Biomass Pyrolysis Reactor With Cyclone Char Separation

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Solution Overview

Problem

Conventional biomass conversion methods, such as combustion, face issues with slagging and fouling due to low eutectic point ash and inefficiencies in removing smaller particulates using bag filters, necessitating an improved system for pyrolysis and gasification.

Innovation Solution

A pyrolysis and gasification system that includes a reactor operable in both gasification and pyrolysis modes, utilizing a feed hopper, cyclone assembly, and fluidized bed materials to produce synthesis gas and bio-char, with a method involving fluidization and controlled heating to manage temperature and maintain a fluidized condition, effectively removing bio-char and addressing slagging and fouling concerns.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Power

If conventional combustion methods are used for biomass conversion, then energy production is achieved, but slagging and fouling occur due to low eutectic point ash

Engineering Contradiction:
Improveenergy productionVSAvoidslagging and fouling
Core Design Contradiction:
PowerVSObject-affected harmful factors

Solution Approach 1:

The patent changes the thermal conversion parameters by using pyrolysis and gasification at controlled temperature ranges instead of conventional combustion. The system maintains temperatures below the eutectic point of ash-forming materials through controlled heating rates and oxygen limitation, transforming the harmful combustion process into a beneficial thermal decomposition process that prevents slagging while still producing energy.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent utilizes phase transitions of biomass components during pyrolysis, where organic matter decomposes into volatile gases and char at specific temperature ranges. This phase transition approach allows energy recovery through gasification while keeping the system temperature controlled to prevent ash melting and slag formation, resolving the contradiction between energy production and slagging prevention.

Inventive Principle:
Principle #36Phase transitions

2Loss of substance

If bag filters are used to remove char by filtration, then char removal is achieved, but smaller particulates are not effectively removed and filter media may be damaged

Engineering Contradiction:
Improvechar removalVSAvoidfilter performance and durability
Core Design Contradiction:
Loss of substanceVSReliability

Solution Approach 1:

The patent replaces the mechanical filtration system (bag filters) with a thermal field-based separation system. By controlling the temperature and oxygen concentration in the reactor, the system naturally separates particulates through thermal decomposition and gasification processes, eliminating the need for mechanical filters that are prone to damage and inefficient at removing fine particulates.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent employs fluidized bed technology where gas flow through the bed materials creates a fluid-like state that enhances mixing and heat transfer. This pneumatic approach allows for effective particulate removal through the fluidized bed dynamics and subsequent cyclone separation, replacing the problematic bag filter system with a more reliable gas-solid separation mechanism.

Inventive Principle:
Principle #29Pneumatics and hydraulics

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 efficient conversion of biomass into synthesis gas and bio-char, reducing slagging and fouling, and allows for a mobile, scalable, and sustainable thermal energy conversion process, suitable for a wide range of biomass feedstocks with low melting point ash, enhancing energy production and reducing operational inefficiencies.

Implementation Method 1

a reactor that is operable in a gasification mode or a pyrolysis mode. The reactor is configured to receive the biomass feedstock from the feed hopper. The reactor is operable to provide heat to the biomass feedstock from the feed hopper to produce the synthesis gas and bio-char

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 2

The reactor is operable in a gasification mode or a pyrolysis mode

Methodology Applied
Scientific EffectGasification:

Implementation Method 3

The produced synthesis gas having bio-char is fed to the cyclone assembly. The cyclone assembly removes bio-char from the synthesis gas

Methodology Applied
Scientific EffectCyclone separation: Cyclone Separation

Implementation Method 4

The reactor includes bed materials. The method includes introducing a fluidizing medium to the bed materials to fluidize the bed materials and to produce a fluidized condition

Methodology Applied
Scientific EffectFluidization: Fluidisation

Data Source

PatentUS11186779B2Devices and methods for a pyrolysis and gasification system for biomass feedstock
Publication Date: 2021.11.30 TEXAS A&M UNIVERSITY
  • US11186779B2 patent drawing
  • US11186779B2 patent drawing
  • US11186779B2 patent drawing

AI summary

A pyrolysis and gasification system produce a synthesis gas and bio-char from a biomass feedstock. The system includes a feed hopper that has a flow measurement device. The system also includes a reactor that is operable in a gasification mode or a pyrolysis mode. The reactor is configured to receive the biomass feedstock from the feed hopper. The reactor is operable to provide heat to the biomass feedstock from the feed hopper to produce the synthesis gas and bio-char. The system also includes a cyclone assembly. The produced synthesis gas including the bio-char is fed to the cyclone assembly. The cyclone assembly removes a portion of the bio-char from the synthesis gas.