Selective Hydrogenation of Styrene Impurities in Paraxylene Streams

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Solution Overview

Problem

The presence of styrene impurities in paraxylene streams from alkylation processes over solid catalysts causes operability issues in downstream processes due to ring saturation and isomerization challenges, making selective hydrogenation difficult, especially when the desired product, paraxylene, is present at higher-than-equilibrium concentrations.

Innovation Solution

A catalyst comprising metals from Groups 8-10 of the Periodic Table, such as Pd, Co, and Ni, optionally with promoters like Ag and supports like Al2O3, is used to selectively hydrogenate styrene impurities in xylenes streams, minimizing isomerization and ring saturation reactions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If selective hydrogenation of styrene is performed using conventional catalysts, then styrene is converted to ethylbenzene, but ring saturation reactions occur converting paraxylene to dimethylcyclohexane and ethylcyclohexane which are difficult to separate

Engineering Contradiction:
Improveselectivity of styrene hydrogenationVSAvoidring saturation of paraxylene
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The patent changes the chemical parameters of the catalyst by selecting specific metals from Groups 8-10 (Pd, Co, Ni, Ru) and controlling their particle size (0.1-10 micrometers), promoters, and supports to achieve high styrene hydrogenation selectivity while minimizing paraxylene ring saturation. The specific catalyst composition parameters create a selective environment that favors styrene conversion without affecting the aromatic ring of paraxylene.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite catalyst materials combining metal active sites (Groups 8-10) with specific promoters and supports. This composite structure provides selective active sites for styrene hydrogenation while the promoter and support components suppress unwanted ring saturation reactions of paraxylene, achieving high selectivity through material composition design.

Inventive Principle:
Principle #40Composite materials

2Productivity

If catalysts with high hydrogenation activity are used, then styrene conversion is improved, but paraxylene isomerization activity increases which is undesirable

Engineering Contradiction:
Improvestyrene conversion rateVSAvoidparaxylene isomerization
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies local quality by creating catalysts with specific metal types (Groups 8-10) and controlled particle sizes that provide localized active sites highly selective for styrene hydrogenation. The promoter and support components create a localized chemical environment that enhances styrene conversion while suppressing paraxylene isomerization at the catalyst-styrene interface.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent optimizes catalyst parameters including metal selection (Pd, Co, Ni, Ru), particle size (0.1-10 micrometers), promoter types and amounts, and support materials to achieve the desired balance. These parameter changes create a catalyst that is highly active for styrene hydrogenation while maintaining minimal isomerization activity toward paraxylene.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If conventional hydrogenation catalysts are used, then styrene is converted, but separation of saturated C8 hydrocarbons from xylenes becomes difficult

Engineering Contradiction:
Improveselectivity of hydrogenation productVSAvoidseparation difficulty of C8 hydrocarbons
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The patent changes the selectivity parameters of the hydrogenation process by using Groups 8-10 metals with specific particle sizes and promoter combinations. This ensures that styrene is converted to ethylbenzene with minimal formation of saturated cyclohexane derivatives, thereby maintaining product separability and ease of downstream manufacturing.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the potential harm of over-hydrogenation (ring saturation) into a benefit by carefully controlling catalyst parameters to achieve complete styrene conversion to ethylbenzene without forming saturated cyclohexane products. The selective catalyst design ensures that the hydrogenation reaction stops at the desired ethylbenzene stage, preventing the formation of difficult-to-separate saturated hydrocarbons.

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 styrene to ethylbenzene with nearly 100% selectivity and minimal para-xylene isomerization, eliminating styrene impurities without affecting the paraxylene concentration, thus preventing operability problems in downstream processes.

Implementation Method 1

a catalyst comprising at least one metal selected Groups 8-10 of the Periodic Table, preferably Pd, Co, Ni, Ru, and mixtures thereof

Methodology Applied
Scientific EffectCatalytic hydrogenation: Catalysis

Implementation Method 2

selective hydrogenation of styrene to ethylbenzene

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Data Source

PatentUS20160244385A1Selective Hydrogenation of Styrene to Ethylbenzene
Publication Date: 2016.08.25 EXXONMOBIL CHEMICAL PATENTS INC

AI summary

A feedstream comprising paraxylene and styrene is contacted, in the presence of hydrogen, with a catalyst comprising at least one metal, selected from one or more metals selected from Groups 8-10.