Continuous Flow Reactor for Aerobic Granular Sludge

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Solution Overview

Problem

Existing wastewater treatment systems, particularly large continuous flow reactors, face challenges in achieving stable granulation and efficient nutrient removal due to instability and high energy requirements, making it difficult to retrofit conventional systems for aerobic granular sludge processes.

Innovation Solution

A continuous flow reactor configuration with an anoxic zone upstream, an anaerobic zone, and an aerobic zone downstream, along with a solids separation device and return line for recycling aerobic granular sludge, is designed to promote stable granulation and efficient nutrient removal, allowing for selective wasting and controlled feast and famine conditions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional activated sludge processes use continuous flow reactors, then treatment capacity is maintained, but granulation stability is poor and energy efficiency is low

Engineering Contradiction:
Improvegranulation stabilityVSAvoidenergy efficiency
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The continuous flow reactor is divided into multiple functional zones (anoxic zone, aerobic zone, and settling zone) rather than using a single mixed reactor. This segmentation allows different physiological conditions to be maintained in each zone, promoting stable granulation while improving overall treatment efficiency and energy utilization.

Inventive Principle:
Principle #1Segmentation

2Reliability

If sequencing batch reactors are used for aerobic granular sludge, then granulation stability is improved, but retrofitting existing continuous flow infrastructure is not feasible

Engineering Contradiction:
Improvegranulation stabilityVSAvoidretrofit capability
Core Design Contradiction:
ReliabilityVSAdaptability or versatility

Solution Approach 1:

The system maintains continuous flow operation (static hydraulic regime) while dynamically creating alternating anoxic and aerobic conditions through the multi-zone configuration. This allows the system to achieve granulation stability similar to sequencing batch reactors without requiring batch operation, making it compatible with existing continuous flow infrastructure.

Inventive Principle:
Principle #15Dynamics

3Productivity

If multiple basins are used for different oxidation conditions, then treatment efficiency is improved, but system complexity and footprint increase

Engineering Contradiction:
Improvetreatment efficiencyVSAvoidsystem complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

Multiple functional zones (anoxic and aerobic reactors) are hydraulically connected and operated as an integrated continuous flow system. The zones are merged through controlled sludge recirculation that creates alternating redox conditions, achieving the treatment efficiency of multiple separate basins while reducing overall system complexity and footprint.

Inventive Principle:
Principle #5Merging (Combining)

4Adaptability or versatility

If conventional activated sludge is used, then infrastructure compatibility is maintained, but volumetric loading and biomass retention are reduced

Engineering Contradiction:
Improveinfrastructure compatibilityVSAvoidvolumetric loading
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The system changes the operational parameters by creating alternating anoxic and aerobic conditions through controlled sludge recirculation between zones. This parameter change promotes the formation of aerobic granular sludge with higher density and better settling properties, enabling significantly higher volumetric loading rates while maintaining compatibility with existing continuous flow reactor infrastructure.

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

This configuration enables stable aerobic granular sludge formation and efficient nutrient removal, reducing energy consumption and maintaining high treatment efficiency, suitable for retrofitting existing reactors to achieve smaller footprints and lower operational costs.

Implementation Method 1

an anoxic zone situated upstream of the anaerobic zone and said anoxic zone comprising one or more additional CMR or PFR

Methodology Applied
Scientific EffectDenitrification: Anaerobic Digestion

Implementation Method 2

an aerobic zone situated downstream of anaerobic zone and comprising at least one PFR or multiple CMR in series

Methodology Applied
Scientific EffectAerobic degradation: Aerobic Digestion

Implementation Method 3

aerobic zone... comprising at least one PFR or multiple CMR in series

Methodology Applied
Scientific EffectNitrification: Oxidation

Implementation Method 4

a solids separation device situated downstream of the aerobic zone

Methodology Applied
Scientific EffectSedimentation: Sedimentation

Implementation Method 5

a return line having an inlet arranged to receive a supply of return activated sludge from the solids separation device and an outlet that feeds into the anoxic zone

Methodology Applied
Scientific EffectGravitational settling: Gravitation

Data Source

PatentUS11746030B2Aerobic granular sludge in continuous flow reactors
Publication Date: 2023.09.05 UNIVERSITY OF MANITOBA
  • US11746030B2 patent drawing
  • US11746030B2 patent drawing
  • US11746030B2 patent drawing

AI summary

Aerobic granular sludge (AGS) is an energy efficient and compact biological wastewater treatment process. There is only one commercially available AGS technology which utilizes sequencing batch reactors (SBR). Many existing wastewater treatment facilities consist of long, continuous flow reactors that would not be readily suitable for retrofit to SBR. Therefore, a continuous flow process is preferred for municipalities that cannot economically invest in the only commercially available SBR technology (i.e., Nere-da®). Lab- and pilot-scale experimentation has demonstrated that stable granulation can be achieved in a continuous flow configuration GT suitable for retrofit into existing infrastructure. An anoxic/anaerobic/aerobic configuration can be designed and stably operated for conversion of flocculent biomass to AGS Preliminary pilot-scale results on primary effluent from a municipal wastewater treatment facility indicated that granules of 0.2-0.5 mm, SVI<75 mL/g, and SV30 min/SVI5 min>70% can be formed within a month of steady operation.