Nitrification Reactor Thermal Management for Cold Climate Lagoons

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Solution Overview

Problem

Aerated lagoons in northern climates face challenges with low nitrification efficiency due to low temperatures, high biological oxygen demand (BOD), and biomass concentration, leading to incomplete nitrogen removal and operational difficulties in cold climates.

Innovation Solution

A water treatment system with a nitrification reactor positioned at the influent end of a lagoon, utilizing a high surface-to-volume ratio and thermally conductive materials to maintain higher temperatures, receiving treated wastewater from a BOD reactor, and incorporating biomedia with a high surface area to promote nitrification and heat exchange.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Volume of stationary object

If aerated lagoons are used in northern climates, then large volumes and long retention times are achieved, but nitrification efficiency deteriorates due to low temperatures

Engineering Contradiction:
Improvelagoon volumeVSAvoidnitrification efficiency
Core Design Contradiction:
Volume of stationary objectVSProductivity

Solution Approach 1:

The system divides the treatment process into two distinct segments: a BOD removal reactor and a nitrification reactor. This segmentation allows each reactor to be optimized for its specific function, with the nitrification reactor operating at higher temperatures independent of the overall lagoon temperature, thus resolving the contradiction between large volume and low nitrification efficiency.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The nitrification reactor is designed with thermally conductive walls and positioning in warmer water layers to maintain locally higher temperatures than the bulk lagoon. This local quality enhancement enables effective nitrification in specific zones without requiring the entire large volume to be warm, resolving the temperature-efficiency contradiction.

Inventive Principle:
Principle #3Local quality

2Reliability

If conventional diffuser anchoring is used, then diffusers are secured in place, but installation and maintenance difficulty increases

Engineering Contradiction:
Improvediffuser positioningVSAvoiddiffuser installation and maintenance
Core Design Contradiction:
ReliabilityVSEase of operation

Solution Approach 1:

The diffuser system transitions from a static permanently anchored design to a dynamic removable design. The diffuser can be easily inserted and removed from the diffuser plate, allowing for simple maintenance and replacement while maintaining reliable positioning during operation through the plate's structural support.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The diffuser element is extracted as a separate removable component from the anchoring system. This allows the diffuser to be easily removed for maintenance or replacement without disturbing the anchoring structure, resolving the contradiction between secure positioning and ease of maintenance.

Inventive Principle:
Principle #2Taking out (Extraction)

3Quantity of substance

If biomass concentration is increased in lagoons, then treatment capacity is improved, but nitrification efficiency deteriorates due to competition for oxygen and space

Engineering Contradiction:
Improvebiomass concentrationVSAvoidnitrification efficiency
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The system segments the biological treatment into two distinct functional reactors: one for BOD removal and another for nitrification. This segmentation eliminates competition between heterotrophic and autotrophic bacteria by providing separate environments optimized for each bacterial type, allowing high biomass concentration in the BOD reactor without compromising nitrification efficiency in the nitrification reactor.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system changes the environmental parameters between the two reactors - the BOD reactor operates with high organic matter and heterotrophic bacteria, while the nitrification reactor operates with low organic matter and autotrophic bacteria. This parameter differentiation resolves the competition issue and allows both processes to operate at high efficiency.

Inventive Principle:
Principle #35Parameter changes

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

Enhances nitrification efficiency in colder months without additional heating, reducing operational costs and manpower requirements, while maintaining effective wastewater treatment.

Implementation Method 1

the reactor being positioned at the influent end of the body of water, and having a reactor inlet adapted to receive at least a portion of the wastewater from the effluent end of the body of water

Methodology Applied
Scientific EffectHeat exchange: Convection

Implementation Method 2

utilizing a high surface-to-volume ratio and thermally conductive materials to maintain higher temperatures

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Implementation Method 3

wastewater is aerated by providing gas diffusers which release gas bubbles into the wastewater. The gas released into the wastewater by the diffusers promotes biological decomposition of soluble organic contaminants

Methodology Applied
Scientific EffectGas dissolution and bubble formation: Bubble

Implementation Method 4

incorporating biomedia with a high surface area to promote nitrification

Methodology Applied
Scientific EffectBiofilm formation and adsorption: Adsorption

Data Source

PatentUS11358890B2Water treatment reactors, systems and methods
Publication Date: 2022.06.14 BIONEST TECH
  • US11358890B2 patent drawing
  • US11358890B2 patent drawing
  • US11358890B2 patent drawing

AI summary

A system for wastewater treatment includes a reactor for nitrification of wastewater in a body of water. The body of water has an influent end and an effluent end. The reactor is positioned at the influent end of the body of water, and has a reactor inlet adapted to receive at least a portion of the wastewater from the effluent end of the body of water or from at or near an outlet of the system.