Nitrogen Removal Using Ferrous Ferric Sulfate Mixture
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Solution Overview
Problem
Current methods for nitrogen removal from aqueous solutions, such as CANDO, require additional steps and materials like carbonate green rust, which can be costly and complex, and there is a need for more efficient alternatives.
Innovation Solution
A method using a mixture of ferrous sulfate and ferric sulfate to reduce NO2− to N2O, eliminating the need for carbonate sources and simplifying the process by directly adding the sulfate mixture to the reaction, enhancing the Fe(II)-mediated reduction and optimizing the conversion of NH4+ to N2, with real-time spectrophotometric measurement for precise reduction agent addition.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Productivity
If carbonate green rust or siderite is used for reduction of NO2− to N2O, then the reduction efficiency is maintained, but the process complexity and cost increase due to additional steps for producing green rust and adding carbonate sources
Solution Approach 1:
The invention extracts and eliminates the unnecessary carbonate green rust production step and carbonate source addition from the CANDO process. By using a simplified Fe(II) salt system instead of requiring green rust synthesis, the patent removes complex preparatory steps while maintaining the core reduction function, thus reducing process complexity without sacrificing nitrogen removal efficiency
Solution Approach 2:
The patent replaces the expensive and complex carbonate green rust with inexpensive, readily available Fe(II) salts that can be directly added to the system. These simple iron salts serve the same functional purpose of providing Fe(II) for nitrite reduction but are much cheaper and easier to handle, eliminating the need for complex green rust synthesis and stabilization
2Reliability
If carbonate green rust is used for reduction of NO2− to N2O, then the reduction function is achieved, but the number of process steps increases
Solution Approach 1:
The invention merges the reduction function directly into the existing CANDO process by adding Fe(II) salts in the anoxic zone, eliminating the need for separate green rust production and addition steps. This integration maintains the reduction function while reducing the number of discrete process steps, making the overall nitrogen removal process more efficient and easier to operate
3Productivity
If more iron is added to enhance N2O release and ammonia removal, then the nitrogen removal efficiency increases, but the amount of substance added increases
Solution Approach 1:
The patent optimizes the Fe(II) to Fe(III) ratio and the total iron dosage to achieve maximum nitrogen removal efficiency. By carefully controlling these parameters, the system achieves high productivity without requiring excessive amounts of iron salts, thus balancing effectiveness with material consumption
Applied Scientific Principles
This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.
Function Achieved in This Case
This method effectively reduces nitrogen levels in wastewaters with improved efficiency and reaction rates, minimizing steps and costs, while maintaining energy recovery and ammonia removal, even in wastewaters with high nitrogen concentrations, and allows for precise control of reduction agents.
Implementation Method 1
a mixture of ferrous sulfate and ferric sulfate is used for reduction of NO2− to N2O
Implementation Method 2
The addition of the mixture of ferrous sulfate and ferric sulfate directly to step (b) produces fresh amorphous iron oxyhydroxide
Implementation Method 3
converting NH4+ in the aqueous medium to NO2− by partial aerobic nitrification
Implementation Method 4
partially reducing the obtained NO2− to N2O in anoxic conditions
Implementation Method 5
N2O conversion to N2 with energy recovery via catalytic decomposition of N2O
Data Source
AI summary
The invention relates to a method for nitrogen removal from aqueous medium, comprising steps of (a) converting NH4+ in the aqueous medium to NO2− by partial aerobic nitrification, (b) partially reducing the obtained NO2− to N2O in anoxic conditions, and (c) decomposing N2O to N2 with energy recovery. A mixture of ferrous sulfate and ferric sulfate is used in step (b) for reduction of NO2− to N2O.