Simultaneous Nitrification Denitrification in Sequencing Batch Reactors

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Solution Overview

Problem

Conventional sequencing batch reactors (SBRs) require costly and energy-intensive processes to maintain distinct oxygen levels for nitrification and denitrification, with frequent ramping of air flow rates, leading to inefficiencies and high energy consumption.

Innovation Solution

Implementing a simultaneous nitrification-denitrification (SNDN) process in SBRs by maintaining an oxygen deficit condition, allowing for simultaneous nitrification and denitrification reactions at low dissolved oxygen levels, reducing the number of treatment steps and energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional SBRs maintain distinct oxygen levels for nitrification and denitrification, then treatment effectiveness is improved, but energy consumption increases

Engineering Contradiction:
Improvetreatment effectivenessVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The patent merges the traditionally separate nitrification and denitrification processes into a single simultaneous operation within the same reactor zone. By controlling dissolved oxygen at low levels (0.2-2.0 mg/L) rather than maintaining high oxygen for nitrification followed by complete oxygen removal for denitrification, the system combines both nitrogen removal processes, eliminating the need for frequent air flow ramping and reducing energy consumption while maintaining treatment effectiveness.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent changes the dissolved oxygen parameter from high levels during nitrification to controlled low levels (0.2-2.0 mg/L) that enable simultaneous nitrification and denitrification. This parameter change allows the system to operate in an aerated-anoxic mode where both processes occur concurrently, reducing the energy required for oxygen transfer while maintaining nitrogen removal efficiency.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If conventional SBRs use frequent ramping of air flow rates, then oxygen levels are optimized for each process step, but operational complexity increases

Engineering Contradiction:
Improveoxygen level optimizationVSAvoidoperational complexity
Core Design Contradiction:
ReliabilityVSEase of operation

Solution Approach 1:

The patent combines the separate control sequences for nitrification and denitrification into a single continuous aeration process. Instead of switching between high and low air flow rates, the system maintains a steady low dissolved oxygen level (0.2-2.0 mg/L) throughout the reaction period, simplifying operational control while achieving both nitrogen removal processes simultaneously.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent implements continuous low-level aeration throughout the reaction period rather than intermittent high-level aeration followed by complete oxygen removal. This continuous aerated-anoxic operation eliminates the need for frequent air flow adjustments, maintaining optimal conditions for simultaneous nitrification and denitrification while simplifying operational procedures.

Inventive Principle:
Principle #20Continuity of useful action

3Reliability

If separate nitrification and denitrification steps are used, then nitrogen removal efficiency is improved, but process time increases

Engineering Contradiction:
Improvenitrogen removal efficiencyVSAvoidprocess time
Core Design Contradiction:
ReliabilityVSLoss of time

Solution Approach 1:

The patent merges sequential nitrification and denitrification steps into a single simultaneous process. By maintaining dissolved oxygen at low levels (0.2-2.0 mg/L) during the reaction period, both ammonia oxidation and nitrate reduction occur concurrently in the same reactor zone, eliminating the time required to switch between process modes and reducing total treatment time while maintaining nitrogen removal efficiency.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent implements continuous simultaneous nitrification and denitrification throughout the reaction period without interruption or mode switching. The aerated-anoxic operation with controlled low dissolved oxygen levels ensures both processes proceed continuously and concurrently, maximizing nitrogen removal rate and reducing the overall process time compared to sequential operations.

Inventive Principle:
Principle #20Continuity of useful action

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

The SNDN process achieves efficient wastewater treatment with reduced energy costs and simplified operations by eliminating the need for separate nitrification and denitrification steps, while maintaining effluent quality, and potentially reducing tank volume and blower size.

Implementation Method 1

aerobic, anoxic, and/or anaerobic treatment units to reduce the total organic content and/or biochemical oxygen demand of the wastewater and nutrients such as nitrogen and phosphorus

Methodology Applied
Scientific EffectNitrification: Oxidation

Implementation Method 2

aerobic, anoxic, and/or anaerobic treatment units to reduce the total organic content and/or biochemical oxygen demand of the wastewater and nutrients such as nitrogen and phosphorus

Methodology Applied
Scientific EffectDenitrification: Reduction

Data Source

PatentUS12049416B2Simultaneous nitrification/denitrification (SNDN) in sequencing batch reactor applications
Publication Date: 2024.07.30 EVOQUA WATER TECHNOLOGIES LLC
  • US12049416B2 patent drawing
  • US12049416B2 patent drawing
  • US12049416B2 patent drawing

AI summary

A method of operating a sequencing batch reactor process includes introducing wastewater to be treated into the sequencing batch reactor and subjecting the wastewater to treatment in the sequencing batch reactor in an aerated anoxic mode in in which a quantity of oxygen is supplied at a level insufficient to meet a biological oxygen demand of the wastewater, but sufficient to cause simultaneous nitrification and denitrification reactions to occur in the wastewater.