Fluidized Bed Reactor Gas Rotation for Caking Prevention

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Solution Overview

Problem

Caking and uneven distribution of solids in fluidized bed reactors during exhaust gas cleaning processes lead to reduced material contact, deposition of harmful gases, and operational disruptions, particularly due to improper nozzle design and water spray distribution.

Innovation Solution

Introducing a rotational movement of gas and solids within the fluidized bed reactor using multiple nozzles with guide vanes, which creates a uniform rotation along the flow axis, reducing solid sedimentation and caking, and allowing for efficient recirculation of up to 99% of the sorbent.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If water spray is used to clean deposits in the fluidized bed reactor, then cleaning effect is improved, but deposits form unevenly and clog nozzles and feed lines

Engineering Contradiction:
Improvecleaning effectVSAvoidnozzle clogging
Core Design Contradiction:
Ease of operationVSReliability

Solution Approach 1:

The patent introduces a rotational movement of the gas stream within the fluidized bed reactor, transforming the static fluidized bed into a dynamic system. This rotation prevents uniform deposit formation and clogging by continuously changing the flow patterns and particle distribution, thereby maintaining nozzle functionality while achieving cleaning effects.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The rotational gas stream creates dynamic mechanical motion within the reactor, which prevents deposits from settling uniformly on nozzle surfaces. This continuous motion disrupts the formation of clogging deposits while maintaining effective water spray cleaning throughout the reactor volume.

Inventive Principle:
Principle #18Mechanical vibration

2Quantity of substance

If solids loading is increased to prevent deposits, then material contact is improved, but uniform distribution of recirculating solids is disrupted

Engineering Contradiction:
Improvesolids loadingVSAvoiduniform distribution
Core Design Contradiction:
Quantity of substanceVSStability of the object's composition

Solution Approach 1:

By introducing rotational movement to the gas stream, the system dynamically redistributes solids throughout the reactor volume. This prevents localized accumulation while maintaining high overall solids loading, ensuring both improved material contact and uniform distribution of recirculating solids.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent extracts the gas stream from the conventional vertical flow path and redirects it through a tangential inlet, creating a separate rotational flow component. This extracted and redirected flow path enables independent control of solids distribution patterns, achieving uniform distribution even at high solids loading.

Inventive Principle:
Principle #2Taking out (Extraction)

3Device complexity

If conventional vertical gas flow is used, then simple reactor design is maintained, but deposits form on inner surfaces and operational stability decreases

Engineering Contradiction:
Improvereactor designVSAvoidoperational stability
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The patent modifies the reactor by introducing a tangential gas inlet that creates rotational flow. This dynamic flow pattern prevents deposit formation on inner surfaces by continuously moving particles and gas throughout the reactor, significantly improving operational stability without requiring complex additional components.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent transitions from a conventional one-dimensional vertical gas flow to a two-dimensional rotational flow pattern by introducing tangential inlet. This dimensional change creates spiral motion that effectively prevents deposit formation on reactor walls while maintaining design simplicity.

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 approach significantly reduces caking, ensures uniform solid distribution, maintains effective material contact, and prevents nozzle clogging, thereby enhancing the operational stability and efficiency of the fluidized bed reactor.

Implementation Method 1

the gas undergoes a rotation around the flow axis in the fluidized bed reactor

Methodology Applied
Scientific EffectRotational movement:

Implementation Method 2

circulating fluidized bed in which the flue gas comes into contact with the sorbent

Methodology Applied
Scientific EffectFluidized bed: Fluidisation

Implementation Method 3

A sorbent, such as hydrated lime or calcium oxide, is also injected into the fluidized bed reactor. The circulation of solids separated in a filter to the reactor creates a circulating fluidized bed in which the flue gas comes into contact with the sorbent, and pollutants are separated from the flue gas.

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Implementation Method 4

pollutants are separated from the flue gas

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 5

The flue gas, along with the separated reaction products and the sorbent, is routed from the fluidized bed reactor through a pipeline and dedusted in a downstream filter system with a solids separator.

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Data Source

PatentEP2744589B1Method and device for cleaning exhaust gases by way of fluidized bed reactors
Publication Date: 2019.01.23 FUJIAN LONJING ENVIRONMENT TECH CO LTD
  • EP2744589B1 patent drawingFigure 1
  • EP2744589B1 patent drawingFigure 2~3
  • EP2744589B1 patent drawingFigure 4~5

AI summary

The invention relates to a method for cleaning exhaust gases (1), in which an exhaust gas and a sorbent (4) are combined in a fluidized bed reactor (3). In a subsequent filter system (7), solid matter is segregated, and thereafter, up to 99 per cent of the sorbent is re-channeled (6) into the fluidized bed reactor, wherein the gas is subjected to a rotation around the flow axis in the fluidized bed reactor.