Manganese Copper Catalyst Activation for Ether Selectivity

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Solution Overview

Problem

Conventional processes for producing tetrahydrofuran often require expensive downstream processing and result in catalysts that are not robust enough to maintain high conversion and selectivity under varying operating conditions, leading to increased by-product formation at higher temperatures.

Innovation Solution

Activating a reduced manganese copper catalyst under a hydrogen stream at temperatures between 300° C. to 400° C. improves its robustness and selectivity for producing ethers, allowing for higher tetrahydrofuran yields without the need for extensive downstream processing and maintaining longevity in ether production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional catalysts are used for ether production, then the process can operate at higher temperatures to increase productivity, but by-product formation increases and selectivity deteriorates

Engineering Contradiction:
Improveether production rateVSAvoidby-product formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by modifying the catalyst's chemical composition parameters - specifically incorporating manganese oxide (0.1-10 wt%) and zinc oxide (0.1-10 wt%) as promoters in the copper-based catalyst. This chemical parameter modification enables the catalyst to maintain high selectivity for ether production even at elevated operating temperatures (200-400°C), thereby resolving the contradiction between productivity and by-product formation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite materials by creating a multi-component catalyst system comprising copper oxide as the base catalyst combined with manganese oxide and zinc oxide promoters. This composite catalyst structure synergistically enhances both the activity and selectivity for ether production, allowing the process to operate at higher temperatures without increasing by-product formation, thus resolving the contradiction between productivity and selectivity

Inventive Principle:
Principle #40Composite materials

2Productivity

If operating conditions are varied to optimize ether yield, then productivity improves, but catalyst robustness deteriorates leading to decreased conversion and selectivity

Engineering Contradiction:
Improveether yieldVSAvoidcatalyst robustness
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent applies parameter changes by optimizing the catalyst's chemical composition with specific ranges of manganese oxide (0.1-10 wt%) and zinc oxide (0.1-10 wt%) promoters. This compositional parameter optimization creates a catalyst that maintains stable conversion and selectivity performance across varying operating conditions, thereby resolving the contradiction between productivity and catalyst robustness

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent applies beforehand cushioning by incorporating promoter oxides (manganese and zinc) into the catalyst structure before operation. These promoters act as structural and chemical stabilizers that cushion the catalyst against deactivation and performance degradation when operating conditions vary, thereby maintaining both high productivity and robustness simultaneously

Inventive Principle:
Principle #11Beforehand cushioning (Prior cushioning)

3Device complexity

If downstream processing is reduced to lower device complexity, then manufacturing cost decreases, but manufacturing precision deteriorates requiring extensive processing to achieve desired product purity

Engineering Contradiction:
Improvedownstream processing stepsVSAvoidproduct purity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent applies parameter changes by modifying the reaction conditions parameters - specifically operating at elevated temperatures (200-400°C) and optimized pressure ranges (1-50 atm). These parameter changes shift the reaction selectivity to favor ether production, thereby simplifying downstream processing requirements while maintaining high product purity, resolving the contradiction between device complexity and manufacturing precision

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent applies porous materials by utilizing a catalyst support structure with controlled porosity that facilitates selective catalysis. The porous structure provides high surface area for active sites while enabling efficient mass transfer, which enhances ether selectivity and simplifies product separation, thereby resolving the contradiction between downstream processing complexity and product purity

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 activated catalyst achieves nearly 100% conversion of desired ethers with reduced by-product formation, such as butanol, and maintains production efficiency over time, even at higher temperatures, while minimizing the impact of water in the feed.

Implementation Method 1

Activating a reduced manganese copper catalyst under a hydrogen stream at temperatures between 300° C. to 400° C. improves its robustness and selectivity for producing ethers

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

The reaction will generally be by hydrogenation and/or dehydration

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 3

The reaction will generally be by hydrogenation and/or dehydration

Methodology Applied
Scientific EffectDehydration:

Data Source

PatentUS8816104B2Process
Publication Date: 2014.08.26 JOHNSON MATTHEY DAVY TECHNOLOGIES LTD
  • US8816104B2 patent drawing

AI summary

A process for activating a reduced manganese copper catalyst comprising treating the catalyst at a temperature of more than 300° C. to about 400° C. with hydrogen.