Plasma Gasifier Quench Zone for Syngas Particle Control

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Solution Overview

Problem

Existing plasma gasifiers face challenges in minimizing the number of unreacted particles exiting the reactor, which can deposit on external ductwork, affecting efficiency and increasing operational costs.

Innovation Solution

A plasma gasifier process with a carbonaceous bed in the bottom section, middle section feed ports angled to promote uniform feed distribution, and a top section quench zone with injected quench fluid (water or steam) to partially quench unreacted particles, reducing their likelihood of exiting as molten or sticky deposits.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If the reactor operates at high temperature to promote gasification reactions, then the gasification efficiency is improved, but unreacted particles are more likely to exit as molten or sticky deposits on ductwork

Engineering Contradiction:
Improvegasification efficiencyVSAvoidparticle deposition on ductwork
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The top section is divided into two distinct zones: a first lower part for continued gasification reactions and a second upper part (quench zone) for particle cooling. This segmentation allows the system to maintain high temperature in the reaction zone while providing a separate zone for quenching particles before they exit, thus resolving the contradiction between high gasification efficiency and preventing ductwork deposition

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A quench fluid (water or steam) is introduced as an intermediary substance in the second upper part of the top section. This quench fluid acts as a thermal mediator that rapidly cools unreacted particles through injection and mixing, transforming them from a molten/sticky state to a solidified state that can be effectively removed from the syngas stream before ductwork deposition occurs

Inventive Principle:
Principle #24Intermediary (Mediator)

2Object-generated harmful factors

If quench fluid is injected to cool unreacted particles, then particle deposition on ductwork is reduced, but energy is lost through cooling the syngas mixture

Engineering Contradiction:
Improveparticle deposition on ductworkVSAvoidenergy loss from syngas cooling
Core Design Contradiction:
Object-generated harmful factorsVSLoss of energy

Solution Approach 1:

The quench fluid injection is applied locally and selectively in the second upper part of the top section rather than throughout the entire reactor. This localized quenching approach targets only the unreacted particles that need cooling while minimizing the cooling of the bulk syngas mixture, thus reducing energy loss while still preventing ductwork deposition

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The quenching action is performed preliminarily within the reactor vessel before the syngas exits to the ductwork. By cooling and solidifying particles inside the reactor in the second upper part, the system prevents the harmful deposition problem from occurring in the external ductwork, avoiding the need for downstream energy-intensive particle removal systems

Inventive Principle:
Principle #10Preliminary action

3Stability of the object's composition

If feed material is fed into the middle section to form a deposited bed, then uniform feed distribution is achieved, but the reactor complexity increases with multiple feed ports and sections

Engineering Contradiction:
Improveuniform feed distributionVSAvoidreactor structure with multiple sections
Core Design Contradiction:
Stability of the object's compositionVSDevice complexity

Solution Approach 1:

The reactor employs asymmetric feed port configuration in the middle section with ports positioned at different locations and angles. This asymmetric arrangement creates a controlled feed material deposition pattern that promotes uniform distribution across the carbonaceous bed, achieving stable composition without requiring symmetric complexity throughout the entire reactor structure

Inventive Principle:
Principle #4Asymmetry

Solution Approach 2:

The feed material introduction is moved from the top section to the middle section, utilizing the vertical dimension strategically. By feeding into the middle section where material can deposit and redistribute under gravity and gas flow, the system achieves uniform distribution through a three-dimensional deposition process rather than requiring complex two-dimensional mixing mechanisms

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

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 configuration enhances syngas quality by minimizing unreacted particle deposition on ductwork, reducing operational and capital costs, and promoting more thorough gasification of feed materials.

Implementation Method 1

providing a plasma heated carbonaceous bed in a bottom section of a reactor vessel

Methodology Applied
Scientific EffectPlasma heating: Plasma

Implementation Method 2

reacting the feed material with hot gases rising from the bottom section

Methodology Applied
Scientific EffectThermal convection: Convection

Implementation Method 3

at least partially quenching, by injecting a quench fluid including water, steam, or a mixture thereof, in a second, upper part of the top section, at least some of the unreacted particles sufficiently to reduce the number of unreacted particles exiting the reactor vessel that are likely to be deposited on walls of external ductwork

Methodology Applied
Scientific EffectQuenching: Cooling

Data Source

PatentUS9540579B2Process for producing syngas using plasma gasifiers
Publication Date: 2017.01.10 ALTER NRG INT CORP
  • US9540579B2 patent drawing
  • US9540579B2 patent drawing
  • US9540579B2 patent drawing

AI summary

A process for gasification of solid feed material to produce a syngas includes: providing a plasma heated carbonaceous bed in a bottom section of a reactor vessel; forming a bed of deposited feed material on top of the carbonaceous bed; reacting the feed material with hot gases rising from the bottom section; forming, in a middle section of the reactor vessel, a syngas mixture containing a varying quantity of unreacted particles of the feed material; allowing the syngas mixture to rise into a top section of the reactor vessel; and at least partially quenching, by injecting a quench fluid including water, steam, or a mixture thereof, in a second, upper part of the top section, at least some of the unreacted particles sufficiently to reduce the number of unreacted particles exiting the reactor vessel that are likely to be deposited on walls of external ductwork.