NiFeAl Catalyst for Methane Partial Oxidation

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Solution Overview

Problem

Current catalysts for partial oxidation of methane to synthesis gas suffer from coke formation, leading to rapid deactivation and safety concerns due to reactor blockage and increased processing costs, despite efforts to improve their performance through doping and using basic metal oxides as supports.

Innovation Solution

A Ni-supported catalyst on high-surface-area Fe-doped γ-Al2O3 is developed, with a Ni concentration of approximately 10% by weight and an Fe:Al molar ratio of 0.03:0.97-0.05:0.95, which significantly reduces coke formation and enhances the catalyst's durability and efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If Ni-based catalysts are used for partial oxidation of methane, then cost is reduced compared to noble metals, but coke formation occurs leading to rapid deactivation

Engineering Contradiction:
Improvecatalyst costVSAvoidcatalyst stability
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The patent uses a composite catalyst structure with Ni particles supported on Fe-doped γ-Al2O3. The Fe-doped support creates a composite material that combines the low cost of Ni with the coke-resistant properties of Fe-modified alumina, resolving the contradiction between cost and stability

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent applies local quality by doping Fe specifically at the support-catalyst interface and within the alumina structure. This localized Fe doping creates oxygen-deficient sites and modifies the support properties in specific regions to prevent coke formation without requiring Fe throughout the entire catalyst structure, maintaining cost-effectiveness while improving stability

Inventive Principle:
Principle #3Local quality

2Object-affected harmful factors

If doping with Ru is applied to decrease coke formation, then coke formation is reduced, but catalyst cost increases due to expensive metal modifiers

Engineering Contradiction:
Improvecoke formationVSAvoidcatalyst cost
Core Design Contradiction:
Object-affected harmful factorsVSEase of manufacture

Solution Approach 1:

The patent replaces expensive Ru doping with cheap Fe doping on the alumina support. Fe is abundant and low-cost compared to Ru, while still providing effective coke prevention through the creation of oxygen-deficient sites and modified support properties, resolving the cost contradiction

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The patent changes the chemical composition parameter by substituting Fe for Ru as the dopant element. This parameter change maintains the functional effect of coke prevention through similar mechanisms (modification of support properties and creation of oxygen-deficient sites) while dramatically reducing cost

Inventive Principle:
Principle #35Parameter changes

3Object-affected harmful factors

If basic metal oxide supports are used to reduce coke formation, then coke deposits are reduced, but coke formation challenge remains unsolved

Engineering Contradiction:
Improvecoke depositsVSAvoidcoke formation resistance
Core Design Contradiction:
Object-affected harmful factorsVSReliability

Solution Approach 1:

The patent modifies the support properties by doping Fe into γ-Al2O3, which changes the oxygen content and creates oxygen-deficient sites. This parameter change in the support structure provides enhanced coke resistance beyond what basic metal oxides alone achieve, solving the remaining coke formation challenge

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 NiFeAl-based catalyst exhibits 91% methane conversion with nearly zero coke formation after 100 hours, maintaining high selectivity to H2 and CO with a desired H2:CO ratio of 2, thus preventing deactivation and ensuring safe, efficient, and cost-effective natural gas conversion.

Implementation Method 1

catalytic reactions, where the performance depends mainly on different characteristics of the catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

POM, which is based on CH4 reaction with O2 as shown in equation (1) below, has a significant advantage over the other routes since its reaction is exothermic

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Data Source

PatentUS11890596B2Coking resistant NiFeAl catalyst for partial oxidation of methane to synthesis gas
Publication Date: 2024.02.06 UNITED ARAB EMIRATES UNIVERSITY
  • US11890596B2 patent drawing
  • US11890596B2 patent drawing

AI summary

A novel NiFeAl-based catalytic material was developed for the conversion of methane, the main constituent of natural gas, to synthesis gas, which is a mixture of H2 and CO in a H2/CO molar ratio of 2, through partial oxidation by air at reasonable temperatures.