Solids Feeder Discharge Port Design for Flow Stability

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Solution Overview

Problem

Pneumatic conveying systems experience time-varying fluctuations in solids flow rate due to flow separation and agglomeration, leading to poor gasifier performance and inconsistent power generation in IGCC systems.

Innovation Solution

The improved solids feeder incorporates a discharge port design with a reduced cross-sectional area and transitional sections to increase conveying gas velocity, break up agglomerates, and enhance mixing, along with optional features like moveable plates and agitators to maintain a steady flow rate.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Stability of the object's composition

If conventional discharge port design is used, then device complexity is low, but solids flow rate stability deteriorates due to flow separation and agglomeration

Engineering Contradiction:
Improvesolids flow rate stabilityVSAvoiddischarge port structure complexity
Core Design Contradiction:
Stability of the object's compositionVSDevice complexity

Solution Approach 1:

The discharge port is divided into multiple sections with different cross-sectional areas (reduced cross-sectional area section and transitional section), allowing the conveying gas to undergo progressive acceleration and mixing stages, which stabilizes solids flow rate by preventing sudden flow separation and agglomeration

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different sections of the discharge port are designed with locally optimized properties: the reduced cross-sectional area section creates high velocity zones to break agglomerates, while the transitional section provides gradual area change to maintain flow stability, addressing flow separation issues at specific locations

Inventive Principle:
Principle #3Local quality

2Stability of the object's composition

If conveying gas velocity is increased to break agglomerates, then solids flow rate stability improves, but energy consumption increases

Engineering Contradiction:
Improvesolids flow rate stabilityVSAvoidconveying gas energy consumption
Core Design Contradiction:
Stability of the object's compositionVSUse of energy by moving object

Solution Approach 1:

The discharge port incorporates curved transitional sections instead of sharp angles, allowing conveying gas to smoothly accelerate through the reduced cross-sectional area and mix with solids. This curved geometry maintains high velocity for aggregate breaking while minimizing energy loss from abrupt flow changes, achieving solids flow stability with reduced energy consumption

Inventive Principle:
Principle #14Spheroidality (Curvature)

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 solution ensures a smoother and more consistent solids flow, reducing fluctuations and improving gasifier performance by preventing agglomeration and maintaining high gas velocity, thus enhancing overall power plant efficiency.

Implementation Method 1

a discharge port in communication with the outlet channel, the discharge port comprising: a reduced cross-sectional area section; and a transitional section

Methodology Applied
Scientific EffectGas velocity increase through reduced cross-sectional area: Venturi Effect

Data Source

PatentEP2632832B1Solids feeder
Publication Date: 2018.04.11 GENERAL ELECTRIC CO
  • EP2632832B1 patent drawingFigure 1
  • EP2632832B1 patent drawingFigure 2~4
  • EP2632832B1 patent drawingFigure 5~7

AI summary

The present application provides a solids feeder in communication with a flow of solids and a flow of a conveying fluid. The solids feeder may include an outlet channel with the flow of the solids therein and a discharge port in communication with the outlet channel. The discharge port further may include an inlet in communication with the flow of the conveying fluid and a flow channel. The flow channel may include a reduced cross-sectional area about the outlet channel as compared to the inlet.