Abstract
Solvent-free ball milling was used to activate kaolin, a trioctahedral clay material, with diammonium phosphate[(NH4)2HPO4] to serve as a fast-acting phosphorus and nitrogen releasing fertilizer. Different tests on a mixture of 3:1 weight ratio of kaolin: (NH4)2HPO4 were performed to analyze the level of incorporation of (NH4)2HPO4 in the kaolin and the degree of liberation of
1 Introduction
Most manufactured fertilizers contain N, P, and K compounds that are highly soluble and volatile which makes them susceptible to environmental loss into the surrounding soil that, in turn, increases soil and water pollution [1]. This loss can lead to the increased usage of fertilizers in order to fulfill a sustainable and sufficient food production which means more pollution and more cost. Furthermore, the lack of NPK resources may undermine food security and requires changing the way to deal with fertilizer management [2].
Inorganic fertilizers are the most common type in the agricultural chemical industry. Generally, fertilizers should boost plant development by delivering the needed nutrients to crops. They also play a vital role in controlling the pH and fertility of the soil. Mineral fertilizers production has increased over the years in parallel with the rise of human population and their need for food [3, 4]. In this regard, it is known that the main nutrients for plant growth are nitrogen, phosphorus, and potassium [5]. Usually, phosphorus is recovered from different types of clay minerals such as kaolin and feldspar, which are abundant in the soil, but quite imbalanced in their allocation.
Solid-state mechanochemical processes are regarded as a long-term free-solvent material synthesis approach [2, 6, 7]. Co-grinding clay minerals like talc and kaolin with chemical salts of N, P, and K as source ingredients could result in extremely efficient slow-release fertilizers [7,8,9].
According to previous research results, the solid-state mechanochemical reactions to prepare slow-release fertilizers (SRF) can be achieved by the ball milling of kaolin or Al2O3 with soluble salts of N, P and K [10,11,12].
Al-Rawajfeh et al. [13] used a planetary ball mill to crush various mixtures of kaolin with KH2PO4 or (NH4)2HPO4. To investigate the intercalation of KH2PO4 and (NH4)2HPO4 into kaolin layers to release K+,
Even though solubilization and release of compound species are basic physico-chemical processes with a range of applications [14], the examination of release kinetics and mechanisms is of enormous importance for the deep understanding of the behavior of SRFs, mechanisms and kinetic processes for drug administration and formulation have been reported in various research [15]. Natural and/or manufactured chemicals have been employed for the release of plant nutrients, moreover, corrosion behavior study of galvanized steel in seawater environment and for solar panels [16, 17].
The current research aims to investigate the effects of milling speed and time on the characteristics of the (kaolin–(NH4)2HPO4) system, to reduce the kaolin clay mineral to an amorphous phase and develop a novel chemical bonding as an amorphous phase between K-Al-Si-P-O. The one-of-a-kind target product will eventually deliver a moisture layer structure SRFs that limit
2 Experimental
2.1 Materials and mechanochemical process
Diammonium phosphate [(NH4)2HPO4] was purchased from Panreac, Spain (> 90%). Kaolin (Al2Si2O5(OH)4) was collected from Wadi Araba region, south of Jordan [18, 19]. A planetary Fritsch Pulverisette-7 ball mill (Germany) that has two zirconium milling jars (45 cm3 interior volume each) with six zirconium balls of 15 mm diameter was used for the milling process that is considered as solvent-free. Table 1 shows the experimental conditions involved in the experiments (ratio, milling speed and duration).
The experimental mixture ratios and conditions.
| Series | Sample (Kaolin: (NH4)2HPO4) weight ratio | Milling speed (rpm) | Duration (min) |
|---|---|---|---|
| Exp. 1 | 3:1 | 200, 400, 600 700 | 120 |
| Exp. 2 | 3:1 | 600 | 60, 120, 180 |
To avoid excessive heat that might affect the results of the milling process, the experiments were run for 10-minute periods separated by a 5-minute rest time.
2.2 Characterization
The morphology change of the produced samples was followed by using a Fourier transform infrared spectrometer (FTIR, NEXUS, EPS-870) in the wavenumber range of 4000 to 500 cm−1 with 2 cm−1 resolution. Thermogravimetric analysis (TGA) curves were obtained with a (TG-DTA, STA-409 PC, NETZSCH) at a rate of 10°C/min from room temperature to 1000°C in an N2 atmosphere.
To study the kinetics of leaching experiments of the mechanically activated kaolin–(NH4)2HPO4 to release nutrients, the milled materials were disseminated in an aqueous solution (1 g milled sample, 50 mL distilled water) in a 100-mL glass beaker at room temperature for 1 day, 2 days, and 7 days. After leaching, a filter paper with a pore size of 0.45 m was used to carry out the suction filtration for the solid–liquid separation. The quantities of
3 Results and discussion
The first part deals with the results of varying the milling speed for the (3:1) kaolin–(NH4)2HPO4 mixture while the second part shows results of changing the milling duration. Finally, the kinetics study results of ammonium and phosphate ions leaching are presented.
3.1 Effect of milling speed
Figure 1 shows the XRD patterns of kaolin–(NH4)2HPO4 (3:1) mixture as well as their corresponding starting materials milled at a speed of 600 rpm for 120 min. The XRD patterns showed that some characteristic patterns corresponding to (NH4)2HPO4 and kaolin had disappeared in the milled product, which clearly suggests that (NH4)2HPO4 gets incorporated into the amorphous structure of kaolin [13].
![Figure 1 XRD patterns of kaolin–(NH4)2HPO4 sample system milled at speed 600 rpm for 120 min [13]](/document/doi/10.1515/jmbm-2021-0028/asset/graphic/j_jmbm-2021-0028_fig_001.jpg)
XRD patterns of kaolin–(NH4)2HPO4 sample system milled at speed 600 rpm for 120 min [13]
According to the FTIR results, dihydroxylation of the silicate layers occurs after physio-chemical treatment of kaolin clay minerals with (NH4)2HPO4, as shown in Figure 2. The stretching vibrations of the hydroxyl groups at 3688 and 3619 cm−1 diminish with increasing milling speed and disappear for samples prepared at 700 rpm, according to the spectra of kaolin–(NH4)2HPO4 sample mixes.

FTIR spectra of kaolin–(NH4)2HPO4 samples milled at different milling speed for 120 min
Untreated kaolin samples can be classified into one of two types of hydroxyl groups. The inner hydroxyl group resides within lamellae in plane common to both the tetrahedral and octahedral sheets at 3684 cm−1, and inner hydroxyl group lie within lamellae in a plane common to both the tetrahedral and octahedral sheets at 3627 cm−1. The intensity and position of inner surface hydroxyl groups are generally changed by intercalation; however, intercalation did not influence on the band at 3619 cm−1 [20, 21]. As can be shown in this study, kaolin clay material has four distinct IR bands, whereas badly organized kaolin only has three [22]. The Si-O stretching area consists of stretching bands at 1113, 1000–1003, and 1030 cm−1, as well as Si-O bending vibrations at 790, 751 cm−1, and 688 cm−1. The inner hydroxyls are ascribed to the Al-OH bending vibration at 912 cm−1. The sample also shows the vibration of the inner surface hydroxyl groups at 936 cm−1 [22, 23].
The hydroxyl vibration disappearance at 912 cm−1 and the intensity decreases of the Si-O band at ~1000 cm−1 that confirm the mechanochemical decomposition of kaolin at 700 rpm. Solihin, et al., [8] study illustrated a milling process for kaolin–sample mixtures at a minimum of 400 rpm milling speed is required to intercalate nutrients such as (NH4)2HPO4 into the amorphous kaolin structure. However, at mill speeds above 400 rpm, the beginning samples were gradually reduced to an amorphous state at mill speeds above 400 rpm, which could indicate that (NH4)2HPO4 has been integrated into the amorphous structure of kaolin, which has already been proven by XRD [8].
The FTIR spectra shown in Figure 2 elucidated that at lower milling speeds, below 400 rpm, characteristic spectra corresponding to residual raw materials exist in the products, like as a distinct kaolin peak from 3627–3685 cm−1. Moreover, the disappearance of the preceding peaks at milling speed above 400 rpm pointed to reducing the starting samples into an amorphous state, which might suggest that (NH4)2HPO4 has been intercalated into an amorphous kaolin [7].
Also, the broad N-H bands located between 2700–3200 cm−1 was disappeared after samples milling, illustrated the formation of new product kaolin–(NH4)2HPO4 system.
The distinctive band of the Si-O, which stretches approximately 1049 cm−1 for high milling speed samples, increased broader and shifted for milled samples to a higher frequency, as evidenced by the development of amorphous silica during the mechanochemical reaction.
Figure 3 demonstrates that the observed mass loss of 12.3% caused by thermal dehydroxylation of the kaolin in the temperature range of 450 to 650°C agrees well with the predicted value of 13.96%, indicating that the starting kaolin is of good purity. The ammonium monohydrogen phosphate salts disintegrate in essentially two phases, exhibiting endothermic peaks for ammonium monophosphate at 187°C and 600°C, respectively, whereas, decomposing into two steps for sample milled at 200 rpm with peaks at 185°C and 580°C (Figure 3), which illustrate that some of the starting materials have remained. However, decomposing into one step for sample milled at 700 rpm at 100°C is relating to water transfer, these findings revealed that solid-state mechanochemical treatment resulted in increased water sorption due to crystal size reduction. It should also be noted that, unlike the precursors, the thermal decomposition of kaolin/K2HPO4 was not a multi-step process, but rather a sluggish continuous process that terminated approximately 650°C. [9].

TGA patterns of kaolin–(NH4)2HPO4 sample mixture milled for 120 min at different milling speeds
Table 2 shows the release of
Concentration in (ppm) of
| Milling Speed (rpm) | Conc. of
|
Conc. of
|
|---|---|---|
| 200 | 6122.5 | 3456.6 |
| 400 | 4246.7 | 2553.0 |
| 600 | 303.2 | 415.1 |
| 700 | 99.9 | 88.3 |
| St.Dev | 2978.297 | 1637.193 |
The

Profile of nutrients release of kaolin–(NH4)2HPO4 sample mixtures milled for 2 h at different milling speeds and dispersed in distilled water for 24h
3.2 Milling time effect
At three milling times of 60, 120, and 180 minutes, the impact of milling time on the 3:1 weight ratio characteristics of kaolin–(NH4)2HPO4 mixture milled at 700 rpm was examined. FT-IR spectra of kaolin–(NH4)2HPO4 samples with a ratio 3:1 that milled at the speed of 700 rpm for several different durations discussed in [13].
The band vibration intensities fluctuated as the milling time increased, especially at a peak of about 915 cm−1. Also, on the different milling samples, the kaolin peaks with strong absorption intensity, at 3620–3690 cm−1, could not be seen, showing that intercalation occurs. The intensity of the peaks diminished as the time approached 180 minutes. However, the disappearance of peaks detected at 915 cm−1, 3627, and 3684 cm−1 for samples with milling time above 120 min indicated that the raw materials were reduced to an amorphous form, suggesting that (NH4)2HPO4 has been absorbed into the amorphous structure of kaolin.
Figure 5 represents thermal gravimetrical patterns for kaolin–(NH4)2HPO4 samples milled at 700 rpm for different duration and shows that no distinguished mass-loss features were reported for the starting materials at any milled time, which attests to their destruction during grinding indicated that 60, 120 and 180 min are suitable periods for preparing slow released fertilizer from kaolin–(NH4)2HPO4.

TGA patterns of kaolin–(NH4) samples milled at 700 rpm for different duration
Table 3 summarizes the concentration of nitrogen and phosphorus nutrients with milling time released from kaolin–(NH4)2HPO4 that were milled at 700 rpm for different milling times.
Concentration of
| Milling Time (min) | Conc. of
|
Conc. of
|
|---|---|---|
| 60 | 372.5 | 767.0 |
| 120 | 303.0 | 415.1 |
| 180 | 37.0 | 48.4 |
The release of
The nutrients profile of

Nutrients release profile of kaolin–(NH4)2HPO4 milled at 700 rpm at varying milling time and disseminated in distilled water for 24h
3.3 Kinetics results
The nutrient release kinetics were determined in this study using a quantitative examination of the concentration of phosphorous in solution throughout time. Figure 7 shows the concentration of phosphate ion for the system milled at 700 rpm for 2 h.

Release of phosphate ion from the kaolin–(NH4)2HPO4 system milled at 700 rpm for 2 h
For the kaolin–(NH4)2HPO4 system, the concentration changes of
4 Conclusions
A solid-state mechanochemical method was used to synthesize slow-release N and P fertilizer ingredients using kaolin as the host material and (NH4)2HPO4 as the precursor. Only the conversion of diverse N, P sources in solid clay minerals was possible using the free-solvent procedure via milling. The adopted process was both environmentally friendly and economically feasible for supplying an alternative to the current chemical fertilizer, which is typically obtained from some salt-water lakes, and it is expected to make a significant contribution to the balanced development of N and P fertilizers. The slow-release characteristic behavior for phosphorous was evidenced through a kinetics study.
Acknowledgement
The University of Jordan and Tafila Technical University are greatly acknowledged for funding this research project.
Funding information:
The authors state no funding involved.
Author contributions:
All authors have accepted responsibility for the entire content of this manuscript and approved its submission.
Conflict of interest:
The authors state no conflict of interest
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© 2021 Mohammad R. Alrbaihat et al., published by De Gruyter
This work is licensed under the Creative Commons Attribution 4.0 International License.
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