Composite Catalyst for Direct Synthesis Gas to Aromatic Hydrocarbons

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Solution Overview

Problem

Current technologies for synthesizing aromatic hydrocarbons from petroleum are limited by low PX content and high energy consumption, and alternative methods from coal face challenges in selectivity and efficiency, failing to meet the increasing demand in China.

Innovation Solution

A composite catalyst comprising active metal oxides and ZSM-5 zeolite, with specific structural features and preparation methods, enables direct conversion of synthesis gas to aromatic hydrocarbons with high selectivity and low methane byproduct, overcoming the limitations of existing methods.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If traditional petroleum routes are used for aromatic hydrocarbon production, then production maturity is achieved, but PX content in aromatic productions is low and energy consumption is high

Engineering Contradiction:
Improveproduction maturityVSAvoidPX content
Core Design Contradiction:
ReliabilityVSQuantity of substance

Solution Approach 1:

The invention changes the chemical composition parameters of the catalyst by incorporating specific metal oxides (Fe2O3, MnO2, ZnO) with defined weight ratios to enhance the catalytic performance for PX production, thereby increasing PX content in aromatic hydrocarbons while maintaining production maturity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention uses a composite catalyst material combining multiple metal oxides (Fe2O3, MnO2, ZnO) with ZSM-5 zeolite, where each component contributes specific functions: Fe2O3 for CO conversion, MnO2 for selectivity enhancement, ZnO for structure stabilization, and ZSM-5 for aromatic formation, achieving high PX content through synergistic effects

Inventive Principle:
Principle #40Composite materials

2Reliability

If traditional petroleum routes are used for aromatic hydrocarbon production, then production maturity is achieved, but energy consumption is high

Engineering Contradiction:
Improveproduction maturityVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The invention optimizes reaction parameters including temperature (300-500°C), pressure (0.1-6 MPa), and space velocity (500-8000 h-1) to achieve high aromatic hydrocarbon selectivity under milder conditions, reducing energy consumption while maintaining production maturity through the synergistic catalyst system

Inventive Principle:
Principle #35Parameter changes

3Quantity of substance

If direct conversion of synthesis gas is used, then aromatic hydrocarbon selectivity is improved, but methane byproduct formation occurs

Engineering Contradiction:
Improvearomatic hydrocarbon selectivityVSAvoidmethane byproduct
Core Design Contradiction:
Quantity of substanceVSObject-generated harmful factors

Solution Approach 1:

The invention applies local quality by creating specific active sites on the ZSM-5 zeolite surface through metal oxide modification, where Fe2O3, MnO2, and ZnO are distributed to create localized regions that favor aromatic hydrocarbon formation over methane production, achieving high selectivity with reduced harmful byproducts

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

The catalyst achieves a selectivity of 50-85% for aromatic hydrocarbons with low methane production, offering a more efficient and industrially viable solution for aromatic hydrocarbon synthesis.

Implementation Method 1

A catalyst and method for synthesis of aromatic hydrocarbons through direct conversion of synthesis gas

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS10618855B2Catalyst and method for synthesis of aromatic hydrocarbons through direct conversion of synthesis gas
Publication Date: 2020.04.14 DALIAN INSTITUTE OF CHEMICAL PHYSICS CHINESE ACADEMY OF SCIENCES

AI summary

Synthesis of aromatic hydrocarbons from synthesis gas in a fixed bed or a moving bed reactor loaded with a composite catalyst comprising Catalyst Component A and Catalyst Component B mixed via a mechanical mixing mode, wherein the active ingredient of the Catalyst Component A is active metal oxides; and the Catalyst Component B is one or both of ZSM-5 zeolite and metal modified ZSM-5; the pressure of the synthesis gas is 0.1-6 MPa; the reaction temperature is 300-600° C.; and the space velocity is 500-8000 h−1. The reaction process has a high product yield and selectivity, with the selectivity of aromatics reaching 50-85%, while the selectivity of the methane byproduct is less than 15%.