Two-Stage Anaerobic Digester for Wastewater Treatment

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Solution Overview

Problem

Anaerobic wastewater treatment systems face challenges such as high operating costs, sensitivity to pH changes, and reduced tolerance for feed composition fluctuations due to the slow growth and fastidious nature of methanogenic bacteria, particularly in systems with sulfur-containing wastewater streams, which affects the efficiency and robustness of methane production.

Innovation Solution

A two-stage downflow anaerobic digester system with a predigester operating at acidic pH for acidification and an anaerobic bioreactor at neutral pH for methane production, utilizing high surface area porous media to support microbial growth, and incorporating recirculation and buffering agents to maintain optimal pH conditions and reduce the need for expensive chemicals.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a single-stage anaerobic digestion system is used, then the system structure is simple, but the treatment efficiency is low and the system is sensitive to pH changes

Engineering Contradiction:
Improvesystem structureVSAvoidtreatment efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The anaerobic digestion system is divided into two separate stages: an acidogenic stage operating at acidic pH (5.5-6.5) and a methanogenic stage operating at neutral pH (7.0-7.5). This segmentation allows each stage to operate under optimal conditions independently, improving overall treatment efficiency while maintaining manageable system complexity through modular design

Inventive Principle:
Principle #1Segmentation

2Quantity of substance

If methanogenic bacteria are used for anaerobic digestion, then methane production occurs, but the bacteria grow slowly and are fastidious requiring precise pH control

Engineering Contradiction:
Improvemethane productionVSAvoidpH control requirements
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

By separating the acidogenic and methanogenic processes into distinct reactors, the system allows methanogenic bacteria to operate under stable neutral pH conditions without being subjected to the acidic environment of the first stage. This eliminates the need for continuous pH adjustment in the methanogenic stage and reduces sensitivity to feed composition fluctuations

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The acidogenic reactor acts as an intermediary that pre-processes the wastewater, converting complex organic matter into volatile fatty acids and simplifying the substrate before it enters the methanogenic stage. This intermediary step protects the fastidious methanogenic bacteria from direct exposure to harsh feed conditions

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If sulfur-containing wastewater is treated in anaerobic systems, then organic matter degradation occurs, but hydrogen sulfide is produced which is toxic to methanogenic bacteria

Engineering Contradiction:
Improveorganic matter degradationVSAvoidhydrogen sulfide toxicity
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The two-stage configuration separates sulfur reduction and hydrogen sulfide production in the acidogenic stage from the methanogenic stage. The acidic environment of the first stage tolerates hydrogen sulfide generation, while the second stage receives pre-treated wastewater with reduced sulfur compound concentrations, protecting methanogenic bacteria from toxicity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system converts the potentially harmful hydrogen sulfide production into a manageable process by confining it to the acidogenic stage where it can be controlled and partially oxidized. The sulfur compounds serve as an electron acceptor in the acidogenic stage, driving organic matter degradation while the subsequent neutral pH stage provides a safe environment for methane production

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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

The system enhances the robustness and stability of the microbial population, allowing for efficient treatment of high-strength wastewater with reduced operating costs and improved tolerance to environmental changes, while maintaining optimal conditions for methane production and minimizing sludge production.

Implementation Method 1

Biological wastewater treatment involves the use of large numbers of bacteria contained within a bioreactor to degrade organic matter contained within the wastewater thereby creating a clean water discharge. Use of anaerobic bacteria over aerobic bacteria in the treatment of wastewater is preferable

Methodology Applied
Scientific EffectAnaerobic digestion: Anaerobic Digestion

Implementation Method 2

each of the predigester and anaerobic bioreactor further comprise at least one recirculation device withdrawing fluid from a lower portion of each of the predigester and anaerobic bioreactor and returning the withdrawn fluid to an upper portion of each of the predigester and anaerobic bioreactor respectively

Methodology Applied
Scientific EffectRecirculation:

Implementation Method 3

the inlet and the outlet are arranged so that the fluid enters the two stage anaerobic digester at the at least one predigester inlet and flows in a downward direction through the predigester from the at least one predigester inlet to the at least one predigester outlet

Methodology Applied
Scientific EffectGravity: Gravitation

Data Source

PatentEP2558421B1An anaerobic wastewater treatment system
Publication Date: 2017.01.25 BIOTECHN PROCESSES INT
  • EP2558421B1 patent drawingFigure 1

AI summary

A two stage downflow anaerobic digester (100) is provided for the treatment of fluid containing oxygen demanding organic material with microorganisms comprising a predigester (10) and at least one anaerobic bioreactor (11) having a plurality of high surface area porous media (111) suitable for growth of microorganisms contained therein. The influent stream (50) enters the predigester (10) and flows downwardly through the vessel which is then withdrawn from the predigester (10) and introduced into the anaerobic bioreactor (11) such that the fluid flows downwardly through the media (111) thereby engaging with the microorganisms supported thereupon. Both stages operate to reduce the level of oxygen demanding material in the fluid stream relative to the level of oxygen demanding material in the influent stream (50). Each of the predigester (10) and anaerobic bioreactor (11) further comprises a recirculation device (25a, 27a) for recirculating fluid within each vessel. The apparatus further comprises a return circulation feed (25b) between the anaerobic bioreactor (11) and the predigester (10).