Horizontal Fluidized Bed Reactor Cover Plate Design

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Solution Overview

Problem

Fluidized bed reactors face challenges with level variations and clogging issues due to fine particles, leading to increased energy expenditure and potential contamination, especially in long reactors, where continuous nozzle floors struggle to maintain uniform fluidization and prevent particle leakage.

Innovation Solution

A cover plate with nozzles and underflow weirs is introduced above the fluidized bed to create a back pressure, generating an 'air cushion' that reduces level differences and minimizes the fluidized bed inventory, using discrete or continuous nozzle trays to manage gas flow and particle distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Stability of the object's composition

If continuous nozzle floors are used to distribute fluidizing gas evenly, then uniform fluidization is achieved, but level variations cannot be compensated and flow resistance increases

Engineering Contradiction:
Improveuniform fluidizationVSAvoidflow resistance
Core Design Contradiction:
Stability of the object's compositionVSLoss of energy

Solution Approach 1:

The continuous nozzle floor is segmented into multiple discrete nozzle groups arranged in parallel. Each nozzle group serves a specific section of the fluidized bed, allowing independent optimization of gas distribution and level compensation in different regions while reducing overall flow resistance.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different nozzle groups are designed with locally optimized characteristics to compensate for level variations in specific regions. The nozzle orientation, diameter, and spacing are adjusted according to the local bed depth and flow requirements, enabling effective level compensation without increasing overall flow resistance.

Inventive Principle:
Principle #3Local quality

2Stability of the object's composition

If discrete nozzles are used to compensate level variations, then level compensation is achieved, but fine particles can pass through nozzles causing contamination

Engineering Contradiction:
Improvelevel compensationVSAvoidparticle leakage
Core Design Contradiction:
Stability of the object's compositionVSObject-affected harmful factors

Solution Approach 1:

A screen or mesh structure is introduced as an intermediary element between the discrete nozzles and the fluidized bed. This screen allows gas to pass through to the nozzles while blocking fine particles from entering the nozzle system, preventing contamination while maintaining level compensation capability.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The nozzle structure combines discrete nozzle elements with a porous or mesh-like supporting structure. This composite design enables the system to function both as a gas distribution device and as a particle filter, preventing fine particle leakage while maintaining effective level compensation.

Inventive Principle:
Principle #40Composite materials

3Use of energy by moving object

If fine particles are used for fluidized bed, then minimum fluidization conditions are achieved, but particles can pass through nozzles and clog the distribution plate

Engineering Contradiction:
Improveenergy efficiencyVSAvoidnozzle clogging
Core Design Contradiction:
Use of energy by moving objectVSReliability

Solution Approach 1:

A protective screen or filter structure is placed over the nozzle openings to act as an intermediary barrier. This screen prevents fine particles from entering and clogging the nozzles while allowing the gas flow to pass through unchanged, maintaining both energy efficiency and system reliability.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The nozzle design incorporates enlarged inlet openings or chamfered edges that create a protective zone before the particles can reach the critical nozzle opening. This geometric cushioning prevents particle ingress while maintaining the desired gas flow characteristics for energy-efficient operation.

Inventive Principle:
Principle #11Beforehand cushioning (Prior cushioning)

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 solution effectively reduces level variations, maintains a stable fluidized bed height, and prevents particle leakage, thereby optimizing energy efficiency and reducing operational pressures in fluidized bed reactors.

Implementation Method 1

Fluidized beds are suspensions of a solid particulate material in a fluidizing gas blown in from below, counteracting the force of gravity

Methodology Applied
Scientific EffectFluidization: Fluidisation

Implementation Method 2

a cover plate with nozzles and underflow weirs is introduced above the fluidized bed to create a back pressure, generating an 'air cushion' that reduces level differences

Methodology Applied
Scientific EffectPressure gradient: Pressure Gradient

Data Source

PatentEP3154673B1Fluidized bed reactor with horizontal direction
Publication Date: 2018.02.14 VIENNA UNIVERSITY OF TECHNOLOGY
  • EP3154673B1 patent drawingFigure 1
  • EP3154673B1 patent drawingFigure 2
  • EP3154673B1 patent drawingFigure 3

AI summary

The invention relates to a fluidized bed reactor which comprises a static fluidized bed (10) flowing in a horizontal direction and composed of bulk material, at least one windbox (1), and, arranged above the latter, a discrete or continuous nozzle base (2), which may comprise a multiplicity of nozzles, for generating and stabilizing the fluidized bed (10), which fluidized bed reactor is distinguished by the fact that, above the fluidized bed (10), over a part of the flow path thereof through the reactor, there is provided a cover plate (11) which bounds the rising fluidizing gas flow and in which at least one nozzle (12) is provided and at the two ends of which there is provided in each case one underflow weir (13) which runs transversely with respect to the flow direction of the fluidized bed.