Fixed-Bed Reactor Hot Spot Mitigation via Inert Zoning

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Solution Overview

Problem

The challenge in producing aromatic nitriles via ammoxidation reaction in fixed-bed reactors is the occurrence of hot spots, leading to unstable operations, side reactions, and reduced yield due to difficulty in controlling reaction temperature, which results in increased byproducts like carbon dioxide and hydrogen cyanide.

Innovation Solution

The method involves using a fixed-bed reactor with reaction tubes filled with a catalyst composed of vanadium, chromium, and boron, supported on alumina, silica-alumina, zirconia, or titania, where inert substances are strategically placed in areas identified as hot spots to mitigate temperature extremes and stabilize the reaction.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If a fixed-bed reactor is used for ammoxidation reaction, then the reaction can be carried out with good temperature control, but hot spots still occur leading to side reactions and reduced yield

Engineering Contradiction:
Improvereaction temperature controlVSAvoidyield of aromatic nitrile
Core Design Contradiction:
TemperatureVSProductivity

Solution Approach 1:

The patent applies local quality by introducing inert substance specifically at the hot spot location within the catalyst bed, rather than uniformly throughout. This creates a localized modification that suppresses the hot spot while preserving catalytic activity in other regions, thereby preventing side reactions and improving yield without compromising overall temperature control

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The inert substance acts as an intermediary element between the catalytic zones. By placing this inert material at the hot spot, it serves as a thermal barrier and flow modifier that prevents excessive temperature localizations while allowing the catalytic reaction to proceed efficiently in the surrounding areas

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If catalyst is used to promote ammoxidation reaction, then production efficiency increases, but combustion reaction accelerates causing increased byproducts

Engineering Contradiction:
Improveproduction efficiency of aromatic nitrileVSAvoidbyproducts such as carbon dioxide and hydrogen cyanide
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies local quality by introducing inert substance specifically at the hot spot location within the catalyst bed, rather than uniformly throughout. This creates a localized modification that suppresses the hot spot while preserving catalytic activity in other regions, thereby preventing side reactions and improving yield without compromising overall temperature control

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The inert substance acts as an intermediary element between the catalytic zones. By placing this inert material at the hot spot, it serves as a thermal barrier and flow modifier that prevents excessive temperature localizations while allowing the catalytic reaction to proceed efficiently in the surrounding areas

Inventive Principle:
Principle #24Intermediary (Mediator)

3Temperature

If fluidized bed system is used to control reaction temperature, then temperature control improves, but catalyst abrasion and erosion occur making stable operation difficult

Engineering Contradiction:
Improvereaction temperature controlVSAvoidstable operation
Core Design Contradiction:
TemperatureVSReliability

Solution Approach 1:

The patent applies segmentation by dividing the catalyst bed into distinct functional zones: catalytic regions for reaction and inert substance regions for thermal management. This segmentation allows the system to benefit from fixed-bed stability while locally addressing hot spot issues, avoiding the need for fluidized bed dynamics that cause catalyst abrasion

Inventive Principle:
Principle #1Segmentation

4Temperature

If fluidized bed system is used for ammoxidation reaction, then reaction temperature can be controlled, but gas-catalyst separation step is required increasing cost

Engineering Contradiction:
Improvereaction temperature controlVSAvoidgas-catalyst separation step
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

The patent applies segmentation by dividing the catalyst bed into distinct functional zones: catalytic regions for reaction and inert substance regions for thermal management. This segmentation allows the system to benefit from fixed-bed stability while locally addressing hot spot issues, avoiding the need for fluidized bed dynamics that cause catalyst abrasion

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 effectively suppresses hot spots, ensuring stable operation and preventing runaway reactions, thereby enhancing the yield of aromatic nitriles while minimizing byproduct formation.

Implementation Method 1

allow contact reaction of a gaseous mixture containing an aromatic hydrocarbon, ammonia and oxygen on a catalyst to produce the corresponding aromatic nitrile

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

Since ammoxidation reaction generates a large amount of reaction heat, it is very difficult to control the reaction temperature

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Data Source

PatentUS12060311B2Method for producing aromatic nitrile by ammoxidation reaction
Publication Date: 2024.08.13 MITSUBISHI GAS CHEM CO INC
  • US12060311B2 patent drawing
  • US12060311B2 patent drawing
  • US12060311B2 patent drawing

AI summary

The present invention can provide a method for producing an aromatic nitrile in which a fixed-bed reactor including a plurality of reaction tubes is used to subject a gaseous mixture comprising an aromatic hydrocarbon, ammonia, and oxygen by contact catalytic reaction on a catalyst to thereby produce the corresponding aromatic nitrile, wherein the catalyst is composed of an oxide containing vanadium, chromium, and boron and one or more supports selected from among alumina, silica-alumina, zirconia, and titania. One of the reaction tubes is filled with the catalyst of one kind and examined as to where a hot spot lies therein. An inert substance is filled into that portion of each of the plurality of reaction tubes which corresponds at least to the hot spot, and the catalyst is filled into the remaining portions.