Methanol Dehydration Catalyst with Promoter for Dimethyl Ether

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Solution Overview

Problem

Current dehydration processes for methanol to dimethyl ether using high temperatures result in co-production of hydrocarbons, reducing catalytic performance, and existing catalysts do not effectively maintain productivity over time.

Innovation Solution

The use of a solid Brønsted acid catalyst, such as aluminosilicate zeolites with a maximum free sphere diameter greater than 3.67 Angstroms or heteropolyacids, in combination with a promoter like methyl formate, dimethyl oxalate, or dimethyl malonate, at a molar ratio less than 1, to enhance the dehydration reaction efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high reaction temperatures (250°C and higher) are used to achieve acceptable reaction rates, then productivity is improved, but hydrocarbons are co-produced and catalytic performance is reduced

Engineering Contradiction:
Improvereaction rateVSAvoidhydrocarbon co-production
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the chemical parameter of the catalyst system by introducing promoter compounds (metal salts or metal oxides) to modify the catalytic properties. This allows the reaction to proceed at lower temperatures (below 250°C) while maintaining acceptable productivity, thereby preventing hydrocarbon co-production that occurs at high temperatures.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a composite catalyst system consisting of a solid acid catalyst combined with promoter compounds (metal salts or metal oxides). This composite structure enhances catalytic activity and selectivity, enabling efficient methanol dehydration at lower temperatures without significant hydrocarbon formation.

Inventive Principle:
Principle #40Composite materials

2Productivity

If high reaction temperatures are used to maintain productivity over time, then output is sustained, but catalyst stability deteriorates

Engineering Contradiction:
Improvesustained outputVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent modifies the catalytic system by adding promoter compounds that enhance catalyst stability. This modification allows the catalyst to maintain its activity and selectivity over extended periods at lower operating temperatures, preventing the deactivation and hydrocarbon formation that occur with prolonged high-temperature operation.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The promoter compounds act as intermediaries that facilitate the dehydration reaction while protecting the catalyst from deactivation. These metal salts or metal oxides modify the catalyst surface properties, enhancing its stability and resistance to coking and other deactivation mechanisms that occur at high temperatures.

Inventive Principle:
Principle #24Intermediary (Mediator)

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

This approach improves the productivity of dimethyl ether production by maintaining catalytic performance and reducing the need for increased reaction temperatures, thereby minimizing the formation of undesirable by-products and extending catalyst stability.

Implementation Method 1

a process for dehydrating methanol to dimethyl ether product in the presence of a catalyst selected from aluminosilicate zeolites which have a maximum free sphere diameter of greater than 3.67 Angstroms and heteropolyacids

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS11673851B2Process for dehydrating methanol to dimethyl ether product
Publication Date: 2023.06.13 BRITISH PETROLEUM CO PLC

AI summary

A process the dehydration of methanol to dimethyl ether in the presence of a solid Brønsted acid catalyst selected from aluminosilicate zeolites which have a maximum free sphere diameter of greater than 3.67 Angstroms and heteropolyacids and a promoter selected from methyl formate, dimethyl oxalate and dimethyl malonate and the molar ratio of promoter to methanol is maintained at less than 1.