| Literature DB >> 36159737 |
Chongqing Wang1, Dan Luo1, Xue Zhang1, Rong Huang1, Yijun Cao1, Gonggang Liu2, Yingshuang Zhang3, Hui Wang3.
Abstract
Increasing global population and decreasing arable land pose tremendous pressures to agricultural production. The application of conventional chemical fertilizers improves agricultural production, but causes serious environmental problems and significant economic burdens. Biochar gains increasing interest as a soil amendment. Recently, more and more attentions have been paid to biochar-based slow-release of fertilizers (SRFs) due to the unique properties of biochar. This review summarizes recent advances in the development, synthesis, application, and tentative mechanism of biochar-based SRFs. The development mainly undergoes three stages: (i) soil amendment using biochar, (ii) interactions between nutrients and biochar, and (iii) biochar-based SRFs. Various methods are proposed to improve the fertilizer efficiency of biochar, majorly including in-situ pyrolysis, co-pyrolysis, impregnation, encapsulation, and granulation. Considering the distinct features of different methods, the integrated methods are promising for fabricating effective biochar-based SRFs. The in-depth understanding of the mechanism of nutrient loading and slow release is discussed based on current knowledge. Additionally, the perspectives and challenges of the potential application of biochar-based SRFs are described. Knowledge surveyed from this review indicates that applying biochar-based SRFs is a viable way of promoting sustainable agriculture.Entities:
Keywords: Agricultural production; Biochar; Slow-release fertilizer; Soil amendment; Sustainability
Year: 2022 PMID: 36159737 PMCID: PMC9488105 DOI: 10.1016/j.ese.2022.100167
Source DB: PubMed Journal: Environ Sci Ecotechnol ISSN: 2666-4984
Fig. 1Schematic of the research evolution of biochar-based SRFs.
Fig. 2Various methods for the synthesis of biochar-based SRFs.
Biochar-based SRFs fabricated by different methods and slow-release performance.
| Fertilizers | Preparation methods | Fabrication processes | Nutrients | Slow-release performance | References |
|---|---|---|---|---|---|
| Biochar-based P SRF | Impregnation | Corn stover was pyrolyzed at 500 °C for 30 min under limited oxygen, and the obtained biochar was immersed in KH2PO4 solution at a solid: solution ratio of 1:40 for 48 h, and then filtrated, washed, and dried at 60 °C. | 22 mg g−1 P | Bioavailable P release 40% after 5 d | [ |
| Biochar-based P fertilizers | Co-pyrolysis | Coffee husk and poultry litter were mixed with concentrated phosphoric acid and magnesium oxide (P:Mg molar ratio 1:1). After thorough mixing, the samples were moistened by adding water and then left to rest for 16 h. After drying at 60 °C, pyrolysis was performed at 500 °C for 2 h, and samples were marked CHB (coffee husk) and PLB (poultry litter). | 201 mg g−1 P in CHB, and 178% P in PLB | Total P release 6.47% (CHB) and 8.99% (PLB) within 1 h | [ |
| Biochar-based controlled release N fertilizer | Impregnation | Biochar was produced from pyrolysis of corn stover. Biochar was added in ammonium sulfate solution (mass ratio of biochar to ammonium sulfate 1:1) and continually stirred for 20 min, and then kaolin clay was added and stirred for 20 min. The mixture was dried for 5 h at 65 °C, and then blended with methylcellulose and deionized water and pelletized into particles. The pellets were submerged in polylactic acid solution for 10 s and then air-dried at room temperature for 8 h. | – | N release 70% over 12 d in water and 25 d in soil. | [ |
| Mg-enriched biochar fertilizer | Co-pyrolysis | Corn stalk was dispersed MgCl2·solution for 12 h, and the resulting mixture was completely dried at 80 °C. The dried mixture was pyrolyzed at 500 °C for 1 h under N2. The obtained biochar was added into the mixture of biogas effluent and KH2PO4 solution and stirred at 25 °C for 24 h | 200 mg g−1 N and 381 mg g−1 P | N release 18% and P release 16% at 48 h | [ |
| Biochar-based P SRFs | Impregnation Co-pyrolysis | MSRFs: Cotton straw powers were mixed with of MgCl2 solution for 2 h. After drying, the Mg-loaded biochar was prepared in a furnace under N2 at 550 °C for 2 h. Mg-loaded biochar was added into KH2PO4 solutions in a mechanical shaker at 120 rpm min−1 for 24 h at room temperature. | – | P utilization efficiency 53.52% (MSRFs), 65.27% (BSRFs), 74.32% (CSRFs), and 75.83% (PSRFs) after 60 d | [ |
| Biochar-based N/P/K fertilizers | Co-pyrolysis | Residues from biogas production collected from the anaerobic fermentation were air-dried and was ground, and then was pyrolyzed at a temperature of 500 °C for 120 min under nitrogen. Biogas residue-based biochar was mixed commercial compound fertilizer (N: P2O5: K2O = 4:3:3) with a mass ratio of 1:2. Pelletization was conducted using a universal material testing machine, and self-made cylindrical forming molds with different apertures were connected to the universal material testing machine. The pelletized RBF was dried at 25, 65, 105, 145, and 185 °C for 24 h, referred to as RBF-T (RBF-25, RBF-65, RBF-105, RBF-145, and RBF-185. | – | The cumulative N release of RBF-25, RBF-65, RBF-105, RBF-145, and RBF-185 reached 88.68%, 75.35%, 64.89%, 54.39%, and 41.71% after 413 h; the P release of RBF-25, RBF-65, RBF-105, RBF-145, and RBF-185 was 72.07%, 58.75%, 44.12%, 27.48%, and 23.93% after 413 h | [ |
| Biochar scaffolded N SRF | Encapsulation | Autothermal fast pyrolysis of pine biomass at 500 °C was conducted to prepare biochar. Chemical activation of the biochar was accomplished in 5% and 15% H3PO4 solution associated with heat-treated at 465 °C for 2 h under N2. The activated biochar was mixed with dry urea with ratios of 1:2, 1:3, 1:4, and 1:6. The resultant mixtures were ground finely using a mortar and then thermally (137–138 °C) treated for 75 min to melt and infuse the urea into the biochar pores. A 5% Ca-LS aqueous solution and 10% liquefied paraffin wax were added to the urea infused biochar and ground again to prepare the final composite. After manual pelletization of the urea-infused biochar fertilizer, the pellets were dried at 50–55 °C for 48 h. | N content 26.74–34.32% | Urea released in aqueous medium was 61–90% in 4320 min | [ |
| Biochar and biofilm composite towards P SRF | Impregnation | Compound biochar was obtained by pyrolysis of cotton stalk and montmorillonite at 400 °C. Adsorption of PO43- was conducted onto the composite biochar. Cotton straw, polyethylene glycol-400, and glycerin were mixed, and then concentrated sulfuric acid was added to react for 90 min at 160 °C to obtain liquefied cotton stalk-based polyol, which was further reacted with toluene diisocyanate at 75 °C for 20 min to obtain a bio-based membrane material. The toluene diisocyanate and the liquefied cotton stalk-based polyol were stirred at room temperature, and then the mixed liquid was coated on the surface of the composite biochar phosphate fertilizer with a brush. The coated biochar phosphate fertilizer was heated at 75 °C for 20 min. | PO43- 129.92 mg g−1 | The cumulative PO43- release after 30 d was 76%, 65%, 60%, and 53.5% (corresponding the membrane material 0%, 2%–4% and 6%). | [ |
| Biochar-based N SRF | Impregnation | Corn straw was soaked in MgCl2 for 2 h in 1:3 ratios. After drying, the sample was pyrolyzed at 500 °C for 3 h. The modified biochar was soaked in 3 M ammonium nitrate solution for 24 h and then air-dried. Polyvinyl alcohol and corn starch were used as the coating material. The biochar and coating material were mixed at a 1:5 ratio. The biochar was granulated, and 5% solution of coating material was sprayed onto the granules. | Total nitrogen 22.3% | The cumulative nitrate concentration was 886.4 mg L−1 after 24 d; the cumulative ammonium concentration was 1395.5 mg L−1 after 28 d. | [ |
| Biochar embedded-semi-IPN based SRF | Encapsulation | Cotton stalks were heated to 600 °C for 1 h under N2 to prepare biochar. NaAlg, bentonite, biochar, NH4Cl, and K3PO4 were added in distilled water and stirred at 40 °C by mechanical stirring for 45 min. Then, AA, PVP, N-MBA, and APS solution were added into above solution. The polymerization was performed by microwave irradiation at 300 W for 4.5 min under N2. | – | The release ratios of N, P and K within 30 d were less than 80.0% | [ |
| Bentonite modified biochar P SRF | Impregnation | Cotton straw was mixed with H-bentonite, N-bentonite, and OH-bentonite with a ratio of 1:9 and added in deionized water by mechanical stirring at a speed of 750 r min−1 for 45 min. After drying, crushing, and sieving, the samples were pyrolyzed at 600 °C for 2 h under N2. BSRFs was added into KH2PO4 aqueous solution and shaken at 120 rpm min−1 for 24 h at room temperature. | Phosphate was 245.56 mg g−1. | P release within 15 d was 72.6% | [ |
| Biochar-coated urea | Granulation Encapsulation | (1) Urea was added to the coating machine at a speed of 80 rpm, and oxidized starch was sprayed into the machine. (2) biochar was sprinkled in after the urea particles had been uniformly coated with the oxidized starch, and the coating machine continued rotating for 5–10 min to ensure that the coated layer was tight, and then oxidized starch was sprayed again. (3) Step 2 was repeated until all the biochar had been coated onto the particles. (4) Resin was dripped in batches into a plastic container containing BCU from step 3 and embedded in a spiral oscillator to prepare BCU with protective layer I; paraffin was heated until melted and coated on BCU from step 3 with a high-pressure spray gun to prepare BCU with protective layer II. | N content 26.89–34.36% | Cumulative nitrogen release was 72.75–85.71% after 28 d | [ |
| Biochar composite P fertilizer | Granulation Encapsulation | Wood chips were pyrolyzed at 350 °C for 1 h, and the obtained biochar was ground and sieved. Biochar fertilizers were obtained by blending (B) or coating (C) superphosphate with biochar in three proportions (5, 15 and 25% of biochar), and granulating using a rotating granulator. | Total P was 15.4–19.9% | Total P release within 1.5 h was 82% and 36% for blended biochar and coated biochar. | [ |
| Biochar-based N/P fertilizer | Impregnation | The impregnation was done with an NPK fertilizer: oil palm kernel shell biochar was mixed NH4NO3 and KH2PO4 for 21 h at room temperature and then oven-dried at 105 °C until constant weight. | – | NO3− release was 52.9%, 77.4% for NH3 and 55.2% for PO43- after 1 h. | [ |
| Carbon-based SRF treated by biooil coating | Granulation Encapsulation | The dried wheat straw was pyrolyzed at 400 °C for 2 h under CO2, N2 and H2O(g) atmosphere of to prepare the initial biochar. The biochar and KH2PO4 and KNO3 solution were mixed with a ratio of 2.7. After stirring and mixing, the mixture was maintained for 24 h, and then heated at a low temperature to remove the solution. The biochar was placed on the porous bottom plate of the fluidized spraying device, and the biochar particles were uniformly coated with a layer of bio-oil film, and then a desiccant was added and dried to obtain the coated carbon-based slow-release fertilizer. | – | the cumulative release of N, P, and K reached about 45% after 7 d. | [ |
| Biochar/struvite composites as N and P fertilizer | Impregnation | A 1:1:1 M ratio of Mg2+/PO43−/NH4+ was stirred for 30 min and mixed with 10% biochar. After stirring for 30 min and aging for 24 h at room temperature, it was filtered, washed, and dried at 100 °C to obtain biochar/struvite composites. | N 4.93% and P2O5 22.19% | The accumulative release of N and P after 84 d was 10.62% and 6.84% in distilled water, and 59.32% and 59.12% in citric acid solution. | [ |
| P-enriched biochar fertilizer | In-situ pyrolysis | P content 84.7 mg g−1 | The extractable P in water and citric acid reached 52% and 61% after 5 d | [ | |
| Blended biochar pellet | Granulation | Biochar from rice hull was produced from a pyrolysis system at 400–500 °C for 4 h under O-free atmosphere. Biochar was blended with pig manure compost as a binder, mixed using an agitator for 5 min, sprayed with deionized water for 10 min, and then pelletized through the pellet machine. | – | Total water-soluble accumulative NH4+-N and PO43--P were 13.8 mg g−1 and 44.6 mg g−1 after 84 d | [ |
| Biochar-based SRF encapsulated by waterborne copolymers | Encapsulation | Maize straw, rice straw and forest litter were dried, ground, and then heated at 500 °C for 2 h in the muffle furnace. Distilled water and PVA were mixed and was slowly raised to 90 °C with continuously stirring, and then PVP and butanol were added and continuously stirred for 2 h at 60 °C. Then, biochar was added and mixed for 1 h at 60 °C to prepare biochar-based copolymer film. Urea were in a sugar-coating machine for 0.5 h. Using a side-spray nozzle under 0.7 MPa pressure, the urea preheated granules were coated with the mixture solution of biochar and copolymer for 0.5 h. | – | Accumulative nitrogen leaching was 65.28% after 22 d. | [ |
| Biochar-based P SRF | Co-Pyrolysis | The biomass (pine tree sawdust and switchgrass) and fertilizer (TSP and BM) were completely mixed, and pyrolyzed at 500 °C for 2 h under N2. | P content was 4.82–5.82%. | P release from TSP- and BM-composite biochar within 120 h were about 20.0 mg g−1 and 0.30 mg g−1 | [ |
| Biochar pellets embedded with fertilizers | Granulation | Air-dried switchgrass was pyrolyzed at 525 °C for 90 s under N2 using a continuous dual auger pyrolysis process. The biochar was blended with different percentages of lignin as a binder using a mixer, and liquid fertilizer (12:4:8 = N:P2O5:K2O) was added. The biochar mixtures were pelletized using a pellet mill. The pelletized biochar was then processed at 105 or 180 °C for 24 h to dry in the oven. | K content 2.85–8.62 mg g−1, and P content 0.72–2.25 mg g−1 | K and P release was 53–62% and 49–62% within 24 h, and 78–87% and 73–78% after 18 d. | [ |
Fig. 3a. Schematic of BSRFs synthesis via co-pyrolysis; b. microwave-assisted heating behavior; c. SEM image, and d. EDX analysis; e-g. XPS P 2p spectra; h. FTIR spectra; i. XRD spectra; j. P leaching loss and the utilization efficiency. Reprinted (adapted) with permission from [66]. Copyright 2020 American Chemical Society.
Fig. 4a. Schematic of CSRFs preparation via integrating co-pyrolysis and encapsulation; b., d. SEM images; c. AFM image; e., f. TEM images; g. elemental mapping of P; h. degradation behavior of BSRFs and CSRFs; i. fresh weight and dry weight of plant, and j. P leaching loss and utilization efficiency. Reprinted (adapted) with permission from [125]. Copyright 2021 Elsevier.
Fig. 5a. Schematic of the synthesis of urea-infused biochar; b. FTIR of the slow-release fertilizers; c. XRD patterns of slow-release fertilizers prepared from H3PO4 activated biochar; d. SEM image of slow-release fertilizer; e. urea release, f. NH4+-N availability, and g. cumulative N leaching. Reprinted (adapted) with permission from [70]. Copyright 2021 American Chemical Society.
Fig. 6a. Schematic of the synthesis of biofilm coated biochar-based SRFs; b. SEM images; c. P leaching, d. cumulative P release loss; e. fresh weight, f. dry weight, and g. pictures of maize growth. Reprinted (adapted) with permission from [71]. Copyright 2021 Elsevier.
Fig. 7The advantages and disadvantages of method for fabricating biochar-based SRFs.
Fig. 8a. Phosphate adsorption on various biochar materials. Adapted with permission from [135]. Copyright 2018 Elsevier. b. Schematic of nutrient attachment onto biochar-based SRFs. Adapted with permission from [50]. Copyright 2021 Elsevier.