From Waste to Resource: Evaluating the Impact of Biosolid-Derived Biochar on Agriculture and the Environment
Abstract
:1. Introduction
- Explore BDB production: Detail the processes involved in converting biosolids into biochar, including pretreatment and pyrolysis techniques.
- Evaluate agricultural and environmental benefits: Investigate the potential of BDB to enhance soil properties, improve water and nutrient retention, increase crop yields, and mitigate GHG emissions through a review of recent studies.
- Identify challenges and future directions: Discuss the barriers to widespread adoption of BDB in agriculture, including social acceptance, the presence of contaminants, and regulatory issues, and propose future research and policy directions to address these challenges and promote sustainable practices.
2. Production of Biochar from Biosolids
2.1. Pretreatment of Biosolids
2.1.1. Dewatering Process
- Centrifugation: Centrifugation is a widely used method for dewatering biosolids, particularly in large-scale wastewater treatment plants [11]. This technique employs centrifugal force to separate water from solid particles. The biosolids are placed in a rotating drum or bowl, which spins at high speeds. The centrifugal force pushes the heavier solid particles outward against the drum wall, while the water moves inward and is removed through a central outlet [11].
- Filter presses: Filter presses use mechanical pressure to dewater biosolids by compressing them between filter plates [12]. This method involves pumping the biosolid slurry into the press, where it is forced between cloth filters under high pressure. The water is squeezed out through the filter cloth, leaving behind a cake of dewatered biosolids [12].
- Electro-dewatering: Electro-dewatering is an advanced method that enhances traditional dewatering techniques by applying an electric field [13]. This process involves placing biosolids between electrodes and applying a direct current. The electric field induces the movement of water towards the electrodes, enhancing the dewatering efficiency [13].
2.1.2. Drying Process
2.1.3. Integration and Optimization of Dewatering and Drying
2.2. Pyrolysis of Biosolids
2.2.1. Slow Pyrolysis
2.2.2. Fast Pyrolysis
2.2.3. Flash Pyrolysis
3. Effects of Biosolid-Derived Biochar Applications
3.1. Enhanced Water Holding with the Application of Biosolid-Derived Biochar
3.1.1. Mechanisms for Enhancing Soil Water Holding Capacity
3.1.2. Empirical Evidence for Enhanced Water Holding from Previous Studies
3.2. Improved Nutrient Retention with the Application of Biosolid-Derived Biochar
3.2.1. Mechanisms for Improving Soil Nutrient Retention
3.2.2. Empirical Evidence for Improved Nutrient Retention from Previous Studies
3.3. Increased Crop Production with the Application of Biosolids-Derived Biochar
3.3.1. Mechanisms for Increasing Crop Production
3.3.2. Empirical Evidence for Increased Crop Production from Previous Studies
3.4. Mitigating Greenhouse Gas Emissions with the Application of Biosolids-Derived Biochar
3.4.1. Mechanisms for Mitigating Greenhouse Gas (GHG) Emissions
3.4.2. Empirical Evidence for Increased Crop Production from Previous Studies
4. Challenges and Future Perspectives
4.1. Social Acceptance
4.1.1. Issues and Barriers to Social Acceptance
4.1.2. Future Directions for Improving Public Acceptance
4.2. Possible Toxic Effects
4.2.1. Issues and Barriers with Possible Toxic Effects
4.2.2. Future Directions for Eliminating Possible Toxic Effects
4.3. Large-Scale Production
4.3.1. Issues and Barriers with Large-Scale Production
4.3.2. Future Directions for Launching Large-Scale Production
5. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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Centrifugation | Filter Presses | Electro-Dewatering | |
---|---|---|---|
Mechanism | Use centrifugal force to separate water from solid particles. | Use mechanical pressure to compress biosolids between filter plates. | Use a direct current to induce the movement of water towards the electrodes. |
Advantages | (1) Effective for high-throughput operations. (2) Can achieve significant reductions in water content. (3) Relatively fast. (4) Can be automated, thus suitable for continuous operation. | (1) Can achieve high levels of dewatering and achieve a relatively dry case. (2) Versatile and can handle a wide range of biosolid types. | (1) Can achieve higher dewatering rates and lower residual moisture content compared to conventional methods. (2) Particularly effective for biosolids with high initial moisture content. |
Disadvantages | (1) High initial capital costs. (2) Can consume considerable energy. (3) May not be effective for biosolids with very high moisture content. | (1) Batch-based processes can limit throughput compared to continuous methods. (2) Equipment can be bulky, requiring significant space. | (1) It is a relatively new technology and can be costly. (2) Careful control of the electric field is required for the process to prevent overheating and ensure uniform dewatering. |
Biodrying | Solar Drying | Thermal Drying | |
---|---|---|---|
Mechanism | Use heat generated from the decomposition of organic matter by microorganisms. | Use heat from solar radiation. | Use a direct current to induce the movement of water towards the electrodes. |
Advantages | (1) An environmentally friendly process. (2) Can reduce the need for external heat sources. (3) Can enhance the stabilization of biosolids by reducing pathogen levels. | (1) Can achieve high levels of dewatering and achieve a relatively dry case. (2) Versatile and can handle a wide range of biosolid types. | (1) Can achieve higher dewatering rates and lower residual moisture content compared to conventional methods. (2) Particularly effective for biosolids with high initial moisture content. |
Disadvantages | (1) A slow process that may require several weeks to achieve the desired moisture reduction. (2) Performance depends on microbial activities, which can be influenced by external factors such as temperature and aeration. | (1) Batch-based processes can limit throughput compared to continuous methods. (2) Equipment can be bulky, requiring significant space. | (1) It is a relatively new technology and can be costly. (2) Careful control of the electric field is required for the process to prevent overheating and ensure uniform dewatering. |
Slow Pyrolysis | Fast Pyrolysis | Flash Pyrolysis | |
---|---|---|---|
Temperature Range | 350–550 °C | 800–1300 °C | 500–550 °C |
Heating Rate | 0.1–1.0 °C/s | 10–200 °C/s | High heat transfer rates |
Residence Time | 5–30 min | 1–10 s | 0.5–1.0 s |
Main Product | Biochar | Bio-oil and syngas | Bio-oil |
Secondary Products | Syngas and bio-oil | Biochar | Biochar and syngas |
Biochar Yield | High | Moderate | Low |
Bio-oil Yield | Low | High | High |
Syngas Yield | Moderate | Moderate | Moderate |
Carbon Content | High | Lower than slow pyrolysis | Moderate |
Surface Area | Lower than flash pyrolysis | Lower than flash pyrolysis | High |
Porosity | Moderate | Lower than flash pyrolysis | High |
Energy Efficiency | Moderate to high | Moderate | High |
Complexity | Low to moderate | High | Very high |
Cost | Moderate | High | Very high |
Suitability | Soil amendment, carbon sequestration | Energy production, chemical feedstocks | Rapid processing, high-value products |
Advantages | (1) Produces stable biochar with a high carbon content. (2) Enhances soil fertility. (3) Increases soil cation exchange capacity. | (1) High yields of bio-oil and syngas. (2) Versatile for energy production. | (1) High-surface-area biochar. (2) Effective for rapid processing and high-value applications. |
Disadvantages | (1) Lower processing time. (2) Lower yields of bio-oil and syngas. | (1) Requires complex and costly equipment. (2) Biochar with lower stability. | (1) Very short residence time. (2) Requires highly controlled conditions. (3) Lower biochar yield. |
Origin (City/Country) | Pyrolysis Temperature (°C) | Pyrolysis Time (min) | Application Rate of Biochar (% w/w) | N Retention (% Increase) | P Retention (% Increase) | K Retention (% Increase) | Ref. |
---|---|---|---|---|---|---|---|
Brasília, Distrito Federal, Brazil | 300 | 30 | 18% | 600% | −11% | [53] | |
500 | 30 | 18% | 585% | 0.6% | |||
Beijing, China | 500 | 120 | 1% | 148% | 563% | 39% | [54] |
500 | 120 | 5% | 709% | 1567% | 114% | ||
500 | 120 | 10% | 1409% | 2150% | 198% | ||
Guangzhou, China | 700 | 180 | 1% | - | - | 23% | [55] |
Uttar Pradesh, India | 300 | 180 | - | −21% | 158,165% | [56] | |
500 | 180 | - | −80% | 17,467% | |||
600 | 180 | - | −81% | 13,599% | |||
Poland | 300 | 15 | 0.5% | - | 65% | - | [57] |
300 | 15 | 1% | - | 124% | - | ||
300 | 15 | 2% | - | 297% | - |
Origin (City/Country) | Pyrolysis Temperature (°C) | Pyrolysis Time (min) | Application Rate of Biochar (% w/w) | Crop Type | Yield Increase (%) | Duration of Experiment | Ref. |
---|---|---|---|---|---|---|---|
Brasília, Distrito Federal, Brazil | 300 | 150 | - | Corn | 58% | 5 years | [53] |
500 | 230 | - | Corn | 47% | 5 years | ||
Brasília, Distrito Federal, Brazil | 300 | 60 | - | Corn | 50% | 2 years | [58] |
500 | 75 | - | Corn | 54% | 2 years | ||
North China Plain | 700–850 | 240 | - | Peanuts | 60.43% | 2 years | [62] |
Delaware, USA | 300 | 660 | 1% | Mungbean | −31% | 3 months | [63] |
300 | 660 | 2% | Mungbean | 49% | 3 months | ||
300 | 660 | 1% | Winter Wheat | 23% | 3 months | ||
300 | 660 | 2% | Winter Wheat | 118% | 3 months | ||
300 | 660 | 1% | Spinach | 21% | 3 months | ||
300 | 660 | 2% | Spinach | 150% | 3 months |
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© 2024 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/).
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Mcintyre, H.; Li, S. From Waste to Resource: Evaluating the Impact of Biosolid-Derived Biochar on Agriculture and the Environment. Biomass 2024, 4, 809-825. https://doi.org/10.3390/biomass4030045
Mcintyre H, Li S. From Waste to Resource: Evaluating the Impact of Biosolid-Derived Biochar on Agriculture and the Environment. Biomass. 2024; 4(3):809-825. https://doi.org/10.3390/biomass4030045
Chicago/Turabian StyleMcintyre, Hailey, and Simeng Li. 2024. "From Waste to Resource: Evaluating the Impact of Biosolid-Derived Biochar on Agriculture and the Environment" Biomass 4, no. 3: 809-825. https://doi.org/10.3390/biomass4030045
APA StyleMcintyre, H., & Li, S. (2024). From Waste to Resource: Evaluating the Impact of Biosolid-Derived Biochar on Agriculture and the Environment. Biomass, 4(3), 809-825. https://doi.org/10.3390/biomass4030045