Reactor Catalyst Inlet Segmentation for Uniform Mixing

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

In fluid catalytic reactions, such as paraffin dehydrogenation, disparities in catalyst temperature and density lead to hot spots, promoting unselective thermal cracking reactions over desired catalytic reactions, which reduces product selectivity.

Innovation Solution

A reactor design with two spent catalyst inlets and at least one regenerated catalyst inlet, arranged to ensure thorough mixing and uniform temperature and density profiles, minimizing temperature and density variations within the reaction chamber.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If regenerated catalyst at high temperature is used to increase reaction heat, then reaction conversion is improved, but thermal cracking reactions are promoted which reduces product selectivity

Engineering Contradiction:
Improvereaction conversionVSAvoidthermal cracking reactions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The catalyst inlet system is segmented into multiple separate inlets (first regenerated catalyst inlet, second regenerated catalyst inlet, first spent catalyst inlet, second spent catalyst inlet) positioned at different locations and angles within the reaction chamber. This segmentation allows different catalyst streams to be introduced separately and mix progressively, preventing localized high-temperature zones that cause thermal cracking while maintaining overall high conversion through sufficient reaction heat supply.

Inventive Principle:
Principle #1Segmentation

2Temperature

If catalyst circulation is increased to provide additional heat, then reaction temperature is improved, but temperature disparities increase leading to hot spots

Engineering Contradiction:
Improvereaction temperatureVSAvoidcatalyst temperature uniformity
Core Design Contradiction:
TemperatureVSStability of the object's composition

Solution Approach 1:

Different regions of the reaction chamber are provided with different inlet configurations optimized for their local requirements. The inlets are positioned at specific angles (e.g., 45-135 degrees between spent catalyst inlets, 45-135 degrees between regenerated catalyst inlets) and locations to create localized mixing zones that progressively homogenize temperature and density throughout the catalyst bed, preventing hot spots while maintaining overall temperature stability.

Inventive Principle:
Principle #3Local quality

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 catalyst mixing, leading to increased conversion and selectivity of catalytic reactions over thermal cracking, thereby improving overall process efficiency and product yield.

Implementation Method 1

The first spent catalyst stream, the second spent catalyst stream, the first regenerated catalyst stream, and perhaps the second regenerated catalyst stream are mixed in the reaction chamber

Methodology Applied
Scientific EffectConvection: Convection

Data Source

PatentUS11794159B2Process and apparatus for contacting feed and catalyst with improved catalyst mixing
Publication Date: 2023.10.24 UOP LLC
  • US11794159B2 patent drawing
  • US11794159B2 patent drawing
  • US11794159B2 patent drawing

AI summary

A process and reactor for contacting a feed stream with a catalyst stream comprises a reaction chamber comprising two spent catalyst inlets for delivering two spent catalyst streams to the reaction chamber and at least one regenerated catalyst inlet for delivering a regenerated catalyst stream to the reaction chamber. The reaction chamber may also include a second regenerated catalyst inlet for delivering a second regenerated catalyst stream to the reaction chamber. The second spent catalyst inlet enables thorough mixing of catalyst streams.