Supported Fused Fe/Al2O3 Catalyst for Methane Decomposition

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Solution Overview

Problem

The methane catalytic decomposition (MCD) process is hindered by catalyst deactivation due to carbon deposition, leading to CO2 production and hydrogen contamination, which prevents industrialization, as existing catalysts are not stable enough to maintain high selectivity and efficiency.

Innovation Solution

A supported fused Fe/Al2O3 catalyst is developed through a method involving the physical grinding and mixing of Fe nitrate and support nitrate, calcination, and reduction, which forms a stable and active catalyst for selective production of hydrogen or ethane from methane, avoiding rapid deactivation and CO2 production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional MSR is used to produce hydrogen, then hydrogen can be produced, but CO and CO2 are produced as by-products requiring additional water-gas shift and CO2-removal stages

Engineering Contradiction:
Improvehydrogen productionVSAvoidCO and CO2 by-products
Core Design Contradiction:
Quantity of substanceVSObject-generated harmful factors

Solution Approach 1:

The patent extracts the carbon by-products (CO and CO2) from the hydrogen production process by using methane catalytic decomposition instead of steam reforming. The MCD reaction (CH4 → C + 2H2) produces solid carbon that can be separated from the hydrogen gas stream, eliminating the need for water-gas shift and CO2 removal stages while maintaining high hydrogen production efficiency.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent changes the reaction parameters by using different catalysts (Ru, Rh, Pd, Pt, Ir, Ni, Co, Fe, or their alloys) and controlling reaction conditions (temperature, pressure, space velocity) to favor the decomposition pathway over steam reforming. This parameter change transforms the process from producing gaseous carbon oxides to producing solid carbon that can be easily separated.

Inventive Principle:
Principle #35Parameter changes

2Object-generated harmful factors

If MCD is used to produce hydrogen and carbon, then CO2 production is eliminated, but the catalyst deactivates due to carbon deposition on the active metal surface

Engineering Contradiction:
ImproveCO2 productionVSAvoidcatalyst stability
Core Design Contradiction:
Object-generated harmful factorsVSReliability

Solution Approach 1:

The patent introduces a support material (such as alumina, silica, titania, or zeolites) as an intermediary between the carbon-depositing metal particles and the carbon by-product. The support acts as a physical barrier that prevents carbon from completely covering the metal active sites, thereby maintaining catalyst stability while still allowing the reaction to proceed. The support also provides structural stability and can facilitate heat management.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent enables easy removal and regeneration of the catalyst by designing it with a support structure that allows for straightforward separation. The catalyst can be regenerated by burning off the deposited carbon in a controlled manner, and the support structure remains intact to be reused. This approach allows for periodic regeneration without replacing the entire catalyst system.

Inventive Principle:
Principle #34Discarding and recovering

3Reliability

If catalysts are regenerated by burning off deposited carbon, then catalyst activity is restored, but CO2 is produced and hydrogen may be contaminated

Engineering Contradiction:
Improvecatalyst activityVSAvoidCO2 production and hydrogen contamination
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent extracts the carbon by-product in its solid form during the main reaction, allowing it to be separated from the hydrogen stream before regeneration is needed. This prevents carbon accumulation to levels that would require aggressive burning-off procedures, thereby reducing CO2 production during regeneration and minimizing hydrogen contamination risks.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent designs the catalyst system to be easily replaceable or regenerable at low cost. By using robust support materials and simple regeneration procedures, the system can tolerate periodic catalyst replacement or regeneration without significant economic penalty, thereby avoiding the need for complex in-situ regeneration systems that might contaminate the hydrogen product.

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

4Reliability

If a stable MCD catalyst is designed, then catalyst deactivation is prevented, but the process is still far from industrialization due to lack of stable catalysts

Engineering Contradiction:
Improvecatalyst stabilityVSAvoidindustrialization readiness
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent employs composite catalyst systems combining metal particles (Ru, Rh, Pd, Pt, Ir, Ni, Co, Fe, or their alloys) with stable support materials (alumina, silica, titania, zeolites, etc.). This composite structure provides both the catalytic activity of the metal and the structural stability and carbon-resistant properties of the support, creating a catalyst that is ready for industrial application. The composite nature allows for optimization of both activity and stability simultaneously.

Inventive Principle:
Principle #40Composite materials

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 supported fused Fe/Al2O3 catalyst is highly active, stable, and selective, enabling efficient and controlled production of hydrogen or ethane with minimal carbon dioxide emission, thus overcoming the deactivation issues and enhancing the commercial viability of MCD processes.

Implementation Method 1

Methane catalytic decomposition (hereinafter MCD) has been widely studied as an alternative way of methane steam reforming (MSR) to produce hydrogen

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

calcining under static air from about room temperature to 350° C. for about 2 to 4 h

Methodology Applied
Scientific EffectThermal decomposition: Pyrolysis

Implementation Method 3

reducing the temperature down to room temperature under air flow

Methodology Applied
Scientific EffectReduction: Reduction

Data Source

PatentUS10179326B2Supported iron catalysts, methods of making, methods of hydrocarbon decomposition
Publication Date: 2019.01.15 KING ABDULLAH UNIV OF SCI & TECH
  • US10179326B2 patent drawing
  • US10179326B2 patent drawing
  • US10179326B2 patent drawing

AI summary

Embodiments of the present disclosure also provide for a supported fused Fe catalyst, a method of making the supported fused Fe catalyst, methods of hydrocarbon decomposition, and the like.