The Experience and Development of the Treatment Technology of Municipal Solid Waste Leachate in China
Abstract
:1. Introduction
2. Leachate Characteristics and Their Influencing Factors
2.1. Landfill Leachate Characteristics and Their Influencing Factors
- (1)
- Differences in management regulations lead to differences in original landfill materials. During the earlier years, Europe and the United States moderated the organic matter content of materials entering landfills, and the landfill materials were mainly inorganic substances, while the landfill materials in China included much of the original waste [16]. Colombia and India have not yet carried out waste classification, and Colombian landfills continued to add new waste to the landfills, resulting in high concentrations of CODCr and BOD5 and poor biochemical properties.
- (2)
- Due to different dietary habits, the content of food waste in Chinese municipal solid waste was much higher than that in the United States, Japan, and Europe. Therefore, the concentrations of CODCr and BOD5 in Chinese late-stage landfill leachate were higher than those in the United States, Japan, and Europe
- (3)
- In terms of the scale of landfills, municipal solid waste landfills in China, especially in first-tier cities, had a much larger daily landfill scale and landfill storage capacity than similar landfills in the United States, Japan, and Europe. The anaerobic environment was more thorough, and oxygenated air struggled to enter the landfill; hence, the concentrations of CODCr and BOD5 were higher in China.
2.2. Characteristics and Influencing Factors of Leachate in Incineration Power Plants and Transfer Stations
2.3. Characteristics and Influencing Factors of Anaerobic Digested Slurry of Food Waste
2.4. Comparison of Three Kinds of Leachate Characteristics
3. Development History of the Leachate Treatment Process
3.1. The First Stage: Simple Biological Treatment during Early 1990s
3.2. The Second Stage: Ammonia Stripping + Anaerobic + Aerobic Treatment during the Mid to Late 1990s
3.3. The Third Stage: Two-Stage Disc Tube Reverse Osmosis (DT-RO) Process from 2000 to 2008
3.4. The Fourth Stage: Anaerobic + Aerobic + Advanced Treatment Process from 2008 to 2015
- (1)
- The operating cost is high. The external MBR system used in the traditional process system consumes a large amount of electricity [30], and the operating cost is high [31]. In addition, due to the imbalance of the C/N ratio in the aged landfill, a large amount of the carbon source needs to be supplemented, resulting in a higher operating cost.
- (2)
- To ensure that the final treated effluent satisfies the standard requirements, the advanced treatment adopts the NF + RO process [32]. The membrane treatment process inevitably produces a large amount of intractable concentrate. At present, the material of NF concentrate through the material membrane can be solved by ozone catalytic oxidation or other processes, but the operation cost is relatively high. For RO concentrate, there is no mature and stable treatment process in China, and the concentrate produced by the reverse osmosis system contains a large amount of salt. The untreated concentrate is directly returned to the leachate treatment system, which will reduce the activity of microorganisms. This operation leads to serious membrane fouling and accelerates the frequency of membrane cleaning. Therefore, the life of the membrane is reduced [33]. If the untreated concentrate is directly sprayed back to the landfill stack, the salt will accumulate in the landfill. This technology significantly affects the normal operation of the landfill leachate treatment system. Therefore, the concentrate produced by the membrane system must be treated.
- (3)
- The problem of concentrate caused by membrane treatment technology has gradually attracted increasing attention. Enterprises and universities have begun to focus on the development of advanced oxidation and evaporation treatment technology. Evaporation processes include MVR and immersion combustion. The evaporation process also has a series of problems, such as high energy consumption and scaling difficulties when cleaning, and the stability and reliability of operation need to be further verified.
3.5. The Fifth Stage: Diversified and Full Quantitative Process since 2015
3.6. Economic Analysis of Treatment Technologies
4. Future Development Trends
4.1. Increased Scientific Emission Standards and Tendency of Promulgating Local Standards
4.2. Inevitable Green Development of Processing Technology Route
4.3. Increased Professional and Intelligent Construction and Operation
4.4. Stricter Supervision and Management
4.5. Trends in Technology
Number | Reference | Treatment Technology | Classification |
---|---|---|---|
1 | [48] | Membrane | Physical |
2 | [49] | Adsorption | Physical |
3 | [50] | Membrane | Physical |
4 | [51] | Nanofiltration | Physical |
5 | [52] | Adsorption | Physical |
6 | [53] | Membrane | Physical |
7 | [54] | Advanced oxidation | Chemical |
8 | [55] | Fenton based advanced oxidation | Chemical |
9 | [56] | Advanced oxidation | Chemical |
10 | [57] | Photocatalytic | Chemical |
11 | [58] | Electrocatalytic ozonation | Chemical |
12 | [59] | Simultaneous ammonium oxidation denitrifying | Biological |
13 | [60] | Advanced oxidation + Denitrification | Biological + Chemical |
14 | [61] | Ozonization + microalgae | Biological + Chemical |
15 | [62] | Electrocoagulation | Physical + Chemical |
16 | [63] | Advanced oxidation +adsorption | Physical + Chemical |
17 | [64] | Ion exchange+ supercritical water oxidation | Physical + Chemical |
18 | [65] | Ozone direct oxidation + Catalytic oxidation + Membrane | Physical + Chemical |
19 | [66] | Coagulation–flocculation | Physical + Chemical |
20 | [67] | Coagulation + advanced oxidation | Physical + Chemical |
5. Conclusions
- (1)
- The characteristics of the leachate are related to the production mechanism, fermentation cycle, and waste composition. With the increase in landfill years, the concentration of ammonia nitrogen in the landfill leachate increases, the biodegradability decreases, and the C/N is out of balance, resulting in leachate being more difficult to treat. Compared with other countries, although the quality of landfill leachate was similar in the middle and late stages, the concentration of pollutants in the late stage leachate in China was higher, which was attributed to the differences in eating habits, landfill size, and treatment methods.
- (2)
- The leachate treatment process mainly went through five stages. The treatment process and the emission standards have been continuously improving. In recent years, due to the improvement of environmental protection standards and national environmental protection policies, the treatment process of landfill leachate was mainly “secondary A/O + ultrafiltration + nanofiltration (NF) + reverse osmosis (RO)” or “pretreatment + secondary A/O + MBR + Fenton Advanced Oxidation + BAF”.
- (3)
- The future development of the landfill leachate treatment industry and the entire environmental protection industry need to meet the requirements of the Chinese social economy and urban development. Under the background of the global “dual carbon“ strategy, the green ecology of the technical route is represented by new high-efficiency denitrification, new advanced catalytic oxidation, evaporation, and other fully quantitative process technologies.
Author Contributions
Funding
Conflicts of Interest
References
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City Name | Sampling Time | pH | CODCr 1 (mg/L) | BOD5 2 (mg/L) | BOD5/CODCr | NH3-N (mg/L) | Salt Content (mg/L) |
---|---|---|---|---|---|---|---|
Hangzhou | 2007 (early stage) | 6.29 | 13,200 | 5940 | 0.45 | 580 | 8960 |
2015 (mid-term) | 7.13 | 7650 | 1950 | 0.25 | 1890 | 9780 | |
2021 (late stage) | 7.82 | 3840 | 350 | 0.09 | 2380 | 10,120 | |
Tianjin | 2010 (early stage) | 6.08 | 23,680 | 11,300 | 0.48 | 1175 | 13,150 |
2015 (mid-term interim) | 6.76 | 11,100 | 3230 | 0.29 | 1425 | 14,900 | |
2021 (late stage) | 7.49 | 6600 | 1280 | 0.19 | 1840 | 13,700 |
Country | pH | CODCr (mg/L) | BOD5 (mg/L) | BOD5/CODCr | NH3-N (mg/L) | Salt Content (mg/L) | Age | References |
---|---|---|---|---|---|---|---|---|
China | 7.5–9.0 | 500–6000 | 100–550 | 0.01–0.1 | 100–4500 | 2000–12,000 | 15 | |
USA | - | 100–350 | - | - | 30–55 (TN 1) | - | >13 | [11] |
Japan | - | 300 | 20 | 0.07 | 500 | - | 16 | [12] |
Belgium | 8.2–8.8 | 645–1230 | 78–213 | 0.12–0.17 | 255–648 | 9.1–11.2 (EC 2) | 30 | [13] |
Columbia | 7.94–9.3 | 23,000–35,000 | 2700–4000 | 0.11–0.12 | - | - | >10 | [14] |
India | 7.3–9.3 | 72–5100 | 3–207 | 0.04 | - | - | 16 | [15] |
Classification | pH | CODCr (mg/L) | BOD5 (mg/L) | BOD5/CODCr | NH3-N (mg/L) | Salt Content (mg/L) |
---|---|---|---|---|---|---|
Incineration plant | 6–7 | 60,000–80,000 | 25,000–35,000 | 0.45–0.5 | 1500–2500 | 8000–12,000 |
Classification | pH | CODCr (mg/L) | BOD5 (mg/L) | BOD5/CODCr | NH3-N (mg/L) | Salt Content (mg/L) |
---|---|---|---|---|---|---|
Anaerobic digested slurry | 6–9 | 8000–15,000 | 4000–7000 | - | 2000–3000 | 10,000–20,000 |
Classification | pH | CODCr (mg/L) | BOD5 (mg/L) | NH3-N (mg/L) | Salt Content (mg/L) | |
---|---|---|---|---|---|---|
Landfill | early | 6.0–6.5 | 10,000–25,000 | 1200–12,000 | 100–1200 | 2000–14,000 |
middle | 6.5–7.5 | 6000–12,000 | 1500–4000 | 1000–2000 | 6000–15,000 | |
late | 7.5–9.0 | 500–7000 | 100–1500 | 100–3000 | 2000–14,000 | |
Incineration plant or transfer station | 6.0–7.0 | 60,000–80,000 | 25,000–35,000 | 1500–2500 | 8000–12,000 | |
Food waste digestion plant | 6.0–9.0 | 8000–15,000 | 4000–7000 | 2000–3000 | 10,000–20,000 |
Stage | Main Treatment Process | Water Sample | pH | CODCr (mg/L) | BOD5 (mg/L) | NH3-N (mg/L) | SS 1 (mg/L) | Cost 3 (CNY/m3) | Typical Case |
---|---|---|---|---|---|---|---|---|---|
1st | hypoxic tank + sedimentation tank + aerobic tank + sedimentation tank | Influent | 6–9 | 6000 | 3000 | - 2 | - | - | Hangzhou Tianziling Landfill |
Effluent | 6–9 | 300 | 60 | - | 100 | ||||
2nd | ammonia stripping + anaerobic biological filter + SBR reaction tank | Influent | 5.6–7.5 | 3000– 13,000 | 1000–26,000 | 400– 1500 | - | 4–5 | Shenzhen Xiaping Landfill |
Effluent | 6–9 | 500 | 300 | - | - | ||||
3rd | two-stage disc tube reverse osmosis (DT-RO) process | Influent | 6–9 | 6000– 8000 | 3000–4000 | 1500– 3000 | - | 12–15 | Chongqing Changshengqiao Landfill |
Effluent | - | 100 | 30 | 15 | - | ||||
4th | IC anaerobic reactor + two-stage A/O + ultrafiltration + nanofiltration (NF) + reverse osmosis (RO) | Influent | 6.5–7.5 | 75,000 | 30,000 | 2000 | 10,000 | 30–40 | Xuzhou No. 2 Incineration Plant |
Effluent | 6.5–8.5 | 60 | 10 | 10 | 180 | ||||
5th | pretreatment + two-stage A/O + MBR + Fenton advanced oxidation + BAF | Influent | 7.5–8.5 | 15,000– 18,000 | 6000–8000 | 2800– 3000 | 2000– 2500 | 40–75 | Hefei Xiaomiao Food Waste Resource Center |
Effluent | 6.0–8.0 | 300 | 150 | 35 | 200 |
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Song, X.; Min, H.; Zhao, L.; Fu, Q.; Zheng, W.; Wang, X.; Ding, X.; Liu, L.; Ji, M. The Experience and Development of the Treatment Technology of Municipal Solid Waste Leachate in China. Water 2022, 14, 2458. https://doi.org/10.3390/w14162458
Song X, Min H, Zhao L, Fu Q, Zheng W, Wang X, Ding X, Liu L, Ji M. The Experience and Development of the Treatment Technology of Municipal Solid Waste Leachate in China. Water. 2022; 14(16):2458. https://doi.org/10.3390/w14162458
Chicago/Turabian StyleSong, Xinxin, Haihua Min, Lejun Zhao, Qingming Fu, Wei Zheng, Xingjian Wang, Ximing Ding, Lingjie Liu, and Min Ji. 2022. "The Experience and Development of the Treatment Technology of Municipal Solid Waste Leachate in China" Water 14, no. 16: 2458. https://doi.org/10.3390/w14162458
APA StyleSong, X., Min, H., Zhao, L., Fu, Q., Zheng, W., Wang, X., Ding, X., Liu, L., & Ji, M. (2022). The Experience and Development of the Treatment Technology of Municipal Solid Waste Leachate in China. Water, 14(16), 2458. https://doi.org/10.3390/w14162458