Bifunctional Catalyst for C8 Aromatic Conversion

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional catalysts for converting aromatic hydrocarbons are inefficient in producing high-value C8 aromatic hydrocarbons like xylenes, leading to significant aromatic and xylene losses during disproportionation, transalkylation, and dealkylation reactions, which hampers yield and increases operating costs.

Innovation Solution

A bifunctional catalyst is developed by supporting hydrogenation metals like platinum, tungsten, or rhenium on a mixed support comprising specific zeolites and a refractory inorganic oxide binder, with a silica-alumina ratio and pore structure optimized to suppress excessive hydrogenation and enhance reaction activity, reducing aromatic loss and increasing xylene yields.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional catalysts are used for converting aromatic hydrocarbons, then the conversion reaction can proceed, but aromatic loss and xylene loss are significant, reducing yield

Engineering Contradiction:
Improveyield of C8 aromatic hydrocarbonsVSAvoidaromatic loss and xylene loss
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The catalyst employs a bifunctional design with distinct active sites: hydrogenation metals (Pt, Pd, Ni, Co) for hydrogenation functions and zeolite acidic sites for isomerization and transalkylation functions. This local differentiation of catalytic functions allows selective promotion of desired reactions while suppressing unwanted aromatic hydrogenation and xylene loss, resolving the contradiction between productivity and substance loss

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The catalyst combines hydrogenation metals with zeolite materials in a composite structure. The hydrogenation metals provide controlled hydrogenation activity while the zeolite framework provides shape-selective catalysis and acidity for transalkylation. This composite approach enables simultaneous achievement of high C8 aromatic yield and suppression of aromatic/xylene loss that cannot be achieved with single-function catalysts

Inventive Principle:
Principle #40Composite materials

2Productivity

If hydrogenation metals are supported on zeolite to form conventional catalysts, then conversion activity is achieved, but excessive hydrogenation occurs leading to aromatic loss

Engineering Contradiction:
Improveconversion activityVSAvoidexcessive hydrogenation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The hydrogenation metals are strategically positioned on the zeolite support to create localized hydrogenation sites that work synergistically with the zeolite acidic sites. This local quality differentiation ensures that hydrogenation occurs only where needed (on the metal sites) while the zeolite sites handle isomerization and transalkylation, preventing excessive hydrogenation that would degrade aromatic structures

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The zeolite acts as an intermediary material that mediates between the hydrogenation metals and the aromatic hydrocarbon substrates. The zeolite framework provides shape-selective constraints and acidic catalysis that directs the reaction pathway toward desired C8 aromatic products while the hydrogenation metals provide controlled hydrogenation, together preventing excessive hydrogenation harm

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If catalysts are designed for high conversion activity, then reaction efficiency increases, but operating costs increase due to aromatic loss

Engineering Contradiction:
Improvereaction efficiencyVSAvoidoperating costs
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The catalyst optimizes key parameters including the type and amount of hydrogenation metal (Pt, Pd, Ni, or Co), the zeolite composition (silica-alumina ratio), and the physical structure (pore size, surface area). By carefully adjusting these parameters, the catalyst achieves high conversion activity for C8 aromatic production while minimizing aromatic loss, thereby improving reaction efficiency without proportionally increasing operating costs

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 catalyst achieves high yields of mixed xylenes and para-xylene while minimizing aromatic loss, thereby improving process efficiency and reducing overall costs, making it suitable for commercialization.

Implementation Method 1

supporting hydrogenation metals like platinum, tungsten, or rhenium on a mixed support comprising specific zeolites and a refractory inorganic oxide binder

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 2

a bifunctional catalyst is developed by supporting hydrogenation metals like platinum, tungsten, or rhenium on a mixed support comprising specific zeolites

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

with a silica-alumina ratio and pore structure optimized to suppress excessive hydrogenation and enhance reaction activity

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS11648544B2Catalyst for converting alkylaromatic hydrocarbon and preparation method thereof
Publication Date: 2023.05.16 SK INNOVATION CO LTD

AI summary

Disclosed are a bifunctional catalyst and a preparation method therefor, the bifunctional catalyst being suitable to produce high-value aromatic hydrocarbons by subjecting alkylaromatic hydrocarbons to a disproportionation/transalkylation/dealkylation reaction while suppressing aromatic loss or subjecting C8 aromatic hydrocarbons to an isomerization reaction while suppressing xylene loss.