Submitted:
26 February 2024
Posted:
27 February 2024
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Abstract
Keywords:
1. Introduction
2. Literature Review
| Techniques | SO2 (%) | NO2 (%) | Mercury(%) | PM(%) | Cost($) | Applicability |
|---|---|---|---|---|---|---|
| Advanced dry scrubber | 90-95 | - | 0-90 | - | 50-150/Kw | Pilot to commercial scale; depending on type of coal |
| Activated carbon injection with ESAP | - | - | 50-90 | 99 | ACI:3-8/Kw | Pilot scale, retrofit and new plants with Fabric filter (FF) and ESP |
| Combined Hg and SO2 sorbents | 40-85 | - | Upto 90 | - | 30-60/Kw | Pilot scale, integrated with ESP or FF unit |
| WFGD with mercury oxidation process | 95 | - | >80 | 90 for >10µm (up to 39.6% for PM2.5) | 160-275/Kw | Pilot scale testing |
| Wet scrubbers with WESP | 99 | - | 80 | 90-99 | WESP:10-20/Kw | Commercial level; integrated with already installed wet scrubbers |
| Activated coke | 90-98 | 15-80 | 90-99 | 80-85 | 150-200Kw | New plants and retrofits |
| SCR with WFGD | 95 | 90-95 | 40-90 | 90 for >10µm (up to 39.6% for PM2.5) | SCR:50-40/Kw Wet.FGD:160-275/KW (for 400 MW) | Commercial level |
| Electrocatalytic oxidation | 98 | 90 | 90 | 86 | 200/Kw for 500 MW | Demonstration level; new plants and retrofits |
| Name of radical | Efficiency of SO2 removal (%) | Efficiency of NOx removal (%) | Efficiency of Hg0 removal (%) |
|---|---|---|---|
| Hydroxyl radical | 99-100 | 75-100 | 75-98 |
| Sulphate radical | 9-100 | 72-100 | 85-99 |
| Chlorine radical8 | 99-100 | 77-98 | 90-95 |
| Ozone | 97-100 | 91-97 | 82-91 |
- Traffic system improvement
- Urban planning efficiency improvement
4. Discussion
5. Conclusions
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
References
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