New Optimization Framework for Improvement Sustainability of Wastewater Treatment Plants
Abstract
:1. Introduction
2. Materials and Methods
2.1. Overview of the Framework
2.2. Basic Definition and Information Collection
2.2.1. Alternative Technologies Identification
2.2.2. Sustainability Objectives Determination
2.2.3. Information Collection and Treatment
2.3. Model Formulation and Solver Optimization
2.3.1. Weights Assignment
Subjective Weights–Interval SWARA II
Objective Weights–Interval CRITIC
Combined Weights–Minimize Deviation
2.3.2. Multi-Objective Aggregation
2.3.3. Optimal Configuration Generation
3. Case Study and Results
3.1. Basic Definition and Information Collection in the Case Study
3.1.1. Ten Alternative Technologies
3.1.2. Three Sustainability Objectives
3.1.3. Information Collection and Treatment in the Case Study
3.2. Model Formulation and Solver Optimization in the Case Study
3.2.1. Weight Assignment in the Case Study
3.2.2. Multi-Objective Aggregation in the Case Study
3.2.3. Optimal Configuration Generation in the Case Study
4. Discussion
4.1. Effect of the Weighting Result
4.2. Weighted MOO Techniques Comparison
5. Conclusions
Supplementary Materials
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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Linguistic Variables | Preference Values |
---|---|
Extreme low (EL) | 1 |
Very low (VL) | 2 |
Low (L) | 3 |
Medium low (ML) | 4 |
Medium (M) | 5 |
Medium high (MH) | 6 |
High (H) | 7 |
Very high (VH) | 8 |
Extreme high (EH) | 9 |
Pollutant | Influent Concentration (mg/L) | Effluent Concentration (mg/L) | Removal Rate (%) |
---|---|---|---|
BOD5 | 220 | ≤10 | ≥95.45 |
COD | 400 | ≤50 | ≥87.50 |
SS | 280 | ≤10 | ≥96.43 |
NH3-N | 34 | ≤8 | ≥76.47 |
TN | 50 | ≤15 | ≥70 |
TP | 5 | ≤1 | ≥80 |
Technology | Brief Introduction |
---|---|
T1: Advanced aeration system (AAS) [47] | This is an effective wastewater aeration system with small air bubbles that improve biological degradation. The fine bubbles from APAS, having a larger surface area, enhance oxygen transfer. It allows accurate air flow control according to tank needs, ensuring optimal oxygen levels. This results in higher TN removal rates and lower energy usage. |
T2: Precision dosing system (PDS) [48] | This refers to the precise delivery of treatment chemicals to the wastewater treatment process by controlling the design and operational parameters of the dosing system. By utilizing feed-forward control systems, PDS employs online analyzers in the inlet stream to provide real-time data to a dosing control system. This enables automatic adjustments of the dosing amount and timing to achieve optimal wastewater treatment results. |
T3: Advanced automatic sludge control system (ASC) [49] | This utilizes advanced automation control systems to effectively monitor and regulate the sludge removal system in real-time. By incorporating parameters such as sludge flow, quality, and moisture content, the sludge removal equipment can be automatically adjusted, ensuring precise sludge discharge and treatment. Moreover, through sludge analysis and data management, the design and operation of the sludge removal system can be optimized, leading to enhanced sludge treatment efficiency and sustainability. |
T4: External carbon source (ECS) [50] | ECS can enhance the treatment efficiency of the wastewater treatment process, especially in situations where the incoming wastewater has low organic matter concentrations or when nitrogen and phosphorus removal is necessary. This retrofitting technique involves careful control of the type and quantity of external carbon source added to prevent the overgrowth of microorganisms and the consequent production of excess sludge. |
T5: Fluidized carriers supplementary (FCS) [51] | This system with fluidized carriers supplemented into the aerobic tank in the existing AAO system could improve nitrogen removal ability, primarily because of the higher relative abundance of nitrifying bacteria and denitrifying bacterial genera attached onto the biofilm formed on the carrier. |
T6: Moving bed biofilm reactor (MBBR) [52] | Integrating an MBBR reactor into the existing wastewater treatment system can enhance treatment efficiency and improve water quality. MBBR offers several advantages, including high biomass concentrations, the ability to achieve high SRTs with relatively low HRTs, good resilience to shocks from organic loading, minimal sludge bulking issues, and low risks of carrier media clogging. |
T7: Anaerobic digestion of sludge (AD) [53] | AD stabilizes sludge by converting volatile solids into biogas in the absence of air, requiring additional processing to recover and utilize the methane content of the biogas. AD offers advantages such as energy production, reduced sludge volume and disposal costs, and environmental benefits through reduced greenhouse gas emissions. It is a cost-effective and sustainable method for sludge management with resource utilization and minimal environmental impact. |
T8: Solar convective drying (SCD) [54] | Sludge dewatering and drying are crucial processes in WWTPs for effective sludge management. While sludge treatment can be expensive, drying the sludge reduces its mass and volume, benefiting the environment, economy, and society. This innovative retrofit technology utilizes solar convective drying to replace conventional dewatering machines, resulting in significant energy savings and reduced volume of treated sludge. |
T9: Heat pump drying (HPD) [55] | This is another energy-saving technology for drying sludge. This process involves a heat pump absorbing sensible and latent heat from the medium-temperature, high-humidity air leaving the drying chamber. As the air releases moisture, it is reheated and transferred to the sludge, causing internal moisture to migrate to the surface, evaporate into the drying medium, and effectively separate from the sludge, accomplishing the drying objective. |
T10: Hydropower utilization (HPU) [56] | The case study presents an excellent opportunity for installing a mini hydropower system due to the significant 35 m drop in water discharge. Consequently, harnessing the energy generated by flowing water can power the investigated WWTP, reducing the dependence on external sources of electricity. |
O1 | O2 | O3 | Budget Limit (BL, 106 CNY) | Construction Duration (CD, Day) | |
---|---|---|---|---|---|
T1 | [1.7%, 3.3%] | [2.2%, 4.3%] | [6.8%, 13.7%] | 1.2 | 20 |
T2 | [6.7%, 13.3%] | [0.5%, 0.6%] | [3.6%, 3.6%] | 0.5 | 10 |
T3 | [5.0%, 13.3%] | [2.0%, 3.4%] | [3.6%, 3.8%] | 1.0 | 15 |
T4 | [10.0%, 20.0%] | [−6.1%, −5.6%] | [−1.8%, −1.8%] | 0.3 | 15 |
T5 | [10.0%, 20.0%] | [−1.7%, −0.4%] | [−12.3%, −8.2%] | 4.4 | 30 |
T6 | [13.3%, 16.7%] | [−0.4%, 0.2%] | [−4.1%, −2.1%] | 2.8 | 30 |
T7 | [0.0%, 0.0%] | [13.2%, 14.3%] | [10.4%, 13.9%] | 5.2 | 20 |
T8 | [0.0%, 0.0%] | [21.1%, 28.5%] | [0.0%, 0.0%] | 3.6 | 15 |
T9 | [0.0%, 0.0%] | [15.1%, 15.1%] | [−9.7%, −9.7%] | 2.4 | 20 |
T10 | [0.0%, 0.0%] | [2.6%, 2.6%] | [10.4%, 10.4%] | 2.0 | 10 |
Objective | Order | Preference | Subjective Weight |
---|---|---|---|
O2 | 1 | [6, 7] | [0.458, 0.490] |
O3 | 2 | [8, 9] | [0.323, 0.343] |
O1 | 3 | - | [0.182, 0.205] |
O1 | [0.241, 0.416] | [0.768, 1.347] | [0.311, 0.546] |
O2 | [0.236, 0.277] | [0.623, 0.755] | [0.257, 0.307] |
O3 | [0.283, 0.303] | [0.674, 0.747] | [0.274, 0.303] |
Objective | Improvement Degree | Configuration | Cost | Construction Time |
---|---|---|---|---|
T1 + T2 + T3 + T4 + T5 | 7.4 | 90 | ||
T1 + T7 + T8 | 10.0 | 55 | ||
T1 + T2 + T3 + T7 + T10 | 9.9 | 75 |
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Li, H.; Pang, F.; Xu, D.; Dong, L. New Optimization Framework for Improvement Sustainability of Wastewater Treatment Plants. Processes 2023, 11, 3156. https://doi.org/10.3390/pr11113156
Li H, Pang F, Xu D, Dong L. New Optimization Framework for Improvement Sustainability of Wastewater Treatment Plants. Processes. 2023; 11(11):3156. https://doi.org/10.3390/pr11113156
Chicago/Turabian StyleLi, Hang, Fei Pang, Di Xu, and Lichun Dong. 2023. "New Optimization Framework for Improvement Sustainability of Wastewater Treatment Plants" Processes 11, no. 11: 3156. https://doi.org/10.3390/pr11113156
APA StyleLi, H., Pang, F., Xu, D., & Dong, L. (2023). New Optimization Framework for Improvement Sustainability of Wastewater Treatment Plants. Processes, 11(11), 3156. https://doi.org/10.3390/pr11113156