Thermal Decomposition Reactor for MSW Syngas Production

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Solution Overview

Problem

Current methods for converting municipal solid waste (MSW) to energy are inefficient, leading to significant greenhouse gas emissions and waste volume, with landfilling being the most popular but environmentally detrimental method.

Innovation Solution

A system utilizing canisters and specially designed autoclaves for thermal decomposition of MSW, producing syngas with enhanced BTU value and reducing waste volume by up to 95%, while recovering heat for electricity generation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If thermal decomposition is used to convert MSW to energy, then energy production and waste volume reduction are improved, but process complexity and capital investment increase

Engineering Contradiction:
Improveenergy productionVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The thermal decomposition process is divided into distinct stages: drying phase (100-200°C), pyrolysis phase (300-500°C), and combustion phase (600-900°C). Each stage operates in a separate temporal and spatial zone within the reactor, allowing independent optimization of conditions for each phase while maintaining overall process efficiency.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent extracts and utilizes the heat generated during combustion phase to preheat incoming waste material and generate steam for electricity production. This extracts useful energy from what would otherwise be wasted thermal energy, improving overall system efficiency while reducing the need for additional external energy inputs.

Inventive Principle:
Principle #2Taking out (Extraction)

2Ease of manufacture

If landfilling is used for waste disposal, then capital investment is reduced, but greenhouse gas emissions and environmental harm increase

Engineering Contradiction:
Improvecapital investmentVSAvoidgreenhouse gas emissions
Core Design Contradiction:
Ease of manufactureVSObject-generated harmful factors

Solution Approach 1:

The patent converts the potential harm of methane emissions from landfilled waste into beneficial syngas production through controlled thermal decomposition. The organic matter that would otherwise decompose anaerobically to produce harmful methane is instead processed aerobically to generate useful combustible gas and energy, transforming an environmental problem into a resource.

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

Solution Approach 2:

The process changes the fundamental parameters of waste treatment by shifting from anaerobic decomposition at ambient temperature to controlled aerobic thermal decomposition at elevated temperatures (100-900°C). This parameter change fundamentally alters the chemical pathways, converting harmful methane generation into beneficial syngas production while simultaneously reducing waste volume through thermal decomposition.

Inventive Principle:
Principle #35Parameter changes

3Use of energy by moving object

If gasification is used to process MSW, then energy efficiency is improved, but waste sorting and preprocessing requirements increase

Engineering Contradiction:
Improveenergy efficiencyVSAvoidpreprocessing requirements
Core Design Contradiction:
Use of energy by moving objectVSEase of operation

Solution Approach 1:

The reactor is designed to universally accept various forms of municipal solid waste including sorted, unsorted, baled, and loose materials. The multi-functional design allows the same reactor to handle different waste types and configurations without requiring separate preprocessing lines, eliminating the need for mandatory sorting while maintaining high energy efficiency through adaptive thermal decomposition.

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

Solution Approach 2:

The system performs preliminary drying of wet waste materials during the initial heating phase before pyrolysis and combustion occur. This preliminary action removes moisture that would otherwise interfere with efficient thermal decomposition, eliminating the need for separate drying equipment while improving overall energy efficiency by preparing the waste in-situ.

Inventive Principle:
Principle #10Preliminary action

4Quantity of substance

If pyrolysis is used to convert MSW, then syngas production is improved, but waste sorting to remove unsuitable materials is required

Engineering Contradiction:
Improvesyngas productionVSAvoidwaste sorting
Core Design Contradiction:
Quantity of substanceVSEase of operation

Solution Approach 1:

The process uses parameter changes in temperature (progressing from 100°C to 900°C) and oxygen availability (controlled atmosphere) to selectively promote syngas-producing reactions while naturally excluding materials that cannot contribute to syngas formation. These parameter changes create conditions where only organic materials undergo beneficial thermal decomposition, while inorganic materials are automatically separated as non-combustible residue, eliminating the need for pre-sorting.

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

The system effectively converts MSW into a green energy source with reduced volume and greenhouse gas emissions, achieving a 95% reduction in waste volume and emissions, and utilizing heat for electricity production.

Implementation Method 1

engaging an oil/gas burner to begin the thermal decomposition process; providing heated air from the burner through an attached pipe into the lower portion of the reactor vessel

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 2

thermal decomposition of MSW; the thermal decomposition process; continuing the thermal conversion of the solid waste feedstock

Methodology Applied
Scientific EffectThermal decomposition: Pyrolysis

Implementation Method 3

injecting water through atomizing nozzles to produce a water gas shift reaction

Methodology Applied
Scientific EffectWater gas shift reaction: Chemical Transport Reactions

Implementation Method 4

injecting water into the holding canister so that it flashes into steam and flows onto the solid waste feedstock; injecting water through larger nozzles into the reactor vessel sufficient to quench thermal conversion

Methodology Applied
Scientific EffectFlash evaporation: Flash Evaporation

Implementation Method 5

The hot oil system can circulate oil through two heat exchangers: one at the thermal processing chamber absorbing heat, and a second heat exchanger which can be an organic Rankine cycle, steam generator, water evaporator

Methodology Applied
Scientific EffectHeat transfer: Heat Exchanger

Implementation Method 6

generate steam to drive electricity producing turbines

Methodology Applied
Scientific EffectSteam turbine: Turbine

Data Source

PatentEP3928031B1Method and system for the thermal decomposition solid waste
Publication Date: 2024.04.03 DECKER EARL
  • EP3928031B1 patent drawingFigure 1A~1B
  • EP3928031B1 patent drawingFigure 1C~1D
  • EP3928031B1 patent drawingFigure 1E

AI summary

A reactor system made up of a single canister or a plurality of separate canister sections for the advanced thermal chemical conversion processing of municipal solid waste ("MSW"), either sorted or unsorted, and autoclaves specially designed to process the waste at suitable temperature and pressure combinations is disclosed. The canister sections can be individually and separately filled with compressed bales of MSW or with selected loose MSW. A method of processing MSW, either sorted or unsorted, which can be carried out through the use of canisters to hold the waste feedstock, and autoclaves specially designed to process the waste at suitable temperature and pressure combinations is also disclosed. The reactor system can produce syngas that has an enhanced BTU value, typically between about 300 to 700 BTU/ft3. The remainder solid waste material generally amounts to approximately 5% of the original MSW volume. This material can then be sorted for metals with the balance being sent to a landfill or other recycling processes depending on its composition.