Non-Aromatic Hydrocarbon Conversion to Para-Xylene

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Solution Overview

Problem

Current processes for converting non-aromatic hydrocarbons to aromatics, such as para-xylene, face inefficiencies due to low activity of alkane compounds and high energy requirements, with existing methods often producing unwanted byproducts like ethylbenzene that complicate downstream processing.

Innovation Solution

The process involves converting non-aromatic hydrocarbons to aromatics with a focus on increasing benzene and C7 aromatic hydrocarbon yields, reducing C8 aromatic hydrocarbon production, and optimizing methylation conditions to enhance para-xylene production, including separate processing of C8 intermediate streams to improve separation efficiency and reduce equipment size.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional processes are used to convert non-aromatic hydrocarbons to aromatics, then aromatic compounds can be produced, but the activity of alkane compounds is low and additional improvements are desirable

Engineering Contradiction:
Improveconversion rate of non-aromatic hydrocarbons to aromaticsVSAvoidactivity of alkane compounds
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent employs catalysts with specific compositional parameters (metal components, support materials, pore structures) and optimizes reaction parameters (temperature, pressure, space velocity) to enhance alkane conversion activity. The catalyst formulation is specifically designed to increase the reactivity of low-reactivity alkane feedstocks toward aromatic products.

Inventive Principle:
Principle #35Parameter changes

2Quantity of substance

If processes produce C8 aromatic hydrocarbons including ethylbenzene, then aromatic yield increases, but unwanted byproducts complicate downstream processing and reduce para-xylene selectivity

Engineering Contradiction:
Improvearomatic hydrocarbon yieldVSAvoidpara-xylene selectivity
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The patent utilizes catalysts with spatially differentiated properties, including hierarchical pore structures with different pore sizes and acid site distributions, to promote specific reaction pathways. The catalyst design creates localized active sites that favor para-xylene formation while suppressing ethylbenzene and other unwanted C8 aromatics.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

Instead of attempting to convert all C8 aromatics to para-xylene through methylation, the invention inverts the approach by designing the aromatic formation step to selectively produce para-xylene directly, minimizing the need for subsequent conversion of unwanted isomers and byproducts.

Inventive Principle:
Principle #13The other way round (Inversion)

3Device complexity

If C8 intermediate streams are mixed together, then processing is simplified, but separation equipment size and hydraulic capacity requirements increase

Engineering Contradiction:
Improveprocessing complexityVSAvoidseparation equipment size
Core Design Contradiction:
Device complexityVSVolume of stationary object

Solution Approach 1:

The patent divides the C8 aromatic stream into separate intermediate streams based on composition and processing requirements. By segmenting the stream, each portion can be processed optimally, and the overall separation equipment size is reduced compared to handling a single mixed stream, as each segment requires smaller separation capacity.

Inventive Principle:
Principle #1Segmentation

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 increases the yield and selectivity of para-xylene production while minimizing ethylbenzene formation, allowing for more efficient xylene separation and reduced hydraulic capacity in separation equipment.

Implementation Method 1

converting non-aromatic hydrocarbon to an aromatic product in the presence of a catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

U.S. Pat. No. 5,043,502 describes a method for dehydroaromatization of C2-C5 aliphatic hydrocarbons to form aromatics

Methodology Applied
Scientific EffectDehydroaromatization:

Implementation Method 3

separating a first C8 intermediate stream from the aromatic formation effluent and separating a second C8 intermediate stream from the methylation effluent

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS10059641B2Conversion of non-aromatic hydrocarbon
Publication Date: 2018.08.28 EXXONMOBIL CHEMICAL PATENTS INC
  • US10059641B2 patent drawing
  • US10059641B2 patent drawing
  • US10059641B2 patent drawing

AI summary

Systems and methods are provided for converting alkane while generating improved yields of desirable aromatics and/or improved selectivity for forming desired aromatics, such as para-xylene (p-xylene). Aromatics generated during the aromatic formation process can be alkylated to form xylenes with improved yield and/or improved selectivity.