Silicon-Based Mesostructured Catalyst for C4 Alcohol Dehydration

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Solution Overview

Problem

Current processes for producing C4 alkenes from C4 monoalcohols face challenges in achieving high selectivity and stability due to the limitations of existing catalysts, which often result in secondary reactions such as oligomerization, cracking, and coking, especially when attempting simultaneous dehydration and skeletal isomerization.

Innovation Solution

A process utilizing a catalyst comprising mesostructured materials with silicon, such as aluminosilicates, that enables simultaneous dehydration and skeletal isomerization of C4 monoalcohols, optimizing acidity properties and diffusion to enhance selectivity and stability, and incorporating elements like aluminum to achieve a balance between Bronsted acidity and structural properties.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If conventional catalysts (alumina, zeolites) are used for dehydration of C4 alcohols, then the reaction proceeds at relatively low temperatures, but secondary reactions (ether formation, positional isomerization) occur and catalyst stability deteriorates over time

Engineering Contradiction:
Improvereaction temperatureVSAvoidcatalyst stability
Core Design Contradiction:
TemperatureVSReliability

Solution Approach 1:

The patent employs composite catalysts combining alumina with specific metal oxides (silica, titania, zirconia, magnesia) to create a material that maintains low-temperature operation while suppressing secondary reactions and improving stability. The composite structure allows the alumina to provide dehydration activity while the added oxides modify the acid-base properties to reduce unwanted side reactions.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent modifies the chemical and physical parameters of the catalyst by controlling the ratio of alumina to auxiliary oxides, adjusting water content (0.1-10%), and optimizing particle size (0.1-1.0 mm). These parameter changes enable the catalyst to maintain high activity at low temperatures while improving resistance to deactivation from secondary reactions.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If strong acid catalysts are used to promote skeletal isomerization, then isomerization activity increases, but unwanted secondary reactions (oligomerization, cracking, coking) increase and catalyst deactivation accelerates

Engineering Contradiction:
Improveisomerization activityVSAvoidsecondary reactions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent creates localized regions of different acid strength within the catalyst structure. By combining alumina with weaker acid oxides (silica, titania, zirconia, magnesia), the catalyst has zones that favor isomerization while other zones suppress strong acid-catalyzed side reactions like oligomerization and cracking, thereby reducing harmful effects.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The auxiliary metal oxides act as intermediaries that moderate the acid strength of the catalyst. These oxides dilute the strong acid sites in alumina, providing a softer acid character that promotes gentle isomerization while preventing the harsh effects of strong acids such as coking and cracking.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Reliability

If alumina-based catalysts are used for dehydration, then the catalyst is robust and cost-effective, but selectivity for desired products decreases due to prominent secondary reactions

Engineering Contradiction:
Improvecatalyst robustnessVSAvoidproduct selectivity
Core Design Contradiction:
ReliabilityVSManufacturing precision

Solution Approach 1:

The patent adjusts the compositional parameters of the catalyst by varying the ratio of alumina to auxiliary oxides (silica, titania, zirconia, magnesia) within specific ranges. This parameter optimization maintains the robustness and cost-effectiveness of alumina while tuning the acid-base properties to improve selectivity and reduce secondary reactions.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates composite materials where alumina provides structural robustness and cost-effectiveness, while the integrated metal oxides (silica, titania, zirconia, magnesia) enhance product selectivity by modifying the catalytic sites to favor desired dehydration and isomerization products over unwanted side products.

Inventive Principle:
Principle #40Composite materials

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

The use of silicon-based mesostructured materials improves catalytic performance by increasing selectivity of butene isomers, enhancing catalyst stability, and increasing the yield of C4 isomers, while minimizing secondary reactions like oligomerization and cracking.

Implementation Method 1

The dehydration reaction of the alcohols leads to the formation of alkenes

Methodology Applied
Scientific EffectDehydration reaction:

Implementation Method 2

skeletal isomerization of butenes requires stronger Bronsted sites and higher reaction temperatures than the dehydration

Methodology Applied
Scientific EffectSkeletal isomerization:

Implementation Method 3

the formation of positional isomer alkenes from alkenes originally formed during dehydration

Methodology Applied
Scientific EffectPositional isomerization:

Data Source

PatentUS9512050B2Process for dehydration and isomerization of alcohols using a catalyst based on a mesostructured material comprising silicon
Publication Date: 2016.12.06 IFP ENERGIES NOUVELLES

AI summary

This invention has as its object a process for simultaneous dehydration and skeletal isomerization of a feedstock that comprises at least one C4 monoalcohol and that contains between 0.5 and 50% water, for the purpose of producing C4 alkenes, with said process operating at a temperature of between 250 and 550° C., under a pressure of between 0.1 and 1 MPa, with an hourly volumetric flow rate of between 0.1 and 10 h-1, characterized in that it uses a catalyst that comprises at least one mesostructured material that comprises silicon and at least one element X that is selected from among aluminum, boron, gallium, indium, and germanium.