Catalyst Cooler Decouples Regeneration Temperature

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Solution Overview

Problem

In endothermic catalytic reactions such as paraffin dehydrogenation and fluid catalytic cracking, maintaining optimal catalyst residence time in the reactor is challenging due to the dependence on regeneration temperature, leading to increased thermal cracking and catalyst deactivation.

Innovation Solution

Cooling the regenerated catalyst before it is fed to the reactor decouples catalyst residence time from regeneration temperature, allowing for independent control of reactor conditions and minimizing undesirable cracking reactions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If increased regeneration temperature is used to provide additional heat to the reaction, then catalytic activity is improved, but thermal cracking reactions increase and catalyst deactivation accelerates

Engineering Contradiction:
Improveregeneration temperatureVSAvoidthermal cracking reactions
Core Design Contradiction:
TemperatureVSObject-generated harmful factors

Solution Approach 1:

The process separates the heat provision function from the catalytic reaction function by introducing a dedicated heat exchanger unit. The regenerated catalyst is cooled in the heat exchanger before entering the reactor, decoupling the regeneration temperature from the reaction temperature. This allows independent optimization of both parameters.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A heat exchanger is introduced as an intermediary component between the regenerator and reactor. This intermediary device transfers heat from the regenerated catalyst to a heat transfer medium, thereby cooling the catalyst before it contacts the feedstock in the reactor, preventing thermal cracking while maintaining high regeneration temperatures.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Use of energy by moving object

If increased regeneration temperature is used to drive endothermic reaction, then heat supply is improved, but catalyst residence time increases leading to deactivation

Engineering Contradiction:
Improveheat supply to reactionVSAvoidcatalyst residence time
Core Design Contradiction:
Use of energy by moving objectVSDuration of action of moving object

Solution Approach 1:

The process divides the catalyst circulation loop into distinct functional zones: regeneration at high temperature, cooling in the heat exchanger, and reaction at controlled temperature. This segmentation allows the catalyst to be exposed to high temperatures only during regeneration, minimizing residence time at elevated temperatures that cause deactivation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The catalyst is cooled in the heat exchanger before entering the reactor, performing the cooling action in advance. This preliminary cooling prevents the catalyst from introducing excessive heat to the reaction zone, thereby controlling residence time and reducing deactivation while maintaining efficient heat supply during the brief reaction period.

Inventive Principle:
Principle #10Preliminary action

3Productivity

If higher regenerated catalyst temperature is used to increase reaction heat, then catalytic activity is enhanced, but selectivity to desired products decreases

Engineering Contradiction:
Improvereaction rateVSAvoidproduct selectivity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The process separates the catalytic activation function (achieved at high regeneration temperature) from the selective reaction function (performed at controlled reaction temperature). The heat exchanger enables this separation by cooling the catalyst before reaction, ensuring high selectivity while maintaining productivity through efficient heat transfer.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process changes the temperature parameter of the catalyst dynamically: high temperature during regeneration to maximize activity, then rapid cooling via the heat exchanger to optimal reaction temperature for selectivity. This parameter change is achieved through the heat exchanger, allowing independent control of regeneration and reaction conditions.

Inventive Principle:
Principle #35Parameter changes

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 enables a shorter catalyst residence time in the reactor while maintaining high regeneration temperatures, thereby enhancing catalyst activity and reducing deactivation, with minimal impact on fuel requirements and maintaining constant conversion rates.

Implementation Method 1

cooling the regenerated catalyst in a catalyst cooler before the cooled regenerated catalyst is fed to the reactor

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

The catalyst may be regenerated in a catalyst regenerator by combusting coke from the catalyst in the presence of oxygen

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 3

Dehydrogenation is an endothermic reaction which requires external heat to drive the reaction to completion

Methodology Applied
Scientific EffectEndothermic reaction: Endothermic Reaction

Data Source

PatentUS20230133426A1Process and apparatus for reacting feed with cooled regenerated catalyst
Publication Date: 2023.05.04 UOP LLC
  • US20230133426A1 patent drawing
  • US20230133426A1 patent drawing
  • US20230133426A1 patent drawing

AI summary

A fluidized catalytic reactor decouples the catalyst regenerator temperature from the catalyst reactor residence time. Regenerated catalyst is cooled before it contacts reactant feed. The regenerated catalyst may be cooled by heat exchange with oxygen supply gas, spent catalyst or other materials. The process and apparatus are especially useful for fluidized endothermic catalytic reactions.