Pyrolysis Reactor Layout for Fast Oil Yield With Moist Feedstock

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Solution Overview

Problem

Existing pyrolysis systems for converting biomass and hydrocarbons to pyrolysis products face inefficiencies in pyrolysis time and product yield, particularly in the production of pyrolysis oils, due to the presence of moisture in the feedstock and the need for additional fuel sources.

Innovation Solution

A pyrolysis reactor system utilizing an oxygen-free environment, a dual-reactor configuration with angled segments, and a combination of non-catalytic particulate material for heating and grinding, along with a dual-condensation system to rapidly pyrolyze biomass feedstock and maximize pyrolysis oil production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional pyrolysis systems are used with moisture-containing feedstock, then the pyrolysis process can proceed, but the pyrolysis time increases and heat loss increases due to moisture evaporation

Engineering Contradiction:
Improvepyrolysis timeVSAvoidheat loss
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The reactor is divided into multiple segments with different functions: a drying section to remove moisture, a pyrolysis section for rapid conversion, and a combustion section for heat generation. This segmentation allows moisture to be removed separately from the pyrolysis process, preventing heat loss during evaporation while maintaining rapid pyrolysis times.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system performs preliminary drying of the feedstock before it enters the main pyrolysis zone. By removing moisture in advance through the drying section, the subsequent pyrolysis process occurs faster with less heat loss, as the feedstock already has reduced moisture content when entering the high-temperature zone.

Inventive Principle:
Principle #10Preliminary action

2Productivity

If conventional pyrolysis systems are used, then biomass can be converted to pyrolysis products, but additional fuel sources are required and pyrolysis oil yield is reduced

Engineering Contradiction:
Improvepyrolysis oil productionVSAvoidfuel source requirement
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The system uses the char produced during pyrolysis as a fuel source to generate heat for the process. The combustion section burns char to produce heat that feeds back into the pyrolysis section, creating a self-sustaining thermal cycle that eliminates the need for external fuel sources and improves pyrolysis oil yield.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

Instead of discarding char as waste, the system recovers and utilizes it as a fuel source. The combustion section processes char to generate heat, transforming a previously wasted product into a valuable energy source that supports the overall pyrolysis process and increases oil production.

Inventive Principle:
Principle #34Discarding and recovering

3Loss of time

If rapid pyrolysis is implemented to reduce pyrolysis time, then heat loss is minimized, but the system complexity increases due to dual-reactor configuration

Engineering Contradiction:
Improvepyrolysis timeVSAvoidreactor configuration
Core Design Contradiction:
Loss of timeVSDevice complexity

Solution Approach 1:

The system combines multiple functions into integrated reactor sections: the drying, pyrolysis, and combustion functions are merged into a single continuous reactor system with different zones. This integration allows rapid pyrolysis to occur while minimizing heat loss, and the modular design reduces overall system complexity compared to separate dual-reactor configurations.

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 system achieves rapid pyrolysis times of less than 2 seconds, resulting in increased pyrolysis oil production by minimizing moisture-driven heat loss and utilizing char as a fuel source, thereby enhancing the efficiency and yield of pyrolysis products.

Implementation Method 1

a combination of non-catalytic particulate material for heating and grinding

Methodology Applied
Scientific EffectMechanical impact: Impact Force

Implementation Method 2

non-catalytic particulate material for heating and grinding

Methodology Applied
Scientific EffectThermal energy transfer: Conduction (thermal)

Implementation Method 3

a dual-condensation system to rapidly pyrolyze biomass feedstock

Methodology Applied
Scientific EffectRapid cooling: Cooling

Implementation Method 4

dual-condensation system to rapidly pyrolyze biomass feedstock and maximize pyrolysis oil production

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 5

Pyrolysis is a process wherein organic material is heated at high temperatures in an oxygen-free environment

Methodology Applied
Scientific EffectOxygen-free environment: Physical Containment

Implementation Method 6

utilizing char as a fuel source

Methodology Applied
Scientific EffectCombustion: Combustion

Data Source

PatentUS12480055B2Pyrolysis reactor system and method
Publication Date: 2025.11.25 DUKE TECHNOLOGIES LLC
  • US12480055B2 patent drawing
  • US12480055B2 patent drawing
  • US12480055B2 patent drawing

AI summary

A system and method for the pyrolysis of a pyrolysis feedstock utilizes a pyrolysis reactor having a pyrolysis conduit and a solids return conduit segment. Each segment is configured with an outlet and an inlet to receive and discharge solid materials that are circulated through the reactor through the different segments. A solids conveyor is disposed within the pyrolysis conduit segment to facilitate conveying solid materials from the solids inlet upward through the pyrolysis conduit segment toward the solids discharge outlet. A pyrolysis feedstock is introduced into the pyrolysis reactor and at least a portion of the feedstock is converted to pyrolysis gases within the pyrolysis conduit segment, which are discharged through a gas outlet. An eductor condenser unit with an eductor assembly having a venturi-restricted flow path for receives a pressurized coolant fluid. A second flow path for receiving the discharged pyrolysis gases intersects the venturi-restricted flow path so that the received pyrolysis gases are combined with the coolant fluid and are discharged together to a mixing chamber that is used to condense pyrolysis gases.