Plasma Catalytic Biogas Conversion for Selective Liquid Oxygenates

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Solution Overview

Problem

Current biogas conversion technologies face challenges in efficiently converting methane and carbon dioxide into high-value liquid oxygenates like methanol and acetic acid under mild conditions, lacking selectivity and requiring costly CO2 removal and energy-intensive processes.

Innovation Solution

An integrated plasma catalysis system using dielectric barrier discharge (DBD) plasma with plasma-treated mesoporous or microporous catalysts, such as Cu/γ-Al2O3, Co/γ-Al2O3, and Ni/γ-Al2O3, to convert biogas into tailored liquid oxygenates by adjusting process conditions and catalyst composition.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional plasma conversion is used, then biogas can be activated, but product selectivity is lacking and only syngas is produced

Engineering Contradiction:
Improvebiogas conversion efficiencyVSAvoidproduct selectivity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

Metal-based catalysts (Cu, Co, Ni) are introduced as intermediary substances that mediate between the plasma activation step and the final product formation. These catalysts selectively promote specific reaction pathways from the reactive plasma species to produce desired liquid oxygenates (methanol, acetic acid) rather than just syngas, thereby improving product selectivity while maintaining conversion efficiency

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent modifies plasma parameters (discharge power, frequency, gas flow rates) and catalyst parameters (metal type, loading amount, support material) to optimize the balance between conversion efficiency and product selectivity. By adjusting these parameters, the system achieves high productivity while favoring specific liquid product formation over syngas production

Inventive Principle:
Principle #35Parameter changes

2Productivity

If thermo-chemical conversion is used, then biogas can be converted to syngas, but high temperature and pressure are required

Engineering Contradiction:
Improvebiogas conversion rateVSAvoidprocess temperature
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent replaces thermal energy (heat) with non-thermal plasma energy to activate biogas molecules. Instead of using high temperature to drive the conversion reaction, the system uses electronically excited species and reactive radicals generated by plasma discharge at ambient or mild temperatures, thereby achieving high conversion rates without requiring extreme temperature conditions

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The patent utilizes the transition of energy forms from electrical energy to chemical energy through plasma generation. The electrical discharge creates a plasma state that transforms reactive species into highly energetic states, enabling chemical reactions at lower temperatures than conventional thermal methods, thus reducing energy input requirements while maintaining productivity

Inventive Principle:
Principle #36Phase transitions

3Manufacturing precision

If multiple synthesis steps are used, then specific products can be obtained, but process complexity and energy consumption increase

Engineering Contradiction:
Improveproduct specificityVSAvoidprocess steps
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent merges multiple conversion steps into a single integrated plasma catalytic reaction zone. Instead of separating CO2 and CH4 conversion steps or using multiple sequential reactions, the system combines all transformations into one reactor where plasma activation and catalytic conversion occur simultaneously, producing liquid oxygenates directly from biogas in a single step, thereby reducing process complexity

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The plasma catalytic system is designed to perform multiple functions simultaneously: activating biogas components, selecting specific reaction pathways, and producing various liquid oxygenates (methanol, acetic acid, ethanol) in one process. This multi-functional approach eliminates the need for separate synthesis steps for different products, reducing both device complexity and energy consumption while maintaining product specificity

Inventive Principle:
Principle #6Universality (Multi-functionality)

4Manufacturing precision

If CO2 removal is performed, then specific products can be produced, but cost increases

Engineering Contradiction:
Improveproduct purityVSAvoidCO2 removal cost
Core Design Contradiction:
Manufacturing precisionVSQuantity of substance

Solution Approach 1:

Instead of removing CO2 as a separate preliminary step, the patent converts CO2 directly into valuable liquid oxygenates (particularly acetic acid and ethanol) during the plasma catalytic process. The CO2 that would normally be considered a waste product or requires removal is actually utilized as a feedstock, converting a costly removal operation into a beneficial product formation step, thereby reducing overall process cost while maintaining product purity

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 system achieves selective conversion of biogas to methanol or acetic acid with high efficiency, allowing for the production of high-value chemicals in a single step under ambient conditions, optimizing product distribution through discharge power, catalyst type, and process parameters.

Implementation Method 1

Non-thermal plasmas activate inert gases at near room temperature by the highly energetic electrons that can promote reaction of the relatively stable components of biogas

Methodology Applied
Scientific EffectPlasma: Plasma

Implementation Method 2

Among various plasma reactors, dielectric barrier discharge (DBD) is widely used because of flexibility, ease of operation, and scalability

Methodology Applied
Scientific EffectDielectric barrier discharge: Electric Arc

Implementation Method 3

Some metal-based catalysts have been investigated in plasma conversion of CO2 and CH4. Transition metals like Cu promote methanol production, while Fe and Co lead to the formation of acetic acid

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS20250340501A1Non-thermal plasma catalytic conversion of biogas to acetic acid and methanol
Publication Date: 2025.11.06 THE CHINESE UNIVERSITY OF HONG KONG
  • US20250340501A1 patent drawing
  • US20250340501A1 patent drawing
  • US20250340501A1 patent drawing

AI summary

An integrated plasma catalysis system for biogas conversion includes a plasma-treated mesoporous or microporous catalyst and a plasma source for converting a biogas containing methane and carbon dioxide to a liquid oxygenates rich in methanol or acetic acid. Biogas from different solid wastes can be converted under ambient conditions to liquid oxygenates including methanol and acetic acid.