Steam Explosion Reactor Pressure Relief and Sterilization

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Solution Overview

Problem

Current continuous steam explosion reactors face challenges in maintaining high-pressure efficiency, reducing instrumental strain, and effectively sterilizing organic waste streams, which are contaminated with bacteria, making them unsuitable for downstream processing without additional sterilization steps.

Innovation Solution

A semi-continuous steam explosion reactor with a high-pressure retention section, pressure relief section, and discharge section, equipped with adjustable-speed conveyors and integrated carbon dioxide scrubbing units, operates under alkaline conditions to rupture compact fiber structures, facilitate hydrolysis, and sterilize organic materials, using pressurized gas to supplement steam for pressure generation and enhance structural disintegration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If continuous steam explosion reactors operate at high pressure to maintain efficiency, then productivity is improved, but instrumental strain and device complexity increase

Engineering Contradiction:
Improvecontinuous operation efficiencyVSAvoidhigh-pressure instrumentation strain
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The reactor is divided into distinct functional sections: a high-pressure retention section for maintaining pressure, a pressure relief section for controlled depressurization, and a discharge section for material output. This segmentation allows each section to be optimized for its specific function, reducing overall instrumental strain while maintaining continuous high-pressure operation capability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A movable partition wall is introduced as an intermediary element between the high-pressure retention section and the discharge section. This partition wall controls the release of pressurized material, enabling safe pressure relief while maintaining the high-pressure environment in the retention section during continuous operation.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If steam explosion is used to rupture fiber structures and sterilize organic waste, then purity and productivity are improved, but energy consumption increases

Engineering Contradiction:
Improvesterilization and hydrolysis efficiencyVSAvoidsteam generation energy demand
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The process utilizes phase transitions of water (liquid to steam) to achieve both sterilization and structural rupture of organic material. Steam is generated by heating water to high temperatures (180-240°C), and the rapid phase change and expansion of steam provides the mechanical force needed for fiber disruption while simultaneously sterilizing the organic waste stream.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The system operates by dynamically changing temperature and pressure parameters. Water is heated to high temperatures and pressurized to generate steam, then rapidly depressurized to effect the explosion and rupture. This parameter change sequence achieves efficient sterilization and hydrolysis while the high-pressure steam serves dual purposes: sterilization and mechanical disruption.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If pressurized gas is used to supplement steam for pressure generation, then productivity is improved, but device complexity increases

Engineering Contradiction:
Improvepressure generation efficiencyVSAvoidgas supplementation system
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The system merges steam generation and pressurized gas delivery into a unified pressure generation approach. Pressurized gas (such as nitrogen or carbon dioxide) is introduced alongside steam to enhance the pressure differential during the explosion phase. This combination achieves more effective fiber disruption and faster pressure release while the gas-steam mixture is delivered through integrated injection ports in the reactor.

Inventive Principle:
Principle #5Merging (Combining)

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 reactor efficiently pre-treats organic materials, increasing accessibility for further processing, producing value-added products like methane, ethanol, and biodiesel, while providing effective sterilization, reducing energy demands, and minimizing instrumental erosion.

Implementation Method 1

The chips are then steam heated at a temperature of about 285°C and a pressure of 3.5 MPa for about 2 min

Methodology Applied
Scientific EffectSteam heating: Heating

Implementation Method 2

Steam explosion of biomass is a pre-treatment process that opens up the fibers, and makes the biomass polymers more accessible for subsequent processes

Methodology Applied
Scientific EffectSteam explosion: Steam Explosion

Implementation Method 3

pressurized gas to supplement steam for pressure generation and enhance structural disintegration

Methodology Applied
Scientific EffectPressurization: Pressurisation

Data Source

PatentEP3942106B1Steam-explosion equipment and method for treatment of organic material
Publication Date: 2024.01.24 YMIR TECH EHF
  • EP3942106B1 patent drawingFigure 1
  • EP3942106B1 patent drawingFigure 2
  • EP3942106B1 patent drawingFigure 3

AI summary

A continuous-flow steam explosion reactor for pretreatment of organic material for further processing to value-added products is provided. The reactor comprises a loading section, a high-pressure retention section with an adjustable-speed conveyor, a pressure relief section and a discharge section. The reactor comprises means for providing steam into at least said high-pressure retention section and means for providing pressurized gas (e.g. air) to further boost pressure. The loading section is suitably configured to transfer material from ambient pressure to the high-pressure retention section while retaining high pressure and temperature in the high-pressure retention section, and the pressure relief section configured to transfer material from the high-pressure retention section to a discharge section while retaining high pressure in the high-pressure retention section. The pressure relief section is configured to release material with a drop in pressure to said discharge section while retaining high pressure in the high-pressure retention section.