Multi-tubular Reactor Segmentation for Hot Spot Control

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Solution Overview

Problem

Multi-tubular shell-and-tube reactors experience hot spots during high-load reactions, leading to shortened catalyst lifetime and decreased selectivity for desired products, with existing methods insufficiently addressing heat transfer efficiency and stability issues.

Innovation Solution

A method using a fixed-bed multistage heat medium circulating type of multi-tubular shell-and-tube reactor with independent temperature zones and high-activity catalyst layers, where heat transfer occurs at 280 to 400 °C, and the catalyst activity increases from the inlet to the outlet, effectively controlling temperature and improving yield and stability.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a multi-tubular shell-and-tube reactor is used for high-load reaction, then productivity is improved, but hot spots occur causing shortened catalyst lifetime and degraded selectivity

Engineering Contradiction:
Improvereaction loadVSAvoidcatalyst lifetime
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The reactor shell is divided into multiple independent heat transfer zones by inserting partition walls, allowing each zone to be controlled independently. This segmentation enables precise temperature management in different reactor sections, preventing hot spot formation while maintaining high overall reaction load and productivity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Different temperature conditions are applied to different zones within the reactor by controlling heat medium flow in each partitioned section independently. This local quality approach allows optimization of reaction conditions in each zone, maintaining high productivity while preventing localized overheating that would degrade catalyst lifetime.

Inventive Principle:
Principle #3Local quality

2Temperature

If heat transfer efficiency is increased to control hot spots, then temperature control is improved, but operation stability decreases

Engineering Contradiction:
Improvehot spot temperatureVSAvoidoperation stability
Core Design Contradiction:
TemperatureVSStability of the object's composition

Solution Approach 1:

The heat transfer system is segmented into multiple independent zones with separate heat medium circulation. This allows gradual and controlled temperature management across different reactor sections, maintaining operation stability while effectively controlling hot spot temperatures through distributed heat removal.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The heat medium flow rate and temperature can be dynamically adjusted in each zone independently based on local reaction conditions. This dynamic control capability enables precise temperature management to prevent hot spots while maintaining overall system stability through flexible adaptation to changing reaction conditions.

Inventive Principle:
Principle #15Dynamics

3Device complexity

If conventional heat transfer methods are used, then device complexity is kept low, but hot spot control effectiveness is insufficient

Engineering Contradiction:
Improvereactor structureVSAvoidhot spot temperature
Core Design Contradiction:
Device complexityVSTemperature

Solution Approach 1:

Partition walls are inserted into the reactor shell to create multiple heat transfer zones, implementing a relatively simple structural modification that enables effective hot spot control through distributed heat removal while maintaining manageable device complexity.

Inventive Principle:
Principle #1Segmentation

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 hot spot temperatures, enhances the yield and operational stability of unsaturated aldehydes and unsaturated carboxylic acids production, as demonstrated by higher selectivity and yield compared to conventional methods.

Implementation Method 1

a heat medium circulating through a reactor shell so that the chemical reaction can take place in an optimum condition

Methodology Applied
Scientific EffectHeat transfer: Convection

Implementation Method 2

a solid catalyst filled in a plurality of reaction tubes, and supplies a raw material gas into the reaction tubes to create a chemical reaction

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

a multi-tubular shell-and-tube reactor in the form of a heat exchanger... efficiently removing heat produced in a reaction

Methodology Applied
Scientific EffectThermal conduction: Conduction (thermal)

Data Source

PatentEP3415492B1Method for producing unsaturated aldehyde and unsaturated carboxylic acid
Publication Date: 2024.04.17 LG CHEM LTD
  • EP3415492B1 patent drawing
  • EP3415492B1 patent drawing
  • EP3415492B1 patent drawing

AI summary

The present invention relates to a method for producing unsaturated aldehydes and unsaturated carboxylic acids. According to the present invention, a method for producing unsaturated aldehydes and unsaturated carboxylic acids which can impart activity and control temperature independently in fixed catalyst layer zones in a shell-and-tube reactor, thereby exhibiting improved yield and operation stability, is provided.