Partially Neutralised Heteropolyacid Catalysts for Ethanol Dehydration

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Solution Overview

Problem

Conventional heteropolyacid catalysts used in ethanol dehydration for producing ethene suffer from rapid deactivation due to carbon build-up, leading to reduced catalyst lifetime and increased costs associated with frequent regeneration and waste management.

Innovation Solution

Partial neutralization of heteropolyacid catalysts by replacing hydrogen atoms with cations such as alkali metal, alkaline earth metal, or ammonium ions extends catalyst lifetime by modifying surface chemistry and reducing deactivation mechanisms, allowing continuous operation for several hundred hours without regeneration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional heteropolyacid catalysts are used in ethanol dehydration, then the catalyst provides initial high activity, but the catalyst lifetime is short due to rapid deactivation from carbon build-up

Engineering Contradiction:
Improvecatalyst lifetimeVSAvoidcarbon build-up
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by modifying the chemical composition of the heteropolyacid catalyst through partial neutralization. Specifically, it replaces some hydrogen atoms with alkali metal cations (such as sodium, potassium, or cesium) to create partially neutralized heteropolyacid catalysts. This chemical parameter modification reduces the catalyst's affinity for carbonaceous deposits, thereby decreasing carbon build-up and extending catalyst lifetime while maintaining adequate activity for ethanol dehydration

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the harmful effect of carbon build-up into a beneficial outcome by using partial neutralization to modify the catalyst surface properties. The neutralized catalyst maintains sufficient acidity to promote dehydration while simultaneously reducing the harmful carbon deposition that causes deactivation. This transforms the typical trade-off where high acidity leads to both high activity and high carbon build-up, into a scenario where modified acidity provides both activity and resistance to deactivation

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

2Productivity

If heteropolyacid catalysts are used to improve selectivity and reduce ethane formation, then productivity increases, but catalyst deactivation occurs more rapidly

Engineering Contradiction:
Improveethene production rateVSAvoidcatalyst operational duration
Core Design Contradiction:
ProductivityVSDuration of action of stationary object

Solution Approach 1:

The patent modifies the chemical parameters of the heteropolyacid catalyst by implementing partial neutralization with alkali metal cations. This parameter change creates a balanced catalyst that maintains the high selectivity and productivity characteristics of conventional heteropolyacids while simultaneously improving operational durability. The neutralized catalyst preserves the active sites needed for high ethene production rates while reducing the rate of deactivation, thereby extending the operational duration before regeneration is required

Inventive Principle:
Principle #35Parameter changes

3Productivity

If frequent catalyst regeneration is performed to maintain activity, then productivity is maintained, but operational time and economic costs increase

Engineering Contradiction:
Improvecontinuous production capabilityVSAvoidregeneration downtime
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The patent applies preliminary action by pre-modifying the catalyst through partial neutralization before it enters service. This preliminary chemical modification endows the catalyst with inherent resistance to carbon build-up and deactivation. As a result, the catalyst can operate continuously for extended periods without requiring regeneration, eliminating the need for periodic shutdowns and regeneration operations that cause time loss and reduce overall productivity

Inventive Principle:
Principle #10Preliminary action

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 process achieves extended catalyst lifetime, maintaining at least 25% to 85% of maximum activity over prolonged operation periods, reducing the need for frequent catalyst regeneration and associated economic and environmental burdens.

Implementation Method 1

The production of ethene by the vapour phase chemical dehydration of ethanol is a well-known chemical reaction which has been operated industrially for many years

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

It is known that oxygenate dehydration can lead to carbon build-up on acidic catalysts, such as silicotungstic-SiO2, which leads to catalyst deactivation

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS10464051B2Process for producing alkenes from oxygenates by using supported partially neutralised heteropolyacid catalysts
Publication Date: 2019.11.05 TECHNIP E&C LTD
  • US10464051B2 patent drawing
  • US10464051B2 patent drawing
  • US10464051B2 patent drawing

AI summary

A process for the vapour phase chemical dehydration of ethanol in a reactor in the presence of a supported heteropolyacid catalyst, said process comprising a step of contacting the ethanol with the heteropolyacid catalyst, wherein the heteropolyacid catalyst comprises a partially neutralised silicotungstic acid salt, wherein the partially neutralised silicotungstic acid salt has from 30% to 70% of the hydrogen atoms replaced with cations selected from the group consisting of alkali metal cations, alkaline earth metal cations, transition metal cations, ammonium cations, and mixtures thereof; but with the proviso that the alkali metal cation is not lithium; and wherein, after attaining steady-state performance of the catalyst, said process is operated continuously with the same supported heteropolyacid catalyst for at least 150 hours, without any regeneration of the catalyst.