TNU-9 Catalyst Mesoporous-Microporous Structure for Ethylbenzene Selectivity

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current catalysts for producing ethylbenzene from ethanol and benzene face challenges such as rapid deactivation due to coking and poor hydrothermal stability, leading to reduced selectivity and conversion rates, especially in ZSM-5 molecular sieves which have limitations in channel diameter affecting mass transfer and structural collapse.

Innovation Solution

A mesoporous-microporous composite TNU-9 molecular sieve with a high silicon content is synthesized using MCM-48 or SBA-15 as a silicon source and 1,4-MPB as a template, providing a 10-ring structure with intersecting porous channels, enhancing hydrothermal stability and alkylation activity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If ZSM-5 molecular sieve is used as catalyst, then dehydration selectivity and ethylbenzene selectivity are improved, but catalyst stability and hydrothermal stability deteriorate due to rapid deactivation from coking and structural collapse

Engineering Contradiction:
Improveethylbenzene selectivityVSAvoidcatalyst stability
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The patent uses a composite catalyst system comprising ZSM-5 molecular sieve combined with mesoporous materials (MCM-48 or SBA-15) and metal oxides (Al2O3, SiO2, TiO2, or ZrO2). This composite structure combines the high dehydration selectivity of ZSM-5 with the enhanced stability and hydrothermal resistance of the mesoporous support and metal oxide components, preventing rapid deactivation while maintaining high ethylbenzene selectivity.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent modifies specific regions of the catalyst by adding metal oxide promoters (Al2O3, SiO2, TiO2, or ZrO2) to enhance local hydrothermal stability and resistance to coking. The mesoporous materials are introduced to improve mass transfer in specific channels, creating local quality improvements without altering the overall ZSM-5 structure that provides high selectivity.

Inventive Principle:
Principle #3Local quality

2Manufacturing precision

If ZSM-5 molecular sieve with small channel diameter is used, then dehydration selectivity is improved, but mass transfer efficiency deteriorates

Engineering Contradiction:
Improvedehydration selectivityVSAvoidmass transfer efficiency
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent embeds ZSM-5 microporous crystals within mesoporous material matrices (MCM-48 or SBA-15). The mesoporous structures act as outer containers with larger channels that facilitate mass transfer, while the ZSM-5 microporous crystals nested inside maintain high dehydration selectivity. This nested architecture allows reactants to access active sites more efficiently through the mesoporous pathways while still achieving selective dehydration within the ZSM-5 channels.

Inventive Principle:
Principle #7Nested doll (Nesting)

Solution Approach 2:

The patent introduces mesoporous materials with larger pore diameters (MCM-48 or SBA-15) to create a hierarchical porous structure. The mesopores provide efficient mass transfer pathways, while the micropores of ZSM-5 maintain high selectivity. This dual-scale porous architecture resolves the contradiction between selectivity and mass transfer efficiency.

Inventive Principle:
Principle #31Porous materials

3Ease of manufacture

If conventional alkylation reagents are used, then production cost increases due to petroleum depletion, but environmental friendliness deteriorates

Engineering Contradiction:
Improveproduction costVSAvoidenvironmental impact
Core Design Contradiction:
Ease of manufactureVSObject-affected harmful factors

Solution Approach 1:

The patent changes the chemical composition parameters of the catalyst by incorporating metal oxides (Al2O3, SiO2, TiO2, or ZrO2) and mesoporous materials, which enhance catalyst stability and activity. This allows the use of renewable ethanol as feedstock at lower temperatures and pressures, reducing production costs and environmental impact simultaneously.

Inventive Principle:
Principle #35Parameter changes

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 TNU-9 catalyst achieves high selectivity and stability for ethylbenzene production, maintaining catalytic performance over extended periods with improved hydrothermal stability, achieving selectivity greater than 93% under optimized reaction conditions.

Implementation Method 1

a catalyst for vapor-phase alkylation of ethanol and benzene to produce ethylbenzene in one-step... The TNU-9 catalyst achieves high selectivity and stability for ethylbenzene production, maintaining catalytic performance over extended periods

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

A mesoporous-microporous composite TNU-9 molecular sieve with a high silicon content is synthesized... providing a 10-ring structure with intersecting porous channels, enhancing hydrothermal stability and alkylation activity

Methodology Applied
Scientific EffectPorosity: Porosity

Data Source

PatentUS11434183B2Catalyst for preparing ethylbenzene from ethanol and benzene, preparation therefor and use thereof
Publication Date: 2022.09.06 DALIAN INSTITUTE OF CHEMICAL PHYSICS CHINESE ACADEMY OF SCIENCES
  • US11434183B2 patent drawing
  • US11434183B2 patent drawing
  • US11434183B2 patent drawing

AI summary

Disclosed is a catalyst for producing ethylbenzene in one-step by vapor phase alkylation reaction of ethanol and benzene. The catalyst has the following features for the reaction: high alkylation reaction activity, high selectivity of ethylbenzene in an alkylation product, high hydrothermal stability and stable catalytic performance. The catalyst comprises a mesoporous-microporous composite TNU-9 molecular sieve and the silicon to aluminum molar ratio, SiO2/Al2O3, of the meso-microporous composite TNU-9 molecular sieve ranges from 50 to 200.