Downflow Gasifier Nozzle Layout for Slag Blockage Prevention

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Solution Overview

Problem

Existing coal gasification systems face issues with slag accumulation and temperature excursions due to uneven fluid cinder fall and high-temperature erosion, leading to equipment breakdown and safety concerns, especially in large-scale production.

Innovation Solution

A carbonaceous substance gasification system that utilizes a gas return device to cool and purify synthesis gas, incorporating a bottom cooling purify part with an aerostatic press machine to raise pressure and use cooled gas as a cooling material, and a cooling down reaction part to improve carbon conversion and hydrogen-carbon ratio, while arranging nozzles for efficient gas flow and reaction.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If multiple nozzles gasifiers utilize synthesis gas up-flowing process to expand scale, then productivity increases, but fluid cinder concretes and blocks the cinder exit due to temperature drop

Engineering Contradiction:
Improvegasification capacityVSAvoidcinder exit blockage
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent inverts the conventional up-flowing process by implementing a down-flowing synthesis gas process. The synthesis gas flows downward through the gasifier chamber, carrying fluid cinder to the bottom where it is discharged. This reversal prevents temperature drop and concretation in the upper chamber, eliminating cinder exit blockage while maintaining expanded productivity through multiple nozzles.

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

Solution Approach 2:

The patent changes the flow direction parameter of synthesis gas from upward to downward. This parameter change fundamentally alters the temperature distribution and fluid cinder behavior within the chamber, preventing concretation and ensuring reliable cinder discharge while supporting large-scale operation.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If nozzles are arranged on the upper chamber to fully utilize space, then productivity increases, but high temperature gas erodes the top of the chamber causing safety issues

Engineering Contradiction:
Improvespace utilizationVSAvoidchamber erosion
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent inverts the flow direction to downward, which reverses the erosion pattern. Instead of high-temperature gas and fluid cinder eroding the upper chamber, the downward flow directs these erosive elements toward the bottom chamber where they are discharged. This protects the upper chamber structure while maintaining full space utilization for multiple nozzles.

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

3Use of energy by moving object

If cooling material is sprayed to lower temperature, then heat efficiency improves, but energy and water consumption increase

Engineering Contradiction:
Improveheat efficiencyVSAvoidcooling consumption
Core Design Contradiction:
Use of energy by moving objectVSLoss of energy

Solution Approach 1:

The patent implements a self-service cooling system where the down-flowing synthesis gas itself serves as the cooling medium. The hot synthesis gas cools itself and the surrounding structures through its downward flow and contact with chamber walls, eliminating the need for external cooling materials. This achieves effective temperature control while avoiding additional energy and water consumption.

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The synthesis gas acts as an intermediary cooling medium between the reaction zone and the environment. Instead of introducing external cooling materials, the system uses the synthesis gas itself to transfer heat away from the reaction zone, achieving cooling efficiency without the penalties of external cooling systems.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 enhances heat efficiency, reduces energy and water consumption, prevents slag blockages, minimizes ash and humidity, and improves carbon conversion, thereby increasing the hydrogen-carbon ratio and maintaining equipment safety.

Implementation Method 1

the low temperature humid synthesis gas which has been cooled is raised its pressure and fed into the primary cooling device

Methodology Applied
Scientific EffectPressure increase: Pressurisation

Implementation Method 2

the low temperature humid synthesis gas which has been cooled is raised its pressure and fed into the primary cooling device, then it can be used as the cooling material to lower the temperature of the up going crude synthesis gas

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 3

Purifying is realized mainly by utilizing gravity, inertial force to separate the gas and particles

Methodology Applied
Scientific EffectGravity separation: Gravitation

Implementation Method 4

Purifying is realized mainly by utilizing gravity, inertial force to separate the gas and particles

Methodology Applied
Scientific EffectInertial force: Inertia

Implementation Method 5

the carbonaceous substance and the gasifying agent react in the gasification reaction part, generate the crude synthesis gas

Methodology Applied
Scientific EffectGasification reaction: Chemical Bonding

Data Source

PatentEP3075819B1Carbonaceous substance reaction system and method
Publication Date: 2021.05.05 CHANGZHENG ENG
  • EP3075819B1 patent drawingFigure 1~2

AI summary

A carbonaceous substance powder gasification system and gasification method. The system comprises a carbonaceous substance reaction apparatus and a gas return apparatus used for raising the pressure of some of a raw syngas cooled and preliminarily purified downstream of the reaction apparatus, then blending with high-temperature raw syngas upstream of the reaction apparatus and reducing the temperature. The method comprises reacting in a gasification reaction apparatus the carbonaceous substance and a gasification agent to generate raw syngas and ash and slag, some of the high-temperature raw syngas moving downstream with fly ash and liquid slag, and some of the high-temperature syngas moving upstream with fly ash; the downstream part of the high-temperature raw syngas being cooled, preliminarily purified and deslagged, then pressurized, and the wet raw syngas being injected into the system and blended with the upstream high-temperature raw syngas; the remainder of the high-temperature syngas moving upstream with fly ash and blending and cooling with the low-temperature wet syngas injected by the preliminary cooler, and optionally being entered into the cooling reaction stage; the cooled or cooling-reacted raw syngas continuing upstream, passing through the upper cooling stage and cooling again and ash being removed to obtain the raw syngas substance.