1. Introduction
Anaerobic digestion is one of the most important and advantageous processes in livestock manure waste management [
1]. A byproduct of the process is digestate, which contains high concentrations of N, P, and K, that make its storage and disposal costly, especially under the current EU directive strictly limiting the amount of nitrogen spread on fields [
2,
3]. The traditional separation treatment used for digestate is inconsistent in its ability to reduce ammoniacal nitrogen and the digestate volume [
4]. On the other hand, the clarified fraction of digestate contains high levels of ammonium and ammoniacal nitrogen that could serve as agricultural resources if reused as fertilizers. One means by which to reuse these problematic products is to exploit the high affinity and high exchange capacity of zeolites to adsorb ammonium nitrogen from liquid fraction digestate [
5].
The advantage of using zeolites in adsorption processes lies in their lower cost compared to other purification methods (about 300 €/ton). Furthermore, the removal of ammoniacal nitrogen makes clarified fraction digestate comply with required limits, and consequently, downloadable into water bodies and/or fields [
6].
Natural zeolites are a very abundant component of generally volcanic rocks (tuffs), and are low-cost resources that have the capacity to exchange ions in their own structure with those in the aqueous phase [
7].This process is possible because of compensating cations, such as Na, Mg, Ca, K, Sr, Ba, and others, that are linked to a negatively charged framework of the zeolite minerals by relatively weak ionic bonds. Further weakening by the dielectric field exerted on them by the molecules in strong polar water causes them to be replaced by other cations with an equal number of positive charges [
8]. Zeolites show a “selectivity” toward specific cations depending on their structural features. Generally, the selectivity is related to cations of low solvation energy (K, Cs, NH
4+, Pb, Ba, Sr) that are able to easily get rid of the hydration sphere, so that the ions can enter into zeolite extra-framework sites [
9].
The peculiar properties of zeolites make them suitable as adsorbents in liquid digestate separation and purification, and for reuse as plant fertilizers. In fact, they may enhance agroecosystem sustainability by creating a “virtuous” circle between anaerobic digestion and agriculture. The use of natural and enriched zeolites as amendments in agriculture has been studied for its soil characteristic modifications [
10], i.e., reduced N leaching, increased N use efficiency, increased water use efficiency, and improved crop yield [
11,
12,
13]. However, findings on their ability to release N slowly are well known from literature [
14]. Indeed, Leggo [
15] observed an increase in nitrate levels after using natural clinoptilolite enriched by composting with poultry manure.
Ammonia or ammonium added to soil is first oxidized into nitrite and then to nitrate by Ammonia Oxidizing Bacteria (AOB) and Ammonia Oxidizing Archaea (AOA). The production of nitrate can promote plant growth, but too much can cause excess nitrification, the release of nitrate into the groundwater, and eventual pollution and eutrophication. Therefore, any evaluation of the potential to use ammonium-enriched zeolite from anaerobic digestate as a slow release fertilizer must include an assessment of AOA and AOB. Moreover, the effects of zeolite amendments on the soil microbial biomass (MB) have been mostly unexplored [
16].
To test the effectiveness and sustainability of charging zeolite with ammonium from digestate liquid to act as a slow release fertilizer, we enriched natural zeolite (clinoptilolite) with an ammonium-rich solution that simulated field conditions, and assessed its adsorbent properties. To evaluate its potential for use as a fertilizer, ammonium-rich zeolite was applied to a cultivation of strawberries. Plant growth and production parameters during the entire plant cycle, as well as parameters relating to fruit quality, were measured. Strawberry was chosen because it has a short production cycle, and it can be compared to other research on the use of zeolite as substrates in strawberry [
17,
18,
19]. Zeolite was chosen as the substrate for NH
4+ uptake; this choice was made to avoid bringing other nutrients into the system, to stress the model and to verify the benefits of ammonium fully charged zeolite.
The application of the enriched zeolites on strawberries was performed in pots. Three different amounts of ammonium-enriched zeolites were administered to vary the N content supplied, and to detect possible nitrogen release differences. Finally, in order to evaluate the effect on microbial communities and their potential release of nitrate into water, total bacteria (AOB) and archaea (AOA), as well as nitrogen forms, were measured in the plant substrates.
2. Materials and Methods
The study was performed in the summer of 2019 in the experimental farm of DISAFA in Chieri, North West Italy.
2.1. Zeolite Preparation: Enrichment Method and Desorption Evaluation
Natural zeolite (clinoptilolite) from Bulgaria enriched with an ammonium-rich solution was added to a commercial cultural substrate for strawberry growing. To carry out several ammoniacal nitrogen removal tests on standard solution and on the digestate, a zeolite composed almost entirely of clinoptilolite with only small percentages of cristobalite and tridymite was used. The composition and physical features of the zeolite are shown in
Table 1 and
Table 2. Technical data is given in the
Supplementary Materials.
In addition to the physical–chemical features provided by the zeolite supplier, removal efficiency tests on standard solutions and real samples were performed.
To this end, 20 g of zeolite was put in contact with 200 mL of a standard solution of ammonium chloride at 1000 mg/L, pH 6. The nitrogen sorption kinetics was studied; several aliquots of standard solution in the percolation system were taken manually every 30 min until 400 min. The experiments lasted 24 h. The maximum ammonium sorption was reached in about three hours (about 67%).
After these tests, a sample of digestate from a local farm was characterized at the University of Torino Chemistry lab (3700 mg/L of ammonium, pH = 8.5), and zeolite ammonium sorption was tested to prove the removal efficiency in a real case study. However, to limit the focus of the trial to ammonium exchange and to minimize the introduction of nonrelevant variables associated with a real digestate (for example, microbiological interference with future plant growth), a simulated digestate was prepared from a solution of ammonium carbonate (5000 mg/L, pH level about 8). Ammonium carbonate was chosen instead ammonium chloride, due to its more basic features. With the use of ammonium carbonate solutions, it was possible to reach a pH level similar to that of the digestate. First, 200 mL of ammonium carbonate solution was placed in a waterproof container with a hole at the bottom. Inside the system, a filter of zeolite (40 g) was put in contact with the surface of the solution. Digestate has a higher ammonium concentration than standard solutions. The best trade-off of zeolite:solution ratio tested was 1:5, using 40 g of zeolite in 200 mL of solution. With a pump and pipes system, the solution was circulated (10 mL/min) for 24 h on the zeolite filter and pumped out at the bottom. In this way, a percolation system was created. To saturate the zeolites, identical solutions of simulated digestate were prepared, placed in contact with the zeolites and percolated for 24 h. After three percolations, the zeolites were deemed to be fully charged with ammonium. Several replicate samples were performed, yielding fully-charged zeolites each time. Zeolite NH4+ content was measured before and after the percolation process using the Kjeldahl distillation technique. The zeolite was considered to be completely charged when the ammonium content of the solution was unchanged (5000 mg/L). The ammonium content adsorbed in zeolite itself was also tested. The fully charged zeolite reached a 4% w/w NH4+ content. The ammonium desorption process was also evaluated. A sample of the ammonium-charged zeolite (40 g) was placed in water to evaluate NH4+ release using the same percolation system. The experiments lasted 200 min due to the natural water evaporation that changed the total volume of the solution, and due to the microbial activities that occurred.
2.2. Culture Substrate
The chosen culture substrate was a commercial horticultural compost mix (Domotorf).
The substrate was a mix of fine blond, brown peat and bark humus, enriched with fulvic acids and organic substances that improve the soil structure. The chemical–physical features are as follows: Total organic carbon: 30% peat = 50% w/w, Humic + fulvic acids: 7% w/w, total N: 13% w/w, Cu (ppm) = 150, Zn (ppm) = 500; pH (in H2O) = 6.5–7.5, Electric conductivity (dS/m) = 0.4, apparent dry density (Kg/m3) = 180, total porosity = (% v/v) = 87.
2.3. Strawberry Planting and Treatments
The study was conducted on a commercial variety of frigo strawberry plants (cv Clery).
Each plant was transplanted into a 10 L volume plastic pot containing the different cultural substrate. A total of four treatments (9 pots each) were evaluated:
- (1)
zeolite: cultural substrate (600 g) + 280 g of enriched zeolite
- (2)
zeolite + 30%: cultural substrate (600 g) + 360 g of enriched zeolite
- (3)
zeolite − 30%: cultural substrate (600 g) + 200 g of enriched zeolite
- (4)
control: cultural substrate (600 g), not fertilized (no zeolites were added).
The nitric and ammonium nitrogen content of the compost was measured at the start of the trial. Charged zeolites, enriched with 4% ammonium, were introduced into the pots and mixed with the cultural substrate. The zeolite amounts were chosen based on previous work and set to optimal N concentration in the growth medium for strawberry [
20]. After the transplant, water was supplied with a drop by drop automatic system (0.5 L/day) until the plants were well-developed. Thereafter, water was supplied by drip irrigation (one dripper per pot) at a frequency adapted to the climatic demand (approximately 0.5 L four times a week). All the pots were placed in an open field under shade cloth. The cultivation cycle was of 8 weeks. No fertilizers or pesticides were added.
2.4. Measurements and Analyses
2.4.1. Analyses of Strawberry Plants
Several parameters related to plant growth were measured and recorded as follows: (i) plant weight, at the beginning and end of the production cycle (g), (ii) flower count per plant, (iii) leaf length (cm) (iv) leaf count per plant (v) stolon count per plant, (vi) fruit count per plant, (vii) fruit weight (g), (viii) leaf chlorophyll content (SPAD content), and (ix) upper side leaf color (L*, C*).
At the end of the production cycle, the strawberry plants were removed with a shovel to prevent damage to the root system. Any substrate stuck to the roots was carefully removed. The plants were transferred to the laboratory, where they were washed and dried. Leaf chlorophyll content (SPAD index) was measured nondestructively with a portable SPAD-500 chlorophyll meter (Konica Minolta Sensing Inc., Osaka, Japan). Relative values displayed by the instrument were positively correlated with chlorophyll concentration [
21]. The SPAD-values were recorded from five leaves on each plant. Leaf color was measured with a colorimeter (Model CR-400, Minolta, Osaka, Japan) and expressed according to the CIELAB scale (L* a* b*). The L*, a*, and b* values indicate lightness (dark to light), index of redness (green (−) to red (+)) and index of yellowness (blue (−) to yellow (+)), respectively. The dimensions of color Chroma (C = (a*
2 + b*
2)
½) were calculated from the numerical values of a* and b* [
22]. Chroma shows the radial component of the cylindrical coordinate of the L*a*b* color system, and represents color intensity.
All the parameters, except plant weight, were evaluated weekly for the first three weeks, and then again at the end of the cycle (after 60 days).
2.4.2. Analyses of Fruit
All of the strawberries from each treatment plot were picked when about 90% of their surface was red. All the strawberries were hand-picked during the cycle. The first red strawberries were picked after 2 weeks, the last after 8 weeks. A daily log of the number of strawberries picked was made. Freshly picked, strawberries were weighed, put in a closing envelope, immediately frozen and then transported to the lab. At a later time, analyses were performed in the lab after defrosting the strawberries.
Three chemical parameters were measured: total soluble solids content (TSS), titratable acidity (TA), and total polyphenols. TSS (° Brix) was measured with a digital refractometer (ATAGO Co., Ltd., Tokyo Japan). TA was determined by titrating 0.1 NaOH to a pH 8.1 with an automatic titrator (Compact 44–00; Crison Instruments, Barcelona, Spain); the results were expressed as milliequivalents of 0.1 mol NaOH per liter [
23,
24,
25]. Finally, the total concentration of phenols was estimated by a slighty modified Folin-Ciocalteu method [
26,
27]. In a vessel, five g of the pulp was extracted with MeOH after 30 min in an ultrasonic bath and filtered. Then, 0.05 mL of the extract and 0.45 mL distilled water were mixed with 2.5 mL of Folin–Ciocalteu’s phenol reagent (1:10 diluted), followed by 2 mL of 7.5% (
w/
v) sodium carbonate. After 5 min at 50 °C, absorbance was measured at 760 nm using a U-5100 Spectrophotometer (Hitachi, Tokyo, Japan). The total phenolic content was estimated from a standard curve of gallic acid, and the results were expressed as mg gallic acid equivalents (GAE)/100 g fresh weight. The measurements were taken in triplicate and mean values were calculated.
2.4.3. Microbial Analysis
DNA was extracted from the cultivation substrate using the FastDNA
® Spin kit for soil (MP Biomedicals, Solon, OH, USA), according to the manufacturer’s instructions. Three replicate samples of DNA extraction were performed. The quantity and purity of the DNA was measured spectrophotometrically with a NanoDrop ND-1000 (NanoDrop Technologies, Wilmington, DE, USA). Total bacteria and archaea (16S rRNA genes), aerobic ammonia-oxidizing bacteria (bacterial amoA gene—AOB) and archaea (archaeal amoA gene—AOA) standards and samples were analyzed using specific primers described in Mania et al. [
28]. The qPCRs were conducted with a 2 μL 1:10 DNA dilution. The 20 μL reaction mix contained 10 μL SsoAdvanced Universal SYBR Green Supermix (Bio Rad Laboratories, Munich, Germany) and 0.3 μM of forward and reverse primers. The optimal dilution of the DNA extracts was previously tested to compensate for any reaction inhibition (data not shown). The qPCR reactions were done on a Chromo 4TM Continuous Fluorescence Detector, associated with a PTC-200 thermocycler (MJ Waltham, MA, USA), using appropriate target gene-specific amplification cycles. Data acquisition and analysis were conducted with OpticonMonitor 3.1.32 software (Bio-Rad Laboratories). To eliminate artefacts and specific amplification, melting curves were verified and amplicon size checked by electrophoresis.
2.4.4. Chemical Analyses of Zeolite at the Beginning of the Experiment
The sorption kinetics of NH
4+ by zeolite was evaluated. All the withdrawals taken during kinetics were analyzed following the ammonium official distillation method using a Kjeldahl apparatus [
29].
The zeolite removal efficiency was due to the pH of the solution, which affects the zeolite ion exchange mechanism [
30].
For this reason, we chose to evaluate the influence of pH on removal efficiency. Under the same conditions, 20 g of zeolite was put into the percolation system with 200 mL of NH4+ buffered solution at pHs between 5 and 9. All buffer solutions had the same concentration (about 1000 mg/L). Thereafter, a test with a sample of real digestate was conducted in the percolation system, this time using 40 g of zeolite and 200 mL of digestate at about 3700 mg/L and pH 8.5. Characterization by the Kjeldahl method detected the ammonia nitrogen content after the real digestate was in contact with the zeolite.
To evaluate the amount of N absorbed into zeolite frameworks, 20 g of fully charged zeolite was put in contact with 200 mL KCl 2 M and stirred for 1 h at 20 °C. After that step, it was centrifuged for 10 min at 3000 RPM and filtered using Whatman n°4 paper. The filtered solution was analyzed following the official distillation method using a Kjeldahl apparatus [
29].
2.4.5. Chemical Analyses of the Substrate at the End of the Strawberry Growing Cycle
At the end of the growing cycle, the substrates were analyzed to determine the amount of N in them and what was still available to the plant. To evaluate the amount of N sorped into zeolite frameworks at the end of each growing cycle, 20 g of fully charged zeolite was put in contact with 200 mL KCl 2 M and stirred for 1 h at 20 °C. After that step, it was centrifuged for 10 min at 3000 RPM and filtered using Whatman n°4 paper. The filtered solution was analyzed following the official distillation method using a Kjeldahl apparatus [
29].
At room temperature, potassium removes the ammonium ions bound to the soil exchangers, while the nitrogen fraction (comprised of nitrates and nitrites) is brought into solution by the dipolar effect of water. To analyze the zeolite-treated solutions, the distillation method to determine ammonium was followed [
31].
Nitrogen run-off was not evaluated; it was assumed that all the nutrients were sequestered by the plant. In addition, it was supposed that the drip irrigation system had eliminated of any feasible leaching during the strawberry growing cycle.
2.5. Statistical Analyses
One-way analysis of variance (ANOVA) was performed followed by a Duncan’s post hoc test to compare mean values. Differences were considered significant when p-values were lower than 0.05. Statistical software (Statistica 7.0, Statsoft, Tulsa, OK, USA) was used.
4. Conclusions
This study of the effect of zeolite ion exchange in strawberry highlighted their ability to retain amounts of nitrogen that would normally be released into the environment. In particular, the trials demonstrated that the zeolite ammonium removal efficiency is best at a pH of about 8, which corresponds to the normal pH of the liquid fraction of digestate. The solution tested in our hypothesis, i.e., reused, ammonium-enriched zeolites as agricultural soil enhancers or fertilizers, produced positive results. The desorption tests, together with the measures of microbial abundance and nitrogen forms in the plant substrates, showed how absorbed N is slowly released over time and gradually transformed into nitrate. The test compared four treatments that differed in terms of the intake of nitrogen in the cultural substrate. In the control treatment, the nitrogen present characterized the used substrate, without further additions, while in the other treatments, different doses of nitrogen-enriched zeolites in ammonia form were added. Obviously, it was expected that strawberries grown in the presence of increasing doses of nitrogen would be more developed than those from control plants, but the aim was to verify the slow release of nitrogen by the zeolites, and to determine whether different doses of ammonium-enriched zeolites could cause differences in the production cycle of strawberries, i.e., similar to what is detectable with normal nitrogen fertilizations. It is known, however, that there is no linear proportionality in terms of increase in production as more nitrogen is added; therefore, we wanted to study whether different nitrogen inputs added using zeolites as carriers gave rise to different behavior in the study plants. Strawberries grown in the enriched substrates resulted in an improved aerial apparatus, including more leaves. Even at the end of the growth cycle, the plants grown with N released from zeolites were greener and had more leaves, with a higher SPAD index indicating greater photosynthetic activity. Noteworthy as well was an increase in the number of stolons emitted per plant, which allows the plant to multiply in the following season. Fruit growth was also slightly increased during the production cycle in zeolite-treated plants. The relatively poor fruit yield that was obtained in the trial was due to the design of the experiment that limited supply of nutrients to nitrogen. Fruit growth depends on the presence of other nutritive elements in addition to N, such as P and K. On the other hand, the N supplied in the trial led to enhanced fruit acidity and sugar, parameters that improve taste.
In conclusion, strawberry plants treated with ammonium-enriched zeolite showed positive effects in growth and photosynthetic activity measures; however, it wasn’t possible to identify a unique trend with respect to the doses of enriched zeolites added to the substrate. All the data point to environmental benefits for more widespread use of zeolite in livestock waste treatment. In future, we plan to continue the study using a real sample of digestate, and to test the efficiency of ammonium-charged zeolite on a fruit orchard. Another aim will be to investigate the economic impact of this choice.