Fluid Bed Regenerative Thermal Oxidizer Design

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Solution Overview

Problem

Fixed-bed regenerative thermal oxidizers (RTOs) face challenges with uneven airflow distribution, resulting in 'dead spaces' and inefficiencies, along with complex and costly valve systems, and the need for large ceramic saddles, which hinder effective pollutant treatment and heat transfer.

Innovation Solution

A fluid bed regenerative thermal oxidizer design featuring a vertical reactor stack with adsorber and desorber shelves, using small ceramic balls for heat exchange material that moves across shelves, eliminating the need for complex valves and large heat sinks, and ensuring uniform airflow distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If fixed-bed RTO design with large ceramic saddles is used, then heat transfer efficiency is reduced, but device complexity and construction costs are lowered

Engineering Contradiction:
Improveconstruction costVSAvoidheat transfer efficiency
Core Design Contradiction:
Ease of manufactureVSLoss of energy

Solution Approach 1:

The patent changes the size parameter of heat exchange material from large ceramic saddles to small ceramic particles (2-10mm diameter), fundamentally altering the heat transfer characteristics and eliminating dead spaces while maintaining manageable system complexity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces a fluidized bed system using upward gas flow to fluidize the ceramic particles, replacing the static fixed-bed mechanical structure with a dynamic pneumatic system that improves heat transfer without requiring complex valve assemblies

Inventive Principle:
Principle #29Pneumatics and hydraulics

2Reliability

If fixed-bed RTO design is used, then dead spaces and stratification occur, but device complexity is reduced

Engineering Contradiction:
Improvepollutant treatment effectivenessVSAvoidvalve system complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent transitions from a static fixed-bed structure to a dynamic fluidized bed where ceramic particles are suspended and mixed by upward gas flow, eliminating dead spaces and stratification effects that occur in static systems

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent replaces the complex mechanical valve system required for fixed-bed flow reversal with a simpler pneumatic control system that uses gas flow direction changes to achieve the same functional effect without mechanical moving parts

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

3Loss of energy

If small heat exchange particles are used, then heat transfer efficiency improves, but device complexity increases

Engineering Contradiction:
Improveheat transfer efficiencyVSAvoidsystem complexity
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

The patent uses pneumatic principles to fluidize and transport small ceramic particles through the system, replacing complex mechanical handling mechanisms with gas flow-based control that simplifies the overall system while maintaining high heat transfer efficiency

Inventive Principle:
Principle #29Pneumatics and hydraulics

Solution Approach 2:

The upward gas flow automatically fluidizes and circulates the small ceramic particles through the bed, eliminating the need for external mechanical agitation devices or complex control systems while maintaining optimal heat transfer conditions

Inventive Principle:
Principle #25Self-service

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 design enhances heat transfer efficiency by eliminating dead spaces and reducing construction and operation costs, while effectively treating pollutants by ensuring uniform airflow and efficient heat recovery.

Implementation Method 1

passing a hot gas stream over a heat sink material in one direction and recovering that heat by passing a cold gas stream through that same heat sink material

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

The heat sinks comprising such systems often comprise one or more beds of ceramic material configured to absorb heat from the exhaust gas, wherein the captured heat is then used to preheat an incoming process gas stream

Methodology Applied
Scientific EffectConvection: Convection

Implementation Method 3

combustion chamber located within the vertical reactor stack between the gas inlet and the gas outlet wherein the combustion chamber also comprises a fuel burner

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 4

decompose toxic gases and volatile organic compounds (VOCs) that are discharged in industrial process exhausts

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS20240369221A1Fluid bed regenerative thermal oxidizer and a method for its use
Publication Date: 2024.11.07 NESTEC INC
  • US20240369221A1 patent drawing
  • US20240369221A1 patent drawing
  • US20240369221A1 patent drawing

AI summary

The present device is a fluid bed regenerative thermal oxidizer configured to minimize dead spaces within it and eliminate the need for complex valve systems, which are typically required to move treated and untreated air across fixed beds. The present device can be a fluid bed regenerative thermal oxidizer comprising a vertical stack having a combustion chamber near its interior center and desorber shelves located within the vertical stack above the combustion chamber and adsorber shelves located within the vertical stack below the combustion shelves. Ceramic spheres can be used as heat sinks that flow from the desorber shelves, around the combustion chamber and onto the adsorber shelves and then back to the desorber shelves. In this way heat from the combustion can be captured by the heat exchange material on the desorber shelves and released to preheat untreated air on the adsorber shelves.