Countercurrent Oxygen Torrefaction for Biomass Energy

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current torrefaction processes for biomass are energy inefficient, require high energy for grinding torrefied material into a fine powder, and result in low heating value, making it difficult to use in existing fossil fuel-based power plants and gasification systems without significant modifications.

Innovation Solution

A counter-current oxygen-enhanced torrefaction process where torrefaction gases are condensed onto the biomass, increasing energy and heating value, and oxygen is injected downstream to raise temperatures, reducing the energy needed for milling and torrefaction time.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If conventional torrefiction is performed in an inert atmosphere, then biomass is torrefied, but energy yield is low and heating value is low

Engineering Contradiction:
Improveenergy yieldVSAvoidheating value
Core Design Contradiction:
Loss of energyVSUse of energy by moving object

Solution Approach 1:

The patent applies this principle by capturing the volatile gases released during torrefaction (which would normally be wasted) and condensing them back onto the torrefied biomass. This converts the harmful loss of energy through gas release into a beneficial recovery process, increasing both energy yield and heating value of the final product.

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

Solution Approach 2:

The patent implements this principle by discarding the conventional approach of venting torrefaction gases to atmosphere and instead recovering these gases through condensation. The volatile compounds that would be discarded are now captured and returned to the biomass, improving energy retention and overall process efficiency.

Inventive Principle:
Principle #34Discarding and recovering

2Adaptability or versatility

If torrefied biomass is ground into fine powder for use in existing power plants, then it can be used in pulverized coal power plants, but energy consumption for milling is high

Engineering Contradiction:
Improvecompatibility with existing power plantsVSAvoidenergy for milling
Core Design Contradiction:
Adaptability or versatilityVSUse of energy by moving object

Solution Approach 1:

The patent applies this principle by changing the physical and chemical parameters of the biomass through oxygen-enhanced torrefaction at optimized temperatures (200-400°C). This modifies the biomass structure to achieve better grindability and flow characteristics, reducing the energy required for milling while maintaining compatibility with existing power plant equipment.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces controlled oxygen during the torrefaction process to accelerate oxidation reactions. This enhances the torrefaction efficiency and improves the physical properties of the torrefied biomass, making it more suitable for pulverization and reducing subsequent milling energy requirements while maintaining adaptability to existing power plants.

Inventive Principle:
Principle #38Strong oxidants (Accelerated oxidation)

3Temperature

If torrefiction temperature is increased to improve heating value, then energy density increases, but torrefiction time must be extended and reactor size increases

Engineering Contradiction:
Improvetorrefiction temperatureVSAvoidtorrefiction time
Core Design Contradiction:
TemperatureVSLoss of time

Solution Approach 1:

The patent introduces controlled oxygen during torrefaction to accelerate the thermal decomposition and oxidation reactions. This allows achieving the desired heating value and energy density at lower temperatures and shorter residence times compared to conventional inert atmosphere torrefaction, thus reducing reactor size and processing time.

Inventive Principle:
Principle #38Strong oxidants (Accelerated oxidation)

Solution Approach 2:

The patent implements continuous torrefiction with controlled oxygen supply, maintaining optimal reaction conditions throughout the process. This continuous action with enhanced oxidation ensures efficient energy density improvement without requiring extended processing times or oversized reactors.

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 process significantly reduces the energy required for milling torrefied biomass into a fine powder by 60%, increases energy and heating value, and allows for more efficient use in existing power plants and gasification systems, while also decreasing torrefaction time and reactor size.

Implementation Method 1

torrefiction gases released during the torrefiction reaction are condensed onto the biomass

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 2

torrefiction gases released during the torrefiction reaction are condensed onto the biomass thereby increasing the energy and heating value

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 3

oxygen reacts with components of the torrefiction gases under the formation of heat

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 4

oxygen reacts with components of the torrefiction gases under the formation of heat

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Data Source

PatentEP2710097B1Countercurrent oxygen enhanced torrefaction
Publication Date: 2019.12.11 BIOENDEV
  • EP2710097B1 patent drawingFigure 1
  • EP2710097B1 patent drawingFigure 2a
  • EP2710097B1 patent drawingFigure 2b

AI summary

The invention relates to a method of torrefaction of an optionally predried biomass in a torrefaction reactor such that torrefied biomass and torrefaction gases are obtained, and wherein an oxygen-containing gas is supplied to the torrefaction reactor at a first position in the reactor such that oxygen reacts with components of the torrefaction gases under the formation of heat and wherein torrefaction gases are withdrawn from the torrefaction reactor at a second position of the torrefaction reactor and wherein the first position is located downstream of the second position in relation to a biomass transport direction in the torrefaction reactor such that the torrefaction gases moves through the torrefaction reactor countercurrent with the biomass transport and wherein the optionally predried biomass has a temperature of between 30 °C and 230 °C, preferably between 50 °C and 200 °C, most preferably between 60 °C and 180 °C when entering the torrefaction rector.