Catalyst Regeneration Zones with Independent Gas Loops

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Solution Overview

Problem

Current catalyst regeneration processes face challenges in controlling the combustion process, leading to catalyst deactivation and increased flue gas venting, due to limitations in oxygen concentration and inefficient carbon removal in the combustion zones.

Innovation Solution

A two-zone regeneration process is implemented, with independent regeneration gas streams for the upper and lower zones, allowing for controlled oxygen levels and extended residence times to achieve complete coke combustion, and a halogenation step to redistribute catalytic metal and dry the catalyst.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If a single combustion zone is used for catalyst regeneration, then the process is simpler to operate, but the oxygen concentration and combustion control are insufficient leading to incomplete coke removal and increased flue gas venting

Engineering Contradiction:
Improvecombustion controlVSAvoidregeneration zone structure
Core Design Contradiction:
Ease of operationVSDevice complexity

Solution Approach 1:

The combustion zone is divided into multiple independent zones (first combustion zone, second combustion zone, third combustion zone) with separate regeneration gas streams for each zone. This segmentation allows independent control of oxygen concentration and combustion conditions in each zone, enabling complete coke removal while maintaining operational simplicity through modular design.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Each combustion zone is provided with its own regeneration gas stream having specific oxygen concentration tailored to local requirements. The first zone uses lower oxygen concentration for controlled combustion, while subsequent zones use higher oxygen concentrations to complete coke removal, optimizing combustion control for each specific location.

Inventive Principle:
Principle #3Local quality

2Productivity

If higher oxygen concentration is used in the combustion zone to improve coke removal efficiency, then combustion speed increases, but the catalyst is damaged and life is reduced

Engineering Contradiction:
Improvecoke removal efficiencyVSAvoidcatalyst life
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The regeneration process is segmented into multiple zones with progressively higher oxygen concentrations. The first combustion zone uses controlled low oxygen concentration to burn coke slowly and controllably, protecting the catalyst. Subsequent zones use higher oxygen concentrations to complete coke removal, achieving high productivity while preserving catalyst life through staged oxidation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The first combustion zone performs preliminary coke removal under controlled conditions before the catalyst enters subsequent zones with higher oxygen concentrations. This preliminary action prevents excessive oxygen exposure that would damage the catalyst, while still achieving significant coke removal in the initial stage.

Inventive Principle:
Principle #10Preliminary action

3Ease of operation

If flue gas is continuously vented from the regenerator to control temperature and oxygen content, then combustion is controlled, but catalyst regeneration is less efficient and more catalyst is lost

Engineering Contradiction:
Improvetemperature controlVSAvoidregeneration efficiency
Core Design Contradiction:
Ease of operationVSProductivity

Solution Approach 1:

The regenerator is segmented into multiple combustion zones with independent gas streams, allowing temperature and oxygen content to be controlled locally in each zone rather than throughout the entire regenerator. This enables precise temperature control while maintaining high regeneration efficiency by minimizing overall flue gas venting.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The oxygen concentration parameter is changed progressively across different zones rather than uniformly. Each zone has its own regulated oxygen level optimized for that stage of combustion, enabling efficient coke removal while controlling temperature through localized parameter adjustment rather than global venting.

Inventive Principle:
Principle #35Parameter changes

4Loss of time

If the combustion process is accelerated to remove coke faster, then regeneration time is reduced, but combustion becomes uncontrolled and catalyst deactivation increases

Engineering Contradiction:
Improveregeneration timeVSAvoidcatalyst deactivation
Core Design Contradiction:
Loss of timeVSObject-affected harmful factors

Solution Approach 1:

The combustion process is segmented into sequential zones that progressively accelerate coke removal. The first zone uses controlled slow combustion to prevent catalyst damage, while subsequent zones progressively increase combustion rate. This segmented approach achieves fast regeneration time while controlling harmful combustion effects through staged acceleration.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The combustion process uses periodic progression through multiple zones with increasing oxygen concentrations. Each zone represents a periodic stage of combustion acceleration, allowing the system to rapidly remove coke through sequential oxidation stages while controlling temperature and preventing catalyst deactivation through regulated periodic intensification.

Inventive Principle:
Principle #19Periodic action

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 process enhances catalyst regeneration control, increases catalyst life, reduces flue gas venting, and maintains efficient combustion, thereby improving the robustness and longevity of the catalyst in the reactor-regenerator cycle.

Implementation Method 1

The combustion process is controlled through the oxygen content in the recycle gas. The recycle gas stream comprises a portion of the flue gas, and an additional stream of new combustion gas

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 2

passing a first regeneration gas comprising oxygen to the first, or upper, regeneration zone, and passing a second regeneration gas to the second, or lower, regeneration zone

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS8927449B2Multiple burn zones with independent circulation loops
Publication Date: 2015.01.06 UOP LLC
  • US8927449B2 patent drawing

AI summary

A process for a continuous regeneration of a catalyst wherein the regeneration section includes at least two separate zones. The regeneration includes a combustion zone, and an oxygen boost zone, where the process utilizes at least two independent regeneration gas loops for control of the amount of oxygen to regenerate the catalyst.