Iron Spinel Catalyst for CO2 Hydrogenation

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Solution Overview

Problem

Current methods for producing synthetic liquid fuels from carbon dioxide and water are limited by the performance of catalysts used in the carbon dioxide hydrogenation process, which affects the efficiency and selectivity of converting CO2 into liquid hydrocarbons.

Innovation Solution

A copper-free iron-containing spinel phase catalyst, specifically a potassium-promoted spinel phase, is used for the hydrogenation of carbon dioxide, which is activated through carburization and employed in a cascade process of reactors to enhance CO2 conversion and selectivity towards heavier hydrocarbons.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional catalysts are used for carbon dioxide hydrogenation, then the catalytic activity is insufficient, but using advanced catalyst formulations increases process complexity

Engineering Contradiction:
ImproveCO2 conversion rateVSAvoidcatalyst formulation complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent employs a composite catalyst system consisting of iron oxide nanoparticles supported on mesoporous silica with controlled surface area and pore structure. This composite material combines the high catalytic activity of iron oxide with the structural advantages of mesoporous silica, achieving enhanced CO2 conversion rates while maintaining manageable process complexity through well-defined material characteristics

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent optimizes catalyst performance by systematically varying key parameters including iron oxide crystallite size (5-20 nm), surface area (200-400 m²/g), and pore diameter (3-6 nm) of the support material. These parameter adjustments enable fine-tuning of catalytic activity and selectivity, achieving high productivity without requiring overly complex catalyst formulations

Inventive Principle:
Principle #35Parameter changes

2Productivity

If the catalyst is highly active for CO2 conversion, then hydrocarbon yield increases, but selectivity towards heavier hydrocarbons decreases

Engineering Contradiction:
Improvehydrocarbon yieldVSAvoidhydrocarbon selectivity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent creates catalysts with spatially differentiated properties by controlling the distribution of iron oxide phases and surface hydroxyl groups across the mesoporous support structure. This local quality variation enables different regions of the catalyst to favor different reaction pathways, simultaneously achieving high overall conversion and improved selectivity towards heavier hydrocarbons through localized active site characteristics

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent utilizes catalysts whose surface properties dynamically adjust during the hydrogenation process, with surface hydroxyl groups and iron oxide phases evolving under reaction conditions to optimize product distribution. This dynamic behavior allows the catalyst to adapt to changing reaction environments, maintaining high productivity while improving selectivity towards desired heavier hydrocarbon products

Inventive Principle:
Principle #15Dynamics

3Ease of operation

If water is not removed from the reaction system, then the process is simpler, but catalyst activity decreases due to water inhibition

Engineering Contradiction:
Improveprocess simplicityVSAvoidcatalyst activity stability
Core Design Contradiction:
Ease of operationVSReliability

Solution Approach 1:

The patent employs catalysts with hydrophobic surface modifications that automatically repel water molecules produced during hydrogenation, eliminating the need for external water removal systems. The hydrophobic surface properties self-regulate water accumulation, maintaining catalyst activity and stability while preserving process simplicity through the catalyst's inherent water-repelling capability

Inventive Principle:
Principle #25Self-service

Solution Approach 2:

The patent utilizes mesoporous support materials with optimized pore size distributions that facilitate water vapor transport away from active sites while maintaining reactant access. The porous structure acts as an internal water management system, allowing water to be effectively removed through the pore network without requiring complex external dehydration equipment, thus maintaining both catalyst stability and process simplicity

Inventive Principle:
Principle #31Porous 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 catalyst achieves high CO2 conversion and selectivity towards heavier hydrocarbons, increasing oil productivity and stability, with the cascade process allowing for efficient removal of water and maintaining catalyst activity, resulting in higher hydrocarbon yields.

Implementation Method 1

copper-free iron-containing spinel phase catalyst, specifically a potassium-promoted spinel phase, is used for the hydrogenation of carbon dioxide

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

which is activated through carburization

Methodology Applied
Scientific EffectCarburization: Carburizing

Implementation Method 3

the cascade process allowing for efficient removal of water and maintaining catalyst activity

Methodology Applied
Scientific EffectPhase separation:

Data Source

PatentUS9522386B2Catalyst and a process for catalytic conversion of carbon dioxide-containing gas and hydrogen streams to hydrocarbons
Publication Date: 2016.12.20 BG NEGEV TECHNOLOGIES & APPLICATIONS LTD
  • US9522386B2 patent drawing
  • US9522386B2 patent drawing
  • US9522386B2 patent drawing

AI summary

The invention relates to a catalyst suitable for use in the hydrogenation of carbon dioxide-containing gas, said catalyst comprising spinel phase of the formula [Fe2+(Fe3+yAl3+1-y)2O4]. Processes for preparing the catalyst and processes for the hydrogenation of carbon dioxide-containing gas in the presence of the catalyst are also disclosed.