Two-Stage Pyrolysis for Waste Valorization

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Solution Overview

Problem

Existing pyrolysis methods for waste material only optimally extract biogenic combustible gases, leaving behind unutilized synthetic combustible gases and inefficiencies in energy and product quality.

Innovation Solution

A method involving two pyrolysis processes in series, one at a lower temperature for biogenic gas extraction and another at a higher temperature for synthetic gas extraction, followed by condensation and staggered condensation to separate and utilize both gas fractions effectively.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If a single pyrolysis process is used at low temperature, then biogenic gas extraction is optimized, but synthetic combustible gas remains unutilized and energy efficiency is reduced

Engineering Contradiction:
Improveenergy efficiencyVSAvoidgas extraction completeness
Core Design Contradiction:
Loss of energyVSProductivity

Solution Approach 1:

The single pyrolysis process is segmented into two sequential pyrolysis processes operating at different temperature ranges. The first pyrolysis process operates at low temperature (200-400°C) to optimally extract biogenic combustible gas, while the second pyrolysis process operates at high temperature (400-800°C) to extract synthetic combustible gas from the remaining solid material. This segmentation allows each process to be optimized for its specific gas type, eliminating energy waste from unutilized synthetic gas.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention changes the temperature parameter between two sequential pyrolysis processes. The first process uses low temperature (200-400°C) optimized for biogenic gas extraction, while the second process uses high temperature (400-800°C) optimized for synthetic gas extraction. This parameter change enables complete utilization of different gas fractions from the waste material, maximizing overall energy efficiency.

Inventive Principle:
Principle #35Parameter changes

2Quantity of substance

If pyrolysis is performed at low temperature only, then biogenic combustible gas is extracted, but product quality and calorific value are limited

Engineering Contradiction:
Improvegas volumeVSAvoidproduct quality
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The gas production process is segmented into two quality-differentiated streams. The first pyrolysis process at low temperature produces biogenic combustible gas with specific compositional characteristics, while the second pyrolysis process at high temperature produces synthetic combustible gas with different properties and higher calorific value. This segmentation allows each gas fraction to be optimized for its intended application, improving overall product quality.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

By changing the temperature parameter from low (200-400°C) to high (400-800°C) between the two pyrolysis processes, the invention produces gases with different compositional qualities. The high-temperature pyrolysis generates synthetic gas with higher calorific value and different hydrocarbon composition, thereby improving product quality while maintaining substantial gas volume through the combined output of both processes.

Inventive Principle:
Principle #35Parameter changes

3Loss of time

If waste material is not fully processed, then processing time is reduced, but valuable synthetic gas and pyrolytic crude oil are lost

Engineering Contradiction:
Improveprocessing timeVSAvoidvaluable product loss
Core Design Contradiction:
Loss of timeVSLoss of substance

Solution Approach 1:

The first pyrolysis process at low temperature serves as a preliminary action that extracts biogenic gas and prepares the solid residue for the second pyrolysis process. This preliminary extraction prevents potential loss of biogenic gas while the subsequent high-temperature pyrolysis recovers synthetic gas and pyrolytic crude oil that would otherwise be lost. The sequential arrangement ensures complete material utilization without excessive time investment.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The invention maintains continuity of useful action by immediately subjecting the solid residue from the first pyrolysis process to the second pyrolysis process at high temperature. This continuous processing ensures that no valuable synthetic gas or pyrolytic crude oil is lost, while the system operates efficiently without unnecessary idle time between processing stages.

Inventive Principle:
Principle #20Continuity of useful action

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 enables the complete extraction and separation of biogenic and synthetic combustible gases, optimizing energy efficiency and product quality, and achieving self-sufficiency in energy and material utilization.

Implementation Method 1

the pyrolysis technique is widely known and used, understood as a thermal decomposition in the absence of oxygen, of matter having a carbonaceous base

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 2

extracting the gas from pyrolysis, which can be subsequently used as fuel

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentUS20250135515A1Method for Valorization of Waste Material
Publication Date: 2025.05.01 GREENE ENTERPRISE SL
  • US20250135515A1 patent drawing

AI summary

A method for valorizing refuse material comprises a selective pyrolysis, based on: a first step of pyrolysis of the biogenic fraction, with at least one subsequent condensation step, and a second step of pyrolysis of the synthetic fraction with at least one subsequent condensation step; wherein the first and second pyrolysis steps are configured in series; wherein the first pyrolysis step is configured to extract at least a fraction of biogenic combustible gas which continues to the first condensation step, and a fraction of solid material that is transported to the second step of pyrolysis of the synthetic fraction, which is carried out at a higher temperature than the first pyrolysis step, and which is configured to obtain a fraction of synthetic combustible gas which continues to the second condensation step, and a fraction of solid material.