Ascending Cocurrent Gasifier for Low-Tar Solid Fuel Conversion

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Solution Overview

Problem

Existing thermochemical gasification processes for solid fuels face challenges such as high tar content in product gases, complex plant technology, and inefficiency in small and medium-sized plants, leading to high operational costs and equipment wear.

Innovation Solution

A single-stage ascending cocurrent gasification process where fuel is fed against gravity, and a gasification medium and product gas flow in the same direction, forming a stationary fluidized bed in the reduction zone without additional fluidizing means, allowing for simultaneous pyrolysis and coke gasification in a fixed bed, reducing tar content and eliminating the need for mechanical separation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If fluidized-bed gasifiers are used to improve gasification efficiency, then productivity increases, but device complexity and tar content increase requiring additional purification equipment

Engineering Contradiction:
Improvegasification efficiencyVSAvoidplant technology complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The gasifier is divided into three distinct zones (oxidation zone, reduction zone, combustion zone) arranged vertically, with each zone performing a specific function. This segmentation allows efficient gasification while maintaining simpler operation compared to complex fluidized-bed systems

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent uses ascending cocurrent flow where fuel, gasification medium, and product gas all move upward together, opposite to conventional descending counter-current systems. This inversion simplifies the system by eliminating the need for complex mechanical installations while maintaining high efficiency

Inventive Principle:
Principle #13The other way round (Inversion)

2Productivity

If counter-current gasifiers are used to improve gasification efficiency, then productivity increases, but tar content in product gas increases making them unsuitable for small and medium-sized plants

Engineering Contradiction:
Improvegasification efficiencyVSAvoidtar content
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent inverts the conventional counter-current design by implementing ascending cocurrent flow where all streams move upward together. This fundamental inversion transforms the process to produce low-tar gas suitable for small and medium-sized applications while maintaining high gasification efficiency

Inventive Principle:
Principle #13The other way round (Inversion)

Solution Approach 2:

Different zones within the gasifier have specialized functions: the oxidation zone handles combustion, the reduction zone performs gasification with controlled tar formation, and the combustion zone completes the process. This local specialization ensures high efficiency while minimizing tar content through optimized zone-specific conditions

Inventive Principle:
Principle #3Local quality

3Device complexity

If ascending cocurrent gasifiers with fuel fed from below are used to simplify the process, then device complexity decreases, but channel and bridge formation occurs increasing tar content

Engineering Contradiction:
Improvestructural simplicityVSAvoidtar content
Core Design Contradiction:
Device complexityVSObject-generated harmful factors

Solution Approach 1:

Instead of feeding fuel from below as in conventional ascending gasifiers, this patent feeds fuel from the top and uses ascending cocurrent flow. This inverted approach prevents channel and bridge formation while maintaining structural simplicity and producing low-tar gas

Inventive Principle:
Principle #13The other way round (Inversion)

Solution Approach 2:

The continuous upward flow of gasification medium and product gas through the fuel bed ensures constant movement and mixing, preventing the formation of channels and bridges. This continuous action maintains structural simplicity while eliminating tar-related problems

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 results in a low-tar, high-efficiency gas production with reduced structural complexity and wear, suitable for small to medium-sized systems, and eliminates the need for costly gas purification and complex ash discharge systems.

Implementation Method 1

Pyrolysis and reduction thus take place simultaneously throughout the upper bed

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 2

Method for thermochemically gasifying solid fuels

Methodology Applied
Scientific EffectGasification:

Implementation Method 3

the fuel is fed into a gasification chamber against the force of gravity

Methodology Applied
Scientific EffectGravity: Gravitation

Implementation Method 4

a gasification medium and the resulting product gas flow through it in the same direction

Methodology Applied
Scientific EffectConvection: Convection

Data Source

PatentEP2356200B1Method for thermochemically gasifying solid fuels
Publication Date: 2017.12.27 BURKHARDT GMBH
  • EP2356200B1 patent drawingFigure 1
  • EP2356200B1 patent drawingFigure 2

AI summary

The invention relates to a single-step method for thermochemically gasifying solid fuels (8) according to the principle of rising cocurrent gasification, wherein a fuel (8) is fed to a gasification chamber (3) against the force of gravity, a gasification medium (16) is added to the fuel in cocurrent flow, and a resulting product gas (14) is discharged in cocurrent flow. The fuel (8) is continuously fed to the gasification chamber (3), and the gasification medium (16) is fed from below through the fed fuel (8) to an oxidation zone (10) formed as a layer. The amount of the gasification medium (16) fed is adjusted by a control unit (15) in such a way that a stationary fluidized bed (17) is formed in a reduction zone (11) above the oxidation zone (10). In a corresponding gasifier (1), the fuel feed (2) is designed for continuous or quasi-continuous fuel supply, and the feed (6) for the gasification medium (16) is arranged below reaction zones (9, 10, 11) formed as layers in the gasification chamber (3). The fuel (8) forms a distributor floor for the gasification medium (16) in order to achieve a fluidized bed (17).