Ammonia Rebound Prevention in Cold-Weather Bioreactors

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Solution Overview

Problem

Wastewater treatment systems experience ammonia rebound during spring weather, leading to elevated ammonia concentrations in effluent, which exceed regulatory limits due to rapid digestion of stored sludge and biosolids, particularly in northern regions.

Innovation Solution

A wastewater treatment system and method that operates in multiple modes, allowing wastewater to bypass the partial mix cell and flow directly to the polishing cell during springtime warmup, and includes a control system to manage sludge and biosolids removal, thereby controlling ammonia release and stabilization.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If sludge and biosolids are stored in the partial mix cell during cold weather, then effluent quality is maintained, but ammonia rebound occurs during spring warmup exceeding regulatory limits

Engineering Contradiction:
Improveeffluent qualityVSAvoidammonia concentration
Core Design Contradiction:
ReliabilityVSObject-affected harmful factors

Solution Approach 1:

The patent extracts the sludge and biosolids from the partial mix cell through a sludge removal system that directs them to a separate digestion system. This prevents the accumulation of stored sludge in the partial mix cell that would otherwise cause ammonia rebound during spring warmup, while maintaining effluent quality through continuous treatment.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent introduces a separate digestion system as an intermediary to handle sludge and biosolids removal. This intermediate system processes the organic matter before it enters the partial mix cell, preventing ammonia generation in the main treatment cell while still achieving stabilization goals.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Stability of the object's composition

If sludge and biosolids are digested in the partial mix cell during warm weather, then stabilization is achieved, but ammonia is released into the effluent

Engineering Contradiction:
Improvesludge stabilizationVSAvoidammonia release
Core Design Contradiction:
Stability of the object's compositionVSObject-generated harmful factors

Solution Approach 1:

The patent segments the treatment process by separating sludge digestion from the main partial mix cell treatment. Sludge is removed and digested in a separate system, while the partial mix cell focuses on wastewater treatment. This segmentation prevents ammonia generated during digestion from contaminating the effluent.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent extracts the digestion function from the partial mix cell by implementing a dedicated sludge removal and digestion system. This extraction allows stabilization to occur in isolation, preventing harmful ammonia release into the main treatment stream and effluent.

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If wastewater flows through the partial mix cell during spring warmup, then treatment continues, but ammonia rebound from stored sludge exceeds regulatory limits

Engineering Contradiction:
Improvetreatment continuityVSAvoidammonia concentration
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent implements preliminary sludge removal action before spring warmup occurs. By continuously or periodically removing sludge throughout cold weather operations, the system prevents the accumulation of stored organic matter that would otherwise undergo rapid decomposition and cause ammonia rebound during temperature increase.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent maintains continuous sludge removal action to prevent accumulation. The sludge removal system operates continuously or at frequent intervals, ensuring that organic matter does not accumulate to levels that would cause ammonia rebound, thereby maintaining both treatment productivity and effluent quality throughout seasonal transitions.

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

This approach reduces ammonia rebound by retaining sludge and biosolids in the partial mix cell for digestion, preventing excessive ammonia release and maintaining effluent quality within regulatory limits.

Implementation Method 1

During the treatment of the wastewater in the reactor 12, sludge, such as waste activated sludge (WAS), and excess biosolids are generated

Methodology Applied
Scientific EffectAnaerobic Digestion: Anaerobic Digestion

Implementation Method 2

the sludge and biosolids are digested in the reactor 12 and/or partial mix cell 16, and are stabilized

Methodology Applied
Scientific EffectAerobic Digestion: Aerobic Digestion

Implementation Method 3

allowing wastewater to bypass the partial mix cell and flow directly to the polishing cell during springtime warmup

Methodology Applied
Scientific EffectFluid Flow:

Implementation Method 4

Once the temperature of the wastewater drops below a certain temperature, which may be in a range between about 12° C. and 18° C. (e.g., below 15° C.), digestion generally ceases

Methodology Applied
Scientific EffectBiological Degradation: Decomposition (biological)

Data Source

PatentUS10150684B2System and method for preventing ammonia rebound in a cold-weather bioreactor
Publication Date: 2018.12.11 ENVIRONMENTAL DYNAMICS INTERNATIONAL INC
  • US10150684B2 patent drawing
  • US10150684B2 patent drawing
  • US10150684B2 patent drawing

AI summary

A wastewater treatment system and method are provided for preventing or reducing ammonia rebound during periods of warming weather. The system may be operated in first and second modes of operation. During the first mode of operation, wastewater may pass directly from a reactor to a partial mix cell and then to a polishing cell. During the second mode of operation, which typically occurs during a springtime warmup period, wastewater is retained within the partial mix cell until sludge and biosolids therein are substantially digested, while wastewater exiting the reactor is temporarily directed to the polishing cell, thereby bypassing the partial mix cell. Upon digestion and stabilization of the sludge and biosolids in the partial mix cell, the system may return to the first mode of operation. Sludge and biosolids may optionally be removed from the reactor during the first and second modes of operation.