Alkali Metal-Doped Molybdenum Carbide for Selective CO2 Hydrogenation

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Solution Overview

Problem

Current catalysts for CO2 hydrogenation in the reverse water-gas shift reaction, such as Fe and Co-based Fischer-Tropsch catalysts, face challenges in selectivity and stability due to water poisoning and high operating temperatures, while low-cost alternatives like transition metal carbides show promise but require optimization for high CO selectivity across a wide range of conditions.

Innovation Solution

Alkali metal-doped molybdenum carbide supported on gamma alumina (A-Mo2C/γ-Al2O3, where A=K, Na, Li) is synthesized through co-impregnation and carburization, offering a low-cost, stable, and highly selective catalyst for CO2 hydrogenation via the RWGS reaction.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If Fe-based Fischer-Tropsch catalysts are used for CO2 hydrogenation, then C2-C5+ hydrocarbon selectivity is improved (62.4%), but catalyst stability deteriorates due to water poisoning

Engineering Contradiction:
Improveproduct selectivityVSAvoidcatalyst stability
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The patent uses a composite catalyst system comprising Fe carbide phase supported on gamma-Al2O3 with SiO2 promoter and K2CO3 alkali metal additive. This composite structure combines the high hydrocarbon selectivity of Fe carbide with the water tolerance of the alumina support and SiO2 promoter, while K2CO3 enhances CO2 activation. The composite material resolves the contradiction by integrating multiple functional components that collectively provide both high selectivity and stability against water poisoning.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent employs parameter changes by controlling the oxidation state of iron (Fe0 vs Fe2+), the amount of SiO2 promoter (0.5-5 wt%), and K2CO3 additive (0.1-5 wt%) to optimize catalyst performance. By adjusting these parameters, the catalyst achieves high hydrocarbon selectivity while maintaining stability. The Fe carbide phase formation conditions are also controlled to ensure optimal activity and resistance to water poisoning.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If Co-based catalysts are used for CO2 hydrogenation, then catalyst stability is improved (water tolerance), but CO2 conversion efficiency deteriorates compared to Fe-based catalysts

Engineering Contradiction:
Improvecatalyst stabilityVSAvoidCO2 conversion
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent creates a composite catalyst combining Fe carbide (high activity) with gamma-Al2O3 support and SiO2 promoter (water tolerance). This composite structure allows the Fe carbide phase to provide high CO2 conversion rates while the alumina-SiO2 matrix provides water tolerance and structural stability. The synergistic interaction between components resolves the contradiction between activity and stability.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The gamma-Al2O3 support acts as an intermediary that protects the Fe carbide active phase from water poisoning while maintaining its catalytic activity. The SiO2 promoter serves as another intermediary that enhances the interface between Fe carbide and support, improving both stability and activity. These intermediary materials enable the Fe-based catalyst to achieve both high conversion and water tolerance.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If high temperatures (≥600°C) are used for RWGS reaction over ZnO/Al2O3 catalysts, then CO selectivity is improved, but energy consumption and catalyst deactivation worsen

Engineering Contradiction:
ImproveCO selectivityVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent changes the temperature parameter from conventional high temperatures (≥600°C) to moderate temperatures (200-400°C) by using Fe carbide catalyst with K2CO3 promoter. This parameter change enables high CO selectivity at lower temperatures, reducing energy consumption. The Fe carbide phase and alkali metal promoter work synergistically to activate CO2 at mild conditions while maintaining high CO selectivity.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The Fe carbide phase acts as a strong catalyst that accelerates the RWGS reaction at lower temperatures, replacing the need for high thermal energy input. The K2CO3 promoter enhances CO2 activation能力, allowing the reaction to proceed efficiently at 200-400°C instead of requiring 600°C or higher, thus reducing energy consumption while maintaining high CO selectivity.

Inventive Principle:
Principle #38Strong oxidants (Accelerated oxidation)

4Manufacturing precision

If alkali metal doping is applied to Mo2C catalyst, then CO selectivity is improved (up to 96%), but catalyst complexity increases

Engineering Contradiction:
ImproveCO selectivityVSAvoidcatalyst complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent changes the chemical composition parameter by introducing alkali metal dopants (K, Na, Li) at optimized concentrations (0.1-5 wt%). This parameter change dramatically improves CO selectivity from typical Mo2C levels to up to 96%. The alkali metals modify the electronic structure of Mo2C, enhancing CO2 activation and CO desorption, thereby achieving high selectivity with a relatively simple doping approach.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The alkali metal dopants are distributed locally on the Mo2C surface, creating localized active sites with enhanced CO2 activation capability. This local quality modification allows high CO selectivity without requiring complex bulk structure changes. The dopants concentrate their effect at the catalyst surface where CO2 activation occurs, achieving high performance with minimal complexity increase.

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 alkali metal-promoted molybdenum carbide catalyst achieves high CO selectivity and yield, exceeding previous catalysts, with K—Mo2C/γ-Al2O3 reaching 16.5% CO yield and 96% selectivity, and maintaining stability across varying temperatures and conditions, enhancing the feasibility of CO production for downstream hydrocarbon synthesis.

Implementation Method 1

CO2 hydrogenation via the RWGS reaction to achieve high CO selectivity and yield

Methodology Applied
Scientific EffectReverse water-gas shift reaction: Chemical Bonding

Implementation Method 2

alkali metal-promoted molybdenum carbide catalyst achieves high CO selectivity and yield

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

The addition of K to catalysts as a promoter has not yet been recorded with a Mo2C-based catalyst for CO2 hydrogenation. Furthermore, doping Mo2C/γ-Al2O3 with Li and Na has not been attempted in literature for CO2 hydrogenation.

Methodology Applied
Scientific EffectElectronic structure modification: Dopants

Data Source

PatentUS11890598B2Alkali metal doped molybdenum carbide supported on gamma-alumina for selective CO<sub>2 </sub>hydrogenation into CO
Publication Date: 2024.02.06 THE UNITED STATES OF AMERICA AS REPRESENTED BY THE SECRETARY OF THE NAVY
  • US11890598B2 patent drawing
  • US11890598B2 patent drawing
  • US11890598B2 patent drawing

AI summary

A supported heterogeneous catalyst material for catalyzing the reverse water-gas shift (RWGS) reaction for the selective formation of CO using an alkali metal-doped molybdenum carbide on a gamma alumina support (A-Mo2C/γ-Al2O3, A=K, Na, Li). The A-Mo2C/γ-Al2O3 catalyst is synthesized by co-impregnation of molybdemun and alkali metal precursors onto a γ-Al2O3 support. It is then carburized to form the A-Mo2C/γ-Al2O3.