Layered Catalyst Transalkylation Diffusion Control

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Solution Overview

Problem

In the transalkylation of poly-alkylated benzene, where alkyl groups have 5 or more carbon atoms, isomerization and cyclization or cracking reactions occur, leading to catalyst deactivation, lower yields, and complicated separation issues due to the lack of control over diffusion paths and the formation of branched alkylbenzenes, which are difficult to biodegrade.

Innovation Solution

A process using a solid catalyst with a layered structure, comprising an inert core and a thin catalytic layer, is employed to react aromatic hydrocarbons with polyalkylated aromatic hydrocarbons under controlled pressure and temperature conditions, maintaining reactants in a liquid phase to produce monoalkylated aromatic hydrocarbons while limiting the diffusion of reactants into the catalyst, thus preventing isomerization and cyclization.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional solid catalysts are used for transalkylation of polyalkylated benzene, then the reaction can proceed, but isomerization and cyclization reactions occur leading to catalyst deactivation and lower yields

Engineering Contradiction:
Improvetransalkylation efficiencyVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The catalyst is segmented into a core and a shell layer, where the core provides structural support and the shell layer contains the active catalytic sites. This segmentation allows the reaction to occur only at the outer shell, preventing diffusion into the core and avoiding consecutive reactions that lead to isomerization and cyclization.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The catalytic activity is localized to the outer shell layer of the catalyst particle, while the core remains inert or has different properties. This local concentration of active sites ensures that reactants undergo transalkylation at the surface and are quickly desorbed, preventing further unwanted reactions inside the particle.

Inventive Principle:
Principle #3Local quality

2Productivity

If conventional solid catalysts are used for transalkylation, then the reaction can proceed, but cracking reactions occur leading to light hydrocarbon products and complicated separation

Engineering Contradiction:
Improvetransalkylation efficiencyVSAvoidlight hydrocarbon byproducts
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

By segmenting the catalyst into core and shell structures with limited diffusion paths through the shell, the residence time of reactants and products within the catalyst particle is reduced. This prevents cracking reactions that require longer contact times, thereby minimizing light hydrocarbon byproduct formation.

Inventive Principle:
Principle #1Segmentation

3Productivity

If conventional solid catalysts are used for transalkylation, then the reaction can proceed, but branched alkylbenzenes are formed which are difficult to biodegrade

Engineering Contradiction:
Improvetransalkylation efficiencyVSAvoidproduct linearity
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The active sites are localized to the outer shell layer, creating a specific reaction environment that favors transalkylation over isomerization. The limited diffusion path and surface-dominated reaction conditions promote the formation of linear alkylbenzene products while suppressing the formation of branched isomers.

Inventive Principle:
Principle #3Local quality

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 converts polyalkylbenzenes to monoalkylbenzenes while maintaining linearity, reducing catalyst deactivation and improving product quality by confining active sites to the outer layer, thereby enhancing processing efficiency and reducing costs.

Implementation Method 1

it would be beneficial to have the active sites confined to an outer layer to limit the diffusion path of the reactant and primary product

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 2

The aromatic hydrocarbon and the polyalkylated aromatic hydrocarbon are reacted over a solid catalyst comprising a layered structure, thereby generating an effluent stream comprising a monoalkylated aromatic hydrocarbon

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS7803977B2Transalkylation of heavy alkylate using a layered catalyst
Publication Date: 2010.09.28 UOP LLC

AI summary

A layered catalyst is disclosed for use in transalkylation of polyalkylated benzenes. The catalyst comprises an inner core material with a molecular sieve bonded over the core. The process minimizes the cracking of the alkyl groups during the transalkylation reaction.