Bioreactor Process Water Recirculation for Waste Liquefaction

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Solution Overview

Problem

Current waste processing methods, such as incineration and landfill, do not optimally utilize the energy stored in organic waste, and existing bioreactor systems do not effectively recirculate process water from downstream anaerobic digestion processes back into the bioreactor for enzymatic and microbial treatment of municipal solid waste.

Innovation Solution

A method involving the recirculation of process water from downstream processes, including bioliquids and reject water, into the bioreactor for enzymatic and microbial treatment of waste, reducing the need for external water sources and optimizing pH conditions for continuous or batch processing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If process water from downstream processes is recirculated into the bioreactor, then water consumption is reduced and process efficiency is enhanced, but pH control becomes more challenging due to variable composition of recirculated water

Engineering Contradiction:
Improvewater consumptionVSAvoidpH control
Core Design Contradiction:
Loss of energyVSEase of operation

Solution Approach 1:

The patent implements pH monitoring and control systems that continuously measure the pH of recirculated process water and adjust the treatment process accordingly. This feedback mechanism allows the system to maintain optimal pH conditions despite the variable composition of recirculated water from different downstream processes.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent adjusts pH as a controllable parameter to optimize the enzymatic and microbial treatment processes. By dynamically modifying pH levels based on the specific composition of recirculated water, the system maintains optimal conditions for bioliquid production while accommodating variations in recirculated stream characteristics.

Inventive Principle:
Principle #35Parameter changes

2Device complexity

If recirculated process water is used without pH adjustment, then operational complexity is reduced, but enzymatic and microbial activity may be inhibited due to suboptimal pH conditions

Engineering Contradiction:
ImprovepH adjustment systemVSAvoidenzymatic and microbial activity
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The patent employs naturally occurring buffering capacity of the waste substrate and biological communities to self-regulate pH within acceptable ranges. The microbial consortia and enzymatic systems inherently tolerate and adapt to pH fluctuations, reducing the need for external pH adjustment while maintaining treatment effectiveness.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The patent applies pH adjustment only when necessary, rather than continuously. By monitoring key parameters and applying corrections only when pH deviates beyond critical thresholds, the system balances operational simplicity with maintaining reliable enzymatic and microbial activity.

Inventive Principle:
Principle #16Partial or excessive action

3Quantity of substance

If external water sources are used instead of recirculated process water, then pH control is simplified, but water consumption increases and process sustainability is reduced

Engineering Contradiction:
Improvewater consumptionVSAvoidwater management
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

The patent recovers and reuses process water from downstream anaerobic digestion and other treatment processes, transforming what would be waste streams into valuable resources. This circular water management approach reduces freshwater consumption while the recovered water is integrated back into the enzymatic hydrolysis process after appropriate treatment.

Inventive Principle:
Principle #34Discarding and recovering

Solution Approach 2:

The recirculated process water serves multiple functions: it provides process water for enzymatic treatment, maintains moisture content in the bioreactor, and contributes to the overall water balance of the integrated system. This multi-functionality reduces the need for separate water management systems.

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 efficiency of enzymatic and microbial liquefaction processes, reduces water consumption, and maintains optimal pH conditions for bioliquid production, leading to improved energy recovery from waste.

Implementation Method 1

subjecting waste to an enzymatic and/or microbial treatment in a bioreactor

Methodology Applied
Scientific EffectEnzymatic degradation: Enzyme

Implementation Method 2

enzymatic degradation and/or microbial fermentation producing a bioliquid

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Implementation Method 3

enzymatic degradation and/or microbial fermentation producing a bioliquid

Methodology Applied
Scientific EffectMicrobial fermentation: Fermentation

Implementation Method 4

adding the process water obtained from step c) and optionally water from an external water source to the bioreactor in step a)... maintains optimal pH conditions for bioliquid production

Methodology Applied
Scientific EffectpH buffering:

Data Source

PatentUS20230405654A1Method for enzymatic and/or microbial processing of waste comprising recirculation of process water
Publication Date: 2023.12.21 RENESCIENCE AS
  • US20230405654A1 patent drawing
  • US20230405654A1 patent drawing
  • US20230405654A1 patent drawing

AI summary

The present invention relates to a method for continuous or batch processing of waste, such as municipal solid waste, subject to enzymatic and/or microbial degradation in a bioreactor resulting in a bioliquid and a solid fraction, which method comprises recirculation of process water obtained from downstream processing of said bioliquid and/or solid fraction. Water from external sources may also be added to the reactor in addition to the recirculation of process water.