| Literature DB >> 34742971 |
Max D Gillingham1, Rachel L Gomes2, Rebecca Ferrari2, Helen M West3.
Abstract
Recent research on the magnetisation of biochar, a carbon-based material that can be used as a sorbent, has opened novel opportunities in the field of environmental remediation, as incorporating magnetic particles into biochar can simplify subsequent separation. This could offer a sustainable circular economy-based solution in two areas of waste management; firstly, pyrolysis of agricultural waste for magnetic biochar synthesis could reduce greenhouse gas emissions derived from traditional agricultural waste processing, such as landfill and incineration, while secondly, application of magnetic biochar to remove excess nitrogen from soils (made possible through magnetic separation) could provide opportunities for this pollutant to be used as a recycled fertiliser. While sorption of pollutants by magnetic biochar has been researched in wastewater, few studies have investigated magnetic biochar use in polluted soils. Nitrogen pollution (e.g. NH4+), stemming from agricultural fertiliser management, is a major environmental and economic issue that could be significantly reduced before losses from soils occur. This review demonstrates that the use of magnetic biochar tailored to NH4+ adsorption has potential to remove (and recycle for reuse) excess nitrogen from soils. Analysis of research into recovery of NH4+ by sorption/desorption, biochar magnetisation and biochar-soil interactions, suggests that this is a promising application, but a more cohesive, interdisciplinary approach is called for to elucidate its feasibility. Furthermore, research shows variable impacts of biochar upon soil chemistry and biology, such as pH and microbial diversity. Considering wide concerns surrounding global biodiversity depletion, a more comprehensive understanding of biochar-soil dynamics is required to protect and support soil ecosystems. Finally, addressing research gaps, such as optimisation and scaling-up of magnetic biochar synthesis, would benefit from systems thinking approaches, ensuring the many complex considerations across science, industry, policy and economics are connected by circular-economy principles. CrownEntities:
Keywords: Circular economy; Magnetic biochar; Nitrogen sorption; Pollution; Recycling; Remediation
Mesh:
Substances:
Year: 2021 PMID: 34742971 PMCID: PMC8811483 DOI: 10.1016/j.scitotenv.2021.151440
Source DB: PubMed Journal: Sci Total Environ ISSN: 0048-9697 Impact factor: 7.963
Fig. 1Potential options for optimal spatial targeting of magnetic biochar on farmland for removal of excess ammonium.
Fig. 2Magnetic biochar production overview with non-exhaustive examples of possible feedstocks and pyrolysis methods, and the range of ammonium sorption mechanisms that may occur. Different combinations of these variables can lead to production of vastly different magnetic biochar types, which can subsequently affect ammonium sorption mechanisms and capacity.
Fig. 3Comparison of main pyrolysis methods used in biochar production. Microwave pyrolysis can produce relatively higher yields than other methods, while requiring only a short heating duration and low energy inputs. However, other factors not shown in this simplified graphic, such as equipment costs, transport between sites, processing requirements, and influences on morphological and chemical characteristics of the products, are also important considerations.
Pyrolysis conditions of biochars produced from UK-available feedstocks through the microwave (MW) method.
| Biomass Feedstock | Biochar Yield | Application | Source | ||
|---|---|---|---|---|---|
| Biosolids | 600 W | Y | 85.5% | MW optimisation | ( |
| Cellulose | 300 W | Y | ~ 35–78% | MW optimisation | ( |
| Corn Stover | – | Y | N/A | Supercapacitors | ( |
| Corn Stover | – | N | N/A | Phosphorus Sorption | ( |
| Maple Wood | 300 W | N | N/A | Characterisation | ( |
| Municipal Solid Waste | 2000 W | N | ~ 78–83% | Yield optimisation | ( |
| Rapeseed Shell | 600 W | Y | 19.98–41.2% | MW optimisation | ( |
| Sewage Sludge | 750 W | Y | ~ 50 to 72% | MW optimisation | ( |
| Sewage Sludge | 1200 W | Y | N/A | MW optimisation | ( |
| Spent Mushroom Substrate | – | Y | 30–36% | Fertiliser | ( |
| Spruce Pellets | 2000/3000 W, 30/60/120 mins, | Y | 32.4/26.2% | Characterisation | ( |
| Straw Pellets | 1200 W | N | 33.7% | Characterisation | ( |
| Wheat Straw | 900 W | N | N/A | As(V) & Methylene blue sorption | ( |
| Willow | 300 W | N | 27.3% | MW optimisation | ( |
| Willow | 1200 W | N | 27.3% | Characterisation | ( |
| Wood Biomass | – | N | 45.2% | Gasification | ( |
Pyrolysis conditions – MW power (w), heating time (mins) and temperature (°c).
Use of microwave susceptor – yes (Y) or no (N).
Magnetisation methods for different biochars and consequential magnetic properties and applications in water.
| Method | Pre/post | Medium | Conditions | Biomass | Magnetic | Saturation | Application | Source |
|---|---|---|---|---|---|---|---|---|
| Co-precipitation | Pre | FeCl2 | pH 10, | Orange peel | Fe3O4 | N/A | Phosphate & organic removal | ( |
| Iron solution treatment | Pre | Fe(NO3)3 | Ethanol, | Pine bark | CoFe2O4 | N/A | Pb2+ & Cd2+ removal | ( |
| Iron solution Treatment | Post | FeSO4 | 30 mins, | Paper mill sludge | Fe0 | N/A | PCP removal | ( |
| Iron solution treatment | Post | Fe(acac)3 | 30 mins, | Rice hull | Fe3O4 | 13.6 emu/g | Pb2+ removal | ( |
| Co-precipitation | Post | FeCl3 | pH 10–11, | Eucalyptus | Fe3O4 | 16.0 emu/g | Cr6+ removal | ( |
| Co-precipitation | Post | FeCl3 | pH 10, | Mixed wood chips | Fe3O4 | N/A | Phenanthrene & phenol sorption | ( |
| Hematite treatment | Pre | Hematite | 120 mins, | Pine wood | ɣ-Fe2O3 | N/A | As5+ sorption | ( |
| Iron solution treatment | Pre | FeCl3 | 24 h, | ɣ-Fe2O3 | 11.6 emu/g | Cr6+ removal | ( | |
| Iron solution treatment | Pre | FeCl3 | 60 mins, | Peanut hull | ɣ-Fe2O3 | 36.79 emu/g | Cr6+ removal | ( |
| Ball milling | Post | Fe/ | Ball milled, | Nut shells | Fe3O4 | 19.0 emu/g | Carbamazepine & tetracycline sorption | ( |
| Co-precipitation | Post | FeCl2 | NaOH, | Palm kernel shell | Fe3O4 | N/A | 4-nitrotoluene removal | ( |
| Iron solution treatment | Pre | Fe3O4 | 30 °C, | Sugarcane bagasse | Fe3O4 | 6.138 emu/g | Cd2+ | ( |
| Oxidative hydrolysis | Post | FeCl2 | 90 °C | Fe3O4 | 47.8 emu/g | Sulfameth | ( | |
| Co-precipitation | Post | FeCl2 | Stirring, | Rattan | Fe3O4 | 27.11 emu/g | Properties | ( |
| Co-precipitation | Pre | FeCl3 | pH 10, | MgFe2O4 | 52.48 emu/g. | Phosphate | ( | |
| Iron solution treatment | Pre | Fe(NO3)3 | 80 °C, | Corn husk | Fe3O4 | 14.87 emu/g | Paraquat | ( |
| Co-precipitation | Post | FeCl3 | pH 10 | Cellulose | Fe3O4 | 10.7 emu/g | Plastic | ( |
| Co-precipitation | Post | FeCl3 | pH 10–11 | Rice husk | Uncharacterised | N/A | Dye sorption | ( |
| Pyrolysis of Anaerobic Digestate | Pre | None | None | Digestate from manure/food waste | Fe3O4 | N/A | Characterisation | ( |
Potential expenses to be encountered and cost-minimisation strategies in the proposed system.
| Process | Expense | Example(s) | Potential cost-minimisation strategy |
|---|---|---|---|
| Biochar production | Feedstock | Biomass | Use of low-value agricultural by-products or waste. |
| Treatment(s) | Washing, modification | Simplified ‘one-step’ modification/pyrolysis methods ( | |
| Pyrolysis | Energy, labour, quality control, equipment | Microwave pyrolysis for lower-energy inputs Agricultural co-operatives to share costs | |
| Storage/transport | Safe storage of flammable particulate matter, off-farm transport | Production and storage at/near farm to be used on. | |
| Magnetisation | Chemicals | Iron solution, NaOH | Optimisation of methodology to maximise Iron solution-to-magnetic particle conversion efficiency. |
| Processing | Stirring, shaking, heating, N2 supply, labour | ||
| MBES | Separation equipment | Purchase/hire of specially designed technology | Agricultural co-operatives to share costs. Subsidies (from e.g. government agencies) |
| Energy | Fuel for vehicle, separator rotation | Maximising time between separation runs Mechanical innovations to utilise pulling forces of vehicle. | |
| Additional processing | Washing, pollutant desorption | Recycling as many components as possible, such as desorption medium and biochar. | |
| Quality Control | Testing | Potential biochar derived pollutants e.g. Fe, PAH. | Adherence to quantified biochar standards e.g. International Biochar Initiative. Use IBI certified products. |
Surface areas and ammonium sorption by different biochars.
| Biochar | sBET Surface Area (m2 g−1) | Notes | Source | |
|---|---|---|---|---|
| Wood | 37.56 | 0.15 | CEC was dominant mechanism | ( |
| Bamboo | 330 | 0.852 | Primary mechanism – ion exchange | ( |
| Corn stover | No data | 1.1 | pH 7–7.5 was optimal | ( |
| Poultry litter | 15.43 | 1.3 | CEC was dominant mechanism | ( |
| Digested sludge | 20.86 | 1.4 | 450 °C biochar performed best | ( |
| 3.5 | 3.2 | Higher sorption attributed to zeta-potential and C/H ratio | ( | |
| Sawdust | 378.7 | 3.3 | Higher sorption attributed to zeta-potential and C/H ratio | ( |
| Rice straw | 34 | 4.1 | Higher sorption attributed to zeta-potential and C/H ratio | ( |
| Rice husk | 179 | 4.7 | Over 2× the sorption capacity of NO3 | ( |
| Mixed hardwood | No data | 5.29 | 18% of total amount removed | ( |
| Orange peel | 0.54 | 5.6 | Low temp biochar (300 °C) | ( |
| Oak sawdust | 1.57 | 10.1 | Lanthanum-modified biochar | ( |
| 7 | 13.35 | Lower sorption than of cadmium ions | ( | |
| Wheat straw | 4 | 15.5 | No NO3 adsorbed under same conditions | ( |
| 223.08 | 17.6 | Phosphate sorption also maximised | ( | |
| Sugarcane leaves | 27.9–218.9 | 22 | MgO-modified biochar. Sorption the same for all SAs. | ( |
| Corn cob | 0.051 | 22.6 | Modified by soaking in HNO3 and NaOH | ( |
| Rice husk | 11 | 71.94 | – | ( |
| Hardwood | 147 | 114.2 | Low SA chars also performed well. | ( |
| Wood | 273.6 | 133.33 | – | ( |
| Presscake | 2.5 | 136.2 | Phosphate sorption occurred, but at lower capacity | ( |
| Corn cobs | No data | 243.3 | Low-temperature biochars showed relatively fast sorption kinetics | ( |
Maximum sorption capacity as calculated by adsorption isotherm.
Fig. 4Two recycling pathways possible for reuse of magnetic biochar and ammonium after remediation of nitrogen polluted soil. ‘NH4+ loaded magnetic biochar’ refers to magnetic biochar that has been separated from soil after sorption of ammonium.
Fig. 5Typical set-ups of overband magnetic separators (left) and drum magnetic separators (right).