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Ammoniacal Nitrogen Stripping From Landfill Leachate at Open Horizontal Flow Reactors
Summary
Ammonia nitrogen stripping in open horizontal flow reactors effectively removed over 99% of ammonia from landfill leachate. This cost-effective method requires no chemical additives and is ideal for warm climates with ample space.
Area of Science:
- Environmental Engineering
- Water Treatment Technologies
- Waste Management
Background:
- Landfill leachate poses environmental challenges due to high ammonia nitrogen concentrations.
- Conventional ammonia removal methods can be costly or energy-intensive.
- Open horizontal flow reactors offer a potential low-cost alternative for ammonia stripping.
Purpose of the Study:
- To evaluate the efficacy of ammonia nitrogen stripping using open horizontal flow reactors.
- To assess the process's performance in reducing ammonia and chemical oxygen demand (COD) in landfill leachate.
- To determine the influence of superficial loading rates on removal efficiencies.
Main Methods:
- Experimental setup with four open horizontal flow reactors fed with raw landfill leachate.
- Application of varying superficial loads: 650 kgN/ha/day (Phase 1), 750 kgN/ha/day (Phase 2), and 850 kgN/ha/day (Phase 3).
- Monitoring of ammonia nitrogen and total COD concentrations with corresponding hydraulic retention times.
Main Results:
- Ammonia nitrogen removal efficiencies consistently exceeded 99% across all phases (99.0% to 99.5%).
- COD removal efficiency decreased with increasing superficial load, from 69.20% (Phase 1) to 29.23% (Phase 3).
- Ammonia removal efficiency demonstrated a direct proportionality to the applied superficial load.
Conclusions:
- Open horizontal flow reactors are a highly effective and promising technology for ammonia nitrogen reduction in landfill leachate.
- The process is economically viable due to the absence of chemical reagent costs and electricity requirements.
- Optimal performance is expected in regions with sufficient land availability and ambient temperatures above 25°C.
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