Methane to Methanol Catalyst via Dual-Catalyst Segmentation

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current methods for converting methane to methanol require high temperature and pressure, resulting in high costs and low yields, and existing catalysts like Periana catalyst have limited turnover numbers and frequencies, making them inefficient for methanol production.

Innovation Solution

A catalyst represented by specific formulas, which can produce a methanol precursor by reacting with methane in an acid solution under low temperature and pressure conditions, followed by conversion to methanol with improved turnover numbers and frequencies.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high temperature and pressure conditions are used to convert methane to methanol, then the reaction can proceed due to overcoming methane's thermochemical stability, but the equipment cost increases and yield decreases

Engineering Contradiction:
Improvemethanol production yieldVSAvoidequipment cost
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent changes the reaction parameters by using a novel catalyst system that enables methane conversion at lower temperatures (200-400°C) and pressures compared to conventional methods. This parameter change resolves the contradiction by maintaining reaction efficiency while reducing equipment requirements and costs.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces a dual-catalyst system where the first catalyst (complex of formula 1 or 2) activates methane and the second catalyst (from formula 3-9) converts the intermediate to methanol. This intermediary mechanism allows the reaction to proceed under milder conditions, reducing equipment complexity while maintaining high yield.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Temperature

If the Periana catalyst is used to synthesize methanol from methane, then the reaction can proceed at lower temperature, but the turnover number and turnover frequency are limited

Engineering Contradiction:
Improvereaction temperatureVSAvoidturnover number and turnover frequency
Core Design Contradiction:
TemperatureVSProductivity

Solution Approach 1:

The patent uses a composite catalyst system combining two different catalysts with complementary functions. The first catalyst (formula 1 or 2) provides low-temperature activation capability, while the second catalyst (formula 3-9) enhances conversion efficiency. This composite approach resolves the contradiction by achieving both low temperature operation and high productivity.

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent segments the catalytic process into two distinct stages with different catalysts optimized for each stage. This segmentation allows each catalyst to be specialized for its specific function, achieving both low temperature operation in the first stage and high turnover frequency in the second stage, thus resolving the contradiction.

Inventive Principle:
Principle #1Segmentation

3Productivity

If heterogeneous catalysts are used to react methane with oxygen, then high conversion ability is achieved, but selectivity is very low and high temperature is required

Engineering Contradiction:
Improvemethane conversion abilityVSAvoidselectivity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent uses an organic intermediate (methyl hydroperoxide or similar) as a mediator between methane and oxygen. The first catalyst activates methane to form this intermediate with high selectivity, then the second catalyst converts the intermediate to methanol. This intermediary approach resolves the contradiction by achieving both high conversion and high selectivity that cannot be obtained with direct heterogeneous catalysis.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent replaces the mechanical/physical heterogeneous catalyst system with a chemical mechanism involving soluble organic catalysts and intermediate formation. This substitution enables precise control over selectivity through chemical mechanism design while maintaining high conversion through the two-catalyst system, resolving the contradiction between conversion ability and selectivity.

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

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-yield methanol production with increased turnover numbers and frequencies compared to conventional platinum catalysts, maintaining stability and economic efficiency, and can be reused without regeneration.

Implementation Method 1

a catalyst for producing a methanol precursor, represented by Formula 1

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

reacting methane gas with oxygen using a heterogeneous catalyst

Methodology Applied
Scientific EffectOxidation: Oxidation

Data Source

PatentUS10138188B2Catalyst for producing methanol precursor, methanol precursor produced using the catalyst and methanol produced using the methanol precursor
Publication Date: 2018.11.27 KOREA INST OF SCI & TECH
  • US10138188B2 patent drawing
  • US10138188B2 patent drawing
  • US10138188B2 patent drawing

AI summary

Disclosed is a novel catalyst for producing a methanol precursor. The use of the catalyst enables the production of a methanol precursor and methanol with high efficiency under low temperature and low pressure conditions. Also disclosed are a methanol precursor produced using the catalyst and methanol produced using the methanol precursor.