (CaSO4·2H2O) as a by-product, which poses a disposal challenge for the P fertilizer industry.26 Alternatively, hydrothermal treatment methods, such as alkaline hydrolysis, can be attractive due to lower operational costs compared to calcination and mechanical activation, while also offering higher selectivity for removing organic matter from bones.23,27 Nevertheless, alkaline hydrolysis requires the use of strong alkaline reagents, a limitation that can be bypassed by employing treatments solely involving water. For example, near critical conditions—ranging from 100 to 374 °C and 100 kPa to 22.1 MPa—induce significant alteration in the physicochemical properties of water, most notably in the dielectric constant (ε). At 25 °C, water has an ε of 78.3, which drops to 27 at 250 °C above 100 kPa, similar to the dielectric constant of organic solvents such as methanol (ε = 33), or ethanol (ε = 25). Hence, the polarity of subcritical water enables effective extraction of organic matter from bones,23 while preserving bioapatite in comparison to calcination and alkaline hydrolysis methods.
The objectives of this research are to investigate the effect of three different bone treatment methods on the composition, structure, and size of nanometric apatite, and to understand how these characteristics affect the P dissolution kinetics at a pH typical of root exudates. To the best of our knowledge, the application of apatites extracted through alkaline hydrolysis or subcritical water as fertilizers has not been previously evaluated.
The terms bone mineral, bone apatite, biological apatite (bioapatite), hydroxyapatite, and carbonated hydroxyapatite are commonly used in the scientific literature as synonyms to describe the mineral fraction of bone. The bioapatite nomenclature reflects the biological mineralization of bone minerals, in contrast to their geological or synthetic crystallization. Nonetheless, apatite is a generic term used for a group of 15 minerals, which is more strictly used to refer to a subgroup of three minerals: fluorapatite, chlorapatite, and hydroxyapatite.24 An amorphous surface layer and a highly disordered apatitic core, both differing from stoichiometric hydroxyapatite, make it difficult to apply more specific, appropriate terminology to bone minerals, particularly given that the properties of non-processed minerals differ substantially from those of the processed materials. Therefore, we have used the generic term bioapatite to refer to the non-processed CaP phase present in bone, whereas hydroxyapatite (HA) is hereafter used collectively to refer to processed and altered CaP, despite the limitations.
:
1. The material recovered after calcination and mechano-activation is referred to as ‘HAcm’. Alternatively, hydrothermal treatments of bones were performed using deionized water or potassium hydroxide (KOH).28 Briefly, 2 g of HAut was mixed with 60 mL of either deionized water (<0.05 μS cm−1) or 0.5 mol L−1 KOH solution in Teflon containers. Teflon containers were then placed in a steel reactor under constant magnetic stirring, maintaining temperature (200 °C) and pressure (≥30 bar), for 5 h following a reported method.23 The solids were then separated from the supernatant by centrifugation at 8000 rpm, and the resulting pellets were subsequently freeze-dried. The HA isolated by the alkaline treatment is designated as “HAk” while the HA recovered using water under subcritical conditions is referred to as “HAw”.
:
1 mixture of HNO3 and HCl using EPA method 3051A in a microwave furnace (CEM, NC). The extracts were analyzed for Al, B, Ca, Cu, Fe, K, Mg, Mn, Na, P, S, and Zn by inductively coupled plasma optical emission spectroscopy (ICP-OES) using a Thermo 7600 ICAP (Thermo Elemental, WI).
Total carbon (TC) and nitrogen (N) contents were determined in duplicate using the Pregl-Dumas combustion method with an Elementar VarioMax CN Analyzer (Elementar Americas, NJ). Total organic carbon (TOC) was measured after removing inorganic carbon with 1 mol L−1 HCl.27 The total inorganic carbon (TIC) content was calculated as the difference between TC and TOC. Additionally, thermogravimetric (TGA) and differential scanning calorimetry (DSC) analyses were simultaneously conducted with an SDT Q600 analyzer (TA Instruments, DE) to estimate the CO32− content and the mass loss events during heating. For thermal analysis, the furnace was programmed to heat at a rate of 10 °C min−1 up to 160 °C, followed by a 30 min isothermal step to eliminate adsorbed water, and then continued heating at a ramp of 10 °C min−1 until reaching 1000 °C. All thermal analyses were performed under a synthetic air atmosphere at a flow rate of 50 mL min−1.
285 scans per HA sample analyzed.
The HAs were loaded into Kapton capillaries (Ø = 1.37 mm), sealed at both ends with epoxy putty, and then mounted in magnetic spinner-type sample holders (Fig. S2). Data acquisition was performed in high-throughput mode with automated spinner exchange. An X-ray beam energy of 15.99 keV, equivalent to a wavelength of 0.7749 Å was used in data collection. The data were converted to CuKα wavelength (1.5406 Å) using the following formula to enable comparison with standard powder diffraction files (PDF): λ1 sin(θ)2 = λ2 sin(θ)1, where λ1 = 0.7749 Å (conversion of 15.99 keV to wavelength), λ2 = 1.54 Å (CuKα wavelength), and sin(θ1) and sin(θ2) are the sines of the respective diffraction angles. Diffraction data were then processed using the software Match! (Crystal Impact, Bonn). The FWHM values were extracted after full-profile fitting employing the goodness-of-fit (GoF) parameter to optimize the peak profile matching. The Scherrer equation was applied to calculate coherent domain sizes (D) as follows:
, where K is a dimensionless shape factor (0.9), λ is the wavelength of CuKα radiation (1.54 Å), and β is the FWHM (radian). Separate domain size calculations were made for the D002 and D310 planes of the crystal lattice,30 instead of calculating average values. Furthermore, 10 peaks from each diffractogram were chosen to calculate D, which were then plotted using kernel density estimation (KDE) to visualize their probability distribution.
The interplanar distance (d-spacing) of the HA particles was calculated from analysing HRTEM micrographs using ImageJ software (National Institutes of Health, USA), in which pixel counting in the software was calibrated according to the known distances in nm. Image areas with no visible superposition of particles or lattice planes were selected for fast Fourier transform (FFT) analysis. Selected reflections were filtered, and inverse FFT was applied to convert back into the spatial domain, isolating the lattice fringes. The d-spacing was then calculated using the average distance between 10 or more visible fringes. The TEM-based lattice data were compared to those derived from d-spacing in the X-ray diffraction data.
Triplicates of 50 mg HA powder were first dispersed in 1 mL of ethanol using 1.5 mL vials sealed at the edges with a sealing film, agitated on a vortex mixer, and then kept in a sonication water bath for approximately 150 min. Thereafter, each HA sample was homogeneously deposited onto a 10 kDa membrane disc (equivalent to a pore size of 5–6 nm). A second 10 kDa membrane filter was placed above the sample to prevent direct contact of the inflowing solution with the HA and to maintain the uniformity of the deposited layer. This assembly was then placed inside a 10 mL ultra-filtration cell (Fig. S3), and 2 mL of citrate buffer was added on top. In the sequence, an effective residual pressure of 50 psi was applied to the macro-dialysis cell, ensuring a flow rate of 50 μL s−1 of the extractant through the membrane. Eluted solutions (extracts) from the HA powder were collected every 5 s in separate vials over 80 s, yielding approximately 250 μL of extract per vial. The concentration of dissolved P in each eluate was determined using the phosphomolybdate blue method at a wavelength of 881 nm (ref. 31) using a Cary 5000 UV-vis spectrophotometer (Agilent Technologies, CA).
| Treatment | TC (%) | TOC (%) | N (%) |
|---|---|---|---|
| HAut | 12.58 ± 0.01 | 11.59 ± 0.1 | 3.07 ± 0.03 |
| HAc | 0.37 ± 0.01 | 0.22 ± 0.04 | 0.03 ± 0.01 |
| HAcm | 0.56 ± 0.05 | 0.32 ± 0.01 | 0.04 ± 0.01 |
| HAk | 1.19 ± 0.07 | 0.53 ± 0.02 | 0.02 ± 0.01 |
| HAw | 5.45 ± 0.39 | 3.79 ± 0.11 | 0.19 ± 0.01 |
The small amounts of TC and TOC detected in HAc in elemental analyses are consistent with the findings from TGA analysis. Note that TGA was primarily employed for estimating the carbonate content and thus indirectly assessing the organic C content (Fig. 2A). The least mass lost observed under oxidizing conditions at the temperature range of 250–600 °C occurred in HAc, with progressively higher mass losses recorded for HAcm, HAk, HAw, and HAut (Fig. 2A; Table S1). The first derivative of TGA in the range of 200–1000 °C revealed distinct regions of mass loss events related to the collagen and non-collageneous protein degradation, which starts at 327 °C and goes until around 450 °C. This interpretation is reinforced by the exothermic peaks at 338 °C and 445 °C in HAut (Fig. 2C) and by the observation of CO2, N2O, and NH3 released in this temperature range in a previous study on bovine bone calcination.25 The loss of structural water known to occur from 250–550 °C could not be spotted as in pristine HA20 due to the presence of organic matter, while the loss of CO32− in the 600–900 °C range appear overlapping the dehydroxylation and transformation of HA to β-tricalcium phosphate occurring from 700–1000 °C. Notably, both the mass loss events related to organic molecules and those associated with mineral transformations occurred at lower temperatures for HAut compared to HAw. Although HAut has a higher organic content than HAw, its molecular composition is likely different, as indicated by the previously discussed C/N ratio. Moreover, autoclaving of HAut probably denatured and fragmented proteins, decreasing their thermal stability, while in HAw the residual organic compounds may have become more condensed and associated with the HA.
The organic residues in HA were qualitatively assessed using FTIR. The spectral range of 1650–1300 cm−1 in the FTIR spectra, which typically exhibits the ν3CO3 vibrational mode in HA, was overlapped by amide I (1650–1680 cm−1) and amide II (1540–1550 cm−1) bands in HAut (Fig. 3). The high intensity of HAut bands in the 1650–1300 cm−1 region relative to other treatments confirms the higher content of collagen and organic carbon in this material compared to other HA samples. In contrast, the intensities of amide I and II bands were significantly diminished in HAk and completely disappeared in HAc.
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| Fig. 3 FTIR-ATR spectra in the 4000–400 cm−1 mid-infrared region of hydroxyapatites recovered from bovine bones. | ||
Notably, the intensities of amide bands, characterized predominantly by the C
O stretching band for amide I, and N–H bending for amide II, as well as C–H stretching bands (around 3000 cm−1), revealed a higher intensity in HAw compared to both HAc and HAk. This observation is coherent with the results derived from TOC and TGA analysis. Interestingly, the C–H bands, which are of low intensity in HAc, disappear completely in the HAcm, likely due to transient temperatures reaching as high as 400–500 °C in localized microregions during ball collisions,32 which may have contributed to the further volatilization of organic molecules.
In contrast to the TOC content, the highest content of TIC was found in HAw (1.67 wt%), followed by progressively lower contents in HAut (0.99 wt%), HAk (0.67 wt%), HAcm (0.24 wt%), and HAc (0.15 wt%). The higher TIC content in HAw than that in HAut indicates the incorporation of CO32− during the subcritical water extraction process. Similarly, the CO32− incorporation may have also occurred during the mechanochemical activation of HAc, as indicated by the higher TIC content in HAcm compared to HAc (Table S1). The higher CO32− content in the HA structure correlates with the smaller crystal size and a lower degree of crystallinity,33 which are evidenced in HAw and HAut materials (see the hydroxyapatite structure).
The TGA results corroborated the estimated TIC values calculated from elemental analysis. However, it is noteworthy that the content of CO32− obtained from TGA was universally higher than the corresponding TIC estimations (Table S1). This discrepancy can be attributed to the intrinsic limitation inherent to the TGA methodology, wherein multiple overlapping mass loss events occur within a narrow or the same thermal range. Moreover, it is important to note that TIC and TGA results reflect calculated inorganic carbon values, facilitating the assessment of relative content among various HAs but should not be misconstrued as direct measurements. Nevertheless, the inorganic carbon estimations are significant to demonstrate, along with the crystallite size (see the hydroxyapatite structure section), that the most efficient treatments for removing TOC and N were those that imparted the more substantial modifications to HA properties.
A positive correlation was observed between the efficiency of organic removal during treatment and P content in the resultant HA (Table 2). Surprisingly, HAc was 1.5% richer in P than the HAcm, despite both materials being derived from HAut. This deviation might be partially attributed to the structural incorporation of CO32−, as evidenced from TIC and TGA results, as well as the erosion of mill balls, which led to a higher Fe and Al content in HAcm compared to HAc (Table S1). The higher P content observed in HAk than that in HAw cannot be attributed to experimental artifacts but rather reflects the efficiency of alkaline hydrolysis in organic matter removal, as evidenced by a 3.6% difference in TOC between the two materials (Table 1) and a 5.4% difference in mass loss in the TGA results (Table S2). Overall, the average P content in potential innovative slow-release nanofertilizers (HAcm, HAk, HAw) was 16%, which lies between commercial acidulated P fertilizers such as single superphosphate (7–9% P) and triple superphosphate (20% P), and lower than NP fertilizers like monoammonium phosphate (23% P) and diammonium phosphate (20% P).
| Treatment | Ca | P | Mg | Na | K | CCa/P ratio |
|---|---|---|---|---|---|---|
| g kg −1 | ||||||
| HAut | 263.51 ± 2.06 | 121.20 ± 0.19 | 4.49 ± 0.06 | 5.82 ± 0.03 | n.d. | 1.68 |
| HAc | 374.04 ± 0.82 | 171.33 ± 0.17 | 6.54 ± 0.01 | 8.62 ± 0.02 | 0.35 ± 0.03 | 1.69 |
| HAcm | 349.80 ± 0.47 | 156.29 ± 0.16 | 6.72 ± 0.01 | 8.26 ± 0.04 | 0.94 ± 0.03 | 1.73 |
| HAk | 366.62 ± 0.07 | 165.38 ± 0.48 | 6.58 ± 0.03 | 3.01 ± 0.02 | 0.92 ± 0.01 | 1.71 |
| HAw | 345.61 ± 2.12 | 157.94 ± 0.32 | 5.48 ± 0.04 | 3.47 ± 0.02 | n.d. | 1.69 |
The trace element content of bioapatite varied among treatments. For instance, the K+ content in HAcm was minimal and comparable to KOH treatment, suggesting that the alkaline treatment did not significantly facilitate the incorporation of K+ into the HAk structure. A trace amount of Zn2+was found in all treatments, which is presumed to be partial substitution of Ca II sites in seven-fold coordination. The Ca II site—with a Ca2+ ionic radius of 1.07 Å—is more exposed and accessible to accommodate ions with ionic radii between 0.9 and 1.3 Å. This range includes smaller ions such as Zn2+ and Mg2+ and larger ions including Pb2+, Sr2+, and Na+. The minor difference in the ionic radii between Ca2+ and Na+ (1.13 Å, in seven-fold coordination),34 combined with Na+ higher electronegativity and abundance in body fluids relative to K+ (1.46 Å), accounts for the observed high content of Na+ in the HA structure.
The Ca/P molar ratios of HA varied in the range of 1.68–1.73, which is slightly higher than the stoichiometric HA (1.67). It is well recognized that the biological apatites do not adhere to a fixed composition; typically, the Ca/P ratios are lower than the stoichiometric HA. These ratios can range from 1.3 to 1.5 in the ACP found in young bones, and from 1.5 to 1.67 in more crystalline and mineralized mature bones.35 The measured Ca/P ratio of 1.68 in HAut is consistent with the mature bones of a 3-year-old cow used as the source of bioapatite. However, it remains uncertain whether the slightly elevated Ca/P ratio in HAut is attributed to ionic substitutions, vacancies at PO43− sites, or P depletion during processing. If P depletion is the primary cause, it appears that autoclaving, calcination, and subcritical water extraction lead to less P loss compared to alkaline hydrolysis. The higher Ca/P ratio observed in HAcm, in contrast to HAc, is consistent with the thermogravimetric results, suggesting the incorporation of inorganic C during mechanochemical activation, a finding which is further supported by the results from Raman spectroscopy (Fig. 4).
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| Fig. 4 Raman spectra in the 940–980 cm−1 region showing phosphate (PO43−) symmetric stretching vibration (ν1) and the 915–940 cm−1 region characteristic of acid phosphates. | ||
The Raman spectra of HA revealed notable peaks corresponding to the symmetric stretching mode of the phosphate group (ν1) around 960 cm−1. This peak demonstrates a pronounced sensitivity to variations in the chemical environment within the HA structure. In addition, Raman peaks at around 925 cm−1 are indicative of protonated phosphate species (HPO42− or H2PO4−, hereafter collectively referred to as HPO42−), in a P–O–H+ bond configuration.17 The presence of H+ in HA nanoparticles is a critical factor for enhancing the dissolution, as highlighted in a previous study.7
A comparative analysis among different HAs revealed that HAcm displays a lower Raman shift with a maximum intensity at 957 cm−1. In contrast, the other HAs exhibited Raman shifts: HAut at 960.2 cm−1, HAc at 960.8 cm−1, HAw at 961 cm−1, and HAk at 962 cm−1. The relatively lower Raman shift observed for HAcm indicates a weaker P–O bond, which may be attributed to the structural disorder, since its proton content was relatively lower than HAc, HAw, and HAut. The apparent discrepancy between the lowest Raman shift of HAcm at 957 cm−1 and the median intensity around 925 cm−1—correlated to the HPO42− content17—can be explained by the mechanical activation of HAc. This activation potentially facilitates reactions with the adsorbed molecules such as CO2, leading to their incorporation into the structure and causing subsequent disorder (see morphology section). This hypothesis is supported by the elemental quantification data revealing that HAcm has the second lowest P content, which cannot be fully explained by mill fragments (Table S2). Conversely, a high HPO42− content of HAc, shown by the Raman band of around 925 cm−1, may stem from the loss of structural water and the initial stages of dehydroxylation, which can generate vacancies and free H+ ions available for the reaction with PO43−.36 In stark contrast, the smallest HPO42− content of HAk is consistent with the effect of alkaline treatment, during which potential dissolution and recrystallization of HAk may have consumed H+ ions previously bound to PO4 groups. In summary, these findings exhibit the intricate relationship between the structural characteristics of HAs, its H+ content, and structural integrity under different treatment conditions.
While the absence of phase changes was confirmed, the increased photon counts for the (211), (112), and (300) diffraction peaks, in conjunction with larger crystallite dimensions along the [002] and [310] directions across all treatments compared to HAut (Fig. 5B), suggest the occurrence of recrystallization. Distinct impacts were noted for each treatment; for instance, the crystallite size of HAc in the [310] direction was more than fourfold larger compared to HAut, whereas the difference when comparing HAk and HAut was considerably less pronounced. Intriguingly, mechano-activation of HAc resulted in a reduction of crystallite size by approximately 50% along the [310] direction, with no notable change in the [002] direction (Fig. 5B). The subcritical water extraction caused the least impact on the bioapatite structure, as evidenced by the crystallite dimensions of HAw and HAut, which is consistent with previous results (see the hydroxyapatite composition section). Alkaline hydrolysis exhibited an intermediate effect on bioapatite crystallinity, between subcritical water and calcination followed by mechanochemical activation. Overall, the crystallite dimensions and respective impact of different treatments on bioapatite are as follows: HAut < HAw < HAk < HAc and HAcm.
The influence of the bone as a whole cannot be overlooked when evaluating the outcomes of treatments on HAs. Bone is a composite material with significant variability in structure and composition, largely dictated by its functional role.16 Such heterogeneity is observed when comparing distinct bones in an animal (e.g., long bones vs. flat bones), distinct anatomical regions of a single bone (e.g., cortical vs. trabecular tissue), bones at different developmental stages (e.g., juvenile vs. mature), and bones from different species (e.g., bovine vs. chicken femur).38,39 At a molecular level, variations among bones can be detected in the content and identity of both collagenous and non-collagenous proteins.39 In turn, the bioapatite content in bone may exhibit variations in composition, degree of crystallinity, and position relative to collagen fibrils.13 Previous studies have explored the collagen/bioapatite ratio as a proxy for differences in mechanical properties among bones.40 This is particularly relevant to the processing of bones to recover HAs, given that the organic matrix serves as a thermal barrier and inhibits recrystallization during treatments. For instance, heating the cortical portion of avian tibia from 100 °C to 800 °C in 100 °C increments did not result in significant recrystallization of bioapatite integrated within collagen fibrils until the complete removal of the organic matrix, which occurred around 600 °C.41 In contrast, bioapatite embedded in non-collagenous proteins such as proteoglycans present in the medullary portion of tibia revealed evidences of recrystallization at a significantly lower temperature, around 400 °C.41 Calcination of the cortical portion of bovine femur (from 100 to 1000 °C) resulted in no significant recrystallization until surpassing the 600–700 °C range,25 and no secondary phase transformation, such as the conversion of HA to β-tricalcium phosphate, was reported before reaching 1100 °C in cortical bovine femur subjected to calcination.42 Notably, a ratio of 53
:
47 wt% of HA
:
β-tricalcium phosphate was observed following the treatment of fish bone at 850 °C for 1 h43 underscoring the influence of the collagen/bioapatite content on thermal processing outcomes across different bones. Although calcination of HAut (femur and scapulae) resulted in a more pronounced increase in crystallite size compared to hydrothermal treatments, the observed effect could have been magnified with a less mineralized bone or higher processing temperatures.
The influence of bone composition on hydrothermal processing is noteworthy, yet a direct comparison with existing literature data present challenges due to the limited range of processing conditions evaluated, particularly compared to the calcination method.25,42 An exception to this observation was found in a recent study,28 which assessed the effects of varying NaOH or KOH concentrations (0.5 and 2 mol L−1) and treatment time (2 to 10 days) on the HA recovered from the cortical portion of bovine bones. Their findings indicated that the prolonged treatment time and higher concentration of NaOH promoted crystal growth, thereby lending support to the dissolution–reprecipitation mechanistic interpretation.
For the assessment of crystallite size distribution in anisotropic HA crystals in this study, 10 peaks exhibiting high signal-to-noise ratios were selected from the diffraction data. This estimation, visualized through kernel density distribution, facilitated the categorization of HAs into two groups: those recovered via hydrothermal treatments versus those processed using thermal treatment (Fig. 5C). Not surprisingly, the bimodal distribution of the HAut exhibited the smallest size range, varying from 27 to 59 nm. In comparison, crystallite size distributions of HAw and HAk exhibited slightly larger dimensions than HAut, with centroids at 45 nm for HAw and 60 nm for HAk (Fig. 5C). For HAc, the distribution was centered around 120 nm, which is threefold higher relative to HAk and HAw. Similarly, HAcm exhibited a broad size distribution, likely attributed to the combination of the sintering process during calcination (see the morphology section) and preferential cleavage along the a or b axes during mechanochemical activation.
Raman and HRTEM analyses indicated a significant presence of amorphous material in HAcm, highlighting the limitation of the crystallite size calculation from sXRD patterns for estimating particle size. As such, the overall constitution of HAcm encompass a broader spectrum of particles in terms of size and crystallinity.
To ascertain the composition of amorphous particles observed in HAcm, the SEM-EDS technique was utilized. The results affirmed that these particles were predominantly composed of Ca, O, and P (Fig. S5), consistent with the composition of calcium phosphates. The notable carbon content detected in the EDS analysis which originated from the carbon stub did not interfere with the detection of Ca and P, nor did it compromise the confirmed absence of Al in the amorphous particles. Summing these findings, it is reasonable to conclude that the platelets and rods originated from HAc, while the fractal-like aggregates of amorphous particles emerged during the mechano-activation process. The abundance of ultrafine amorphous materials associated with the distinct larger rods and platelets likely played a critical role in enhancing the dissolution of HAcm (see the hydroxyapatite dissolution section).
HRTEM micrographs of HAk and HAw revealed a more uniform distribution of particles in terms of size and shape (Fig. 6E and F). HAk consisted of platelets measuring 20 to 50 nm and rods ranging from 29 to 107 nm in length, with widths of 12 to 40 nm (n = 50). In contrast, HAw displayed platelets of 18 to 38 nm and rods measuring 26 to 73 nm in length and a width of 12 to 40 nm (n = 50). Given that the solvent was the only variable between the alkaline hydrolysis and subcritical water extraction, the observed difference in the particle size distributions further confirms that the greater extent of recrystallization occurred in HAk compared to HAw. The fringes visible in the HRTEM micrographs of HAk exhibited d-spacings consistent with the (111) and (110) of HA, as identified through sXRD (Fig. S4). Similarly, the fringes observed in HAw were compatible with the (111), while HAcm showed fringes corresponding to the d-spacing (210). The HRTEM micrographs of HAut displayed agglomerated rods embedded in the organic matrix measuring 32 to 74 nm in length and 19 to 51 nm in width. Additionally, an extra dimension measuring 4 to 7 nm, consistent with the platelet thickness of bioapatite in mature bovine bone,44 was noted in HAut. However, TEM does not allow for distinguishing this dimension from the width of the rods (Fig. S5).
While thermodynamic solubility remains unchanged between nano-HA and micro-HA, dissolution kinetics is significantly accelerated in the nanomaterial, which was expected to lead to higher dissolution rates of HAw and HAk compared to HAcm. However, the influence of structural defects and compositional differences in HAcm appears to override the effect of particle size, thereby enhancing P release from HAcm compared to other nano-HA (Fig. 7). Specifically, the distinct dissolution pattern of HAcm may be attributed to its higher H+ content compared to HAk, as evidenced by the relative intensity of bands around 925 cm−1 in Raman spectroscopy, and to the heterogeneity in particle size and degree of crystallinity revealed from HRTEM and sXRD analyses, respectively.
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| Fig. 7 Kinetics of P released over dissolution experiments from HAcm, HAk, and HAw. Error bars represent standard deviation (n = 3). | ||
The initial rapid dissolution phase in the HAcm release curve, followed by a 20–40 s plateau, likely results from the dissolution of ultrafine amorphous particles and structurally flawed surfaces of rods and platelets (Fig. S4). This stage precedes micrometric particle dissolution and is followed by a second plateau (65–75 s), indicating more crystalline regions beneath the surface that temporarily delay further dissolution. The dissolution mechanism likely involves the formation of kink sites47 with mechanical shocks in HAcm creating reactive sites for H+, thus enhancing initial dissolution. As the reaction progresses into less imperfect regions, additional activation energy may be needed for further dissolution. Variability in the HAw dissolution pattern is attributed to residual organic molecules (Table 1), which interferes with surface reactivity and hinders reproducibility. Despite its lower dissolution rate, HAk showed the least variable P release pattern, highlighting consistency for potential process engineering replicability. The lower and slower P release from HAk and HAw is likely due to fewer structural and surface imperfections, resulting in fewer reactive sites. Interestingly, the P mass released from both HAk and HAw remained around 5 μg over time, despite decreasing HA mass.
A blend of amorphous, strained, and crystalline particles exhibiting an irregular step-terrace surface structure was observed in HAcm (Fig. 8), probably enhancing dissolution. Amorphous particles present in HAcm may exhibit similarities with amorphous calcium phosphate (ACP) in terms of structural disorder48 and enhanced solubility.49 EDS results of amorphous particle agglomerates in HAcm provided semi-quantitative estimates (Fig. S5), with a Ca/P ratio of 2.09, which is within ACP ranges (1.0–2.2).49
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| Fig. 8 High-resolution transmission electron micrograph depicting the formation of the step-terrace structure on HAcm surfaces during dissolution (magnification of 510 k). | ||
Interestingly, a contrasting trend in P release from HA and citrate-stabilized ACP has been documented.10 This contrast may indicate that P release from HAcm, consisting of ultrafine amorphized particles and HA, may produce a sigmoidal pattern over extended dissolution periods. If so, this product may be an ideal model for slow-release fertilizers.50 Given that bone is a natural source and both calcination and mechano-activation are physical treatments, HAcm may even serve as a nanofertilizer for providing supplant P in organic farming systems.
The interactions between HA nanorods obtained by mechano-activation of microcrystalline HA and P-deficient barley roots were evaluated in a hydroponic system.46 The HA nanorods exhibited a ζ-potential ranging between −25 and −30 mV due to citrate and foreign ion incorporation and successfully provided P to plants, restoring physiological functions associated with the element in less than 48 hours. Interestingly, it was found that P contained in nanocrystalline HA was dissolved prior to uptake at the root cap region, while in mature epidermal and cortical cells, the particles were able to penetrate the apoplastic region before being fully dissolved.46 Unfortunately, the effects of mechanical treatment on the HA structure and dissolution were not evaluated, hindering comparison with HAcm.
The P release profile of HAcm is expected to correlate with the P uptake kinetics of many crops, suggesting its potential as an effective slow-release fertilizer. If so, this approach may enhance P recovery by plants compared to conventional P fertilizers. It is important to highlight that the transition from bench-scale research to greenhouse and field applications presents an opportunity for integrated assessments of P use efficiency and economic viability, including the energy balance associated with calcination and milling processes. Optimizing processing parameters to minimize costs should be a key factor for developing scalable and sustainable fertilizer production. Such efforts, tied with environmental benefits of bone waste valorization and P recycling, could offer economic value while reducing dependence on geogenic P sources.
All data are included in the text and supporting information (SI).
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