Concentric Bioreactor for High Volatile Organic Waste

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Solution Overview

Problem

Current biodigestion technologies face challenges in efficiently treating organic waste with high volatile organic matter content, particularly in maintaining optimal conditions for methanogenesis and managing substrates with varying compositions, leading to inefficiencies and increased costs due to the need for multiple tanks and complex processes.

Innovation Solution

A multi-phase anaerobic digestion process with a continuous piston-type loading system, featuring a specific architectural design with concentric cells and bioturbation zones, which allows for distinct biological retention times and efficient phase separation, utilizing radiant heating and micro-bubbling to maintain microbiological balance and promote granulation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional biodigestion technologies are used to treat organic waste with high volatile organic matter content, then the treatment process can be implemented, but the efficiency is reduced and costs increase due to the need for multiple tanks and complex processes

Engineering Contradiction:
Improvemethane production efficiencyVSAvoidnumber of tanks and process complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The bioreactor is divided into multiple functional zones (aeration zone, anaerobic digestion zone, sedimentation zone) within a single integrated structure, allowing distinct biological processes to occur simultaneously in different spatial regions. This segmentation enables efficient treatment of high volatile organic matter content waste while avoiding the need for multiple separate tanks.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention combines aeration, anaerobic digestion, and sedimentation functions into a single bioreactor system. The aerobic aeration zone and anaerobic digestion zone are integrated, along with the sedimentation zone, creating a unified process that reduces equipment complexity while maintaining high productivity for treating organic waste with high volatile organic matter content.

Inventive Principle:
Principle #5Merging (Combining)

2Reliability

If multiple tanks and complex processes are used to maintain optimal conditions for methanogenesis, then the biological constraints can be satisfied, but the investment costs increase

Engineering Contradiction:
Improveoptimal conditions for methanogenesisVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

Different zones within the bioreactor are designed with specific local characteristics: the aeration zone provides oxygen for aerobic degradation, the anaerobic digestion zone maintains anaerobic conditions with appropriate pH and temperature for methanogenesis, and the sedimentation zone provides quiescent conditions for solids separation. Each zone is optimized for its specific function, ensuring reliable methanogenesis while simplifying the overall process.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The system employs dynamic control of operational parameters including pH adjustment, temperature maintenance, and controlled aeration rates to maintain optimal conditions for methanogenesis. The bioreactor can adapt to varying substrate compositions and loading rates, ensuring reliable performance without requiring overly complex process designs.

Inventive Principle:
Principle #15Dynamics

3Adaptability or versatility

If conventional processes are used to handle substrates with varying compositions, then the treatment can be performed, but the versatility and productivity are reduced

Engineering Contradiction:
Improveability to handle varying substrate compositionsVSAvoidmethane production productivity
Core Design Contradiction:
Adaptability or versatilityVSProductivity

Solution Approach 1:

The bioreactor system allows dynamic adjustment of operational parameters such as aeration rate, pH, temperature, and hydraulic retention time to accommodate varying substrate compositions. The aerobic aeration zone can be adjusted to handle different volatile organic matter contents, while the anaerobic zone maintains conditions optimal for methanogenesis, enabling the system to adapt to diverse organic waste streams while maintaining high productivity.

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 approach enhances the versatility and modularity of the system, improving productivity and reducing investment costs by maintaining optimal conditions for each phase of digestion, effectively handling substrates with high volatile organic matter content and promoting efficient methane production.

Implementation Method 1

The treatment of organic materials by biodigestion is above all subject to biological constraints that the techniques which aim to create and maintain a favorable ecosystem for the microorganisms specific to this type of bio-oxidation attempt to respect.

Methodology Applied
Scientific EffectAnaerobic digestion: Anaerobic Digestion

Implementation Method 2

these particular microbial populations develop bio-oxidation activity, but in the absence of oxygen from the air.

Methodology Applied
Scientific EffectBio-oxidation: Oxidation

Implementation Method 3

A digestate heating device

Methodology Applied
Scientific EffectThermal heating: Heating

Implementation Method 4

A stirring or stirring device

Methodology Applied
Scientific EffectMechanical mixing: Stirring

Implementation Method 5

Inlet and outlet devices for the substrate, digestate and biogas

Methodology Applied
Scientific EffectGas-liquid separation: Flow Separation

Data Source

PatentEP3393984B1Facility and method for biologically treating organic waste and effluents
Publication Date: 2021.04.28 JUA GRP
  • EP3393984B1 patent drawingFigure 1
  • EP3393984B1 patent drawingFigure 2
  • EP3393984B1 patent drawingFigure 3~4

AI summary

The facility comprises: - a first tank (1) comprising separation means (15) extending over a portion of the height of the tank, so as to define a central compartment, or tube (11), a peripheral compartment, or ring (12), and a compartment for stirring and biochemical exchanges (16) in the bottom portion of the tank, comprising stirring means (17), - a second tank (2) comprising separation means (25) extending over a portion of the height of the tank, so as to define a central compartment, or tube (21), a peripheral compartment, or ring (22), and a compartment for stirring and biochemical exchanges (26) in the bottom portion of the tank, comprising stirring means (27), - means (ALIM) for feeding the waste to be treated into the first ring - means (T) for transferring the partially treated waste from the first tube to the second ring, - means (EVAC) for discharging the treated waste out of the second tube, - advantageously pneumatic means (4, 43, 44) for circulating the waste from the first ring to the second tube.