Silver Catalyst Selectivity via Fluoride Carrier and CO2 Control

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Solution Overview

Problem

Silver-based catalysts used in olefin epoxidation processes face challenges in maintaining high selectivity and stability over time, requiring increased reaction temperatures that can lead to equipment limitations and reduced product yield.

Innovation Solution

A process using a catalyst with a silver component and a high-selectivity dopant, such as rhenium, deposited on a fluoride-mineralized carrier, which maintains high selectivity and stability by controlling carbon dioxide levels in the feed below 2 mole-%, achieving selectivity greater than 85% and extending catalyst life.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If the reaction temperature is increased to maintain olefin oxide production as the catalyst ages, then the productivity is maintained, but the selectivity to the desired olefin oxide decreases

Engineering Contradiction:
Improveolefin oxide productionVSAvoidselectivity to olefin oxide
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent modifies the chemical composition parameters of the catalyst by incorporating specific dopants (rhenium at 0.1-3.0 mmole/kg, alkali metals at 0.01-1.0 mmole/kg) and using a fluoride-mineralized carrier, which changes the catalyst's intrinsic properties to maintain high selectivity across a wider temperature range and extended operational period

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent creates a composite catalyst system combining silver (0.5-5.0 mmole/kg) with multiple dopant elements (rhenium, alkali metals) on a fluoride-mineralized alumina carrier, where the synergistic interaction between components maintains both activity and selectivity during aging

Inventive Principle:
Principle #40Composite materials

2Productivity

If the reaction temperature is increased to maintain olefin oxide production, then the productivity is maintained, but the equipment tolerance is exceeded and catalyst stability decreases

Engineering Contradiction:
Improveolefin oxide productionVSAvoidcatalyst stability and equipment tolerance
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent optimizes the catalyst's chemical composition to enhance its thermal stability and resistance to deactivation, allowing the process to operate at lower temperatures for extended periods without exceeding equipment tolerance limits

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent uses dopant levels that exceed conventional amounts (particularly rhenium up to 3.0 mmole/kg and fluoride treatment) to create an over-engineered catalyst with enhanced stability margins, allowing operation well within equipment temperature limits while maintaining productivity

Inventive Principle:
Principle #16Partial or excessive action

3Loss of substance

If carbon dioxide is recovered and recycled in the feed, then the loss of substance is reduced, but the carbon dioxide accumulates and reduces catalyst performance

Engineering Contradiction:
Improveunconverted olefin and oxygen recoveryVSAvoidcatalyst selectivity
Core Design Contradiction:
Loss of substanceVSManufacturing precision

Solution Approach 1:

The patent identifies carbon dioxide concentration as a critical parameter affecting catalyst performance and establishes optimal ranges (0.1-5.0% by volume) that balance CO2 recycling benefits with catalyst selectivity maintenance, preventing accumulation to harmful levels

Inventive Principle:
Principle #35Parameter changes

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 high initial peak selectivity and improved stability, allowing for longer catalyst use and increased olefin oxide production with selectivity maintained above 90% even after significant cumulative production.

Implementation Method 1

The catalyst comprises silver, usually with one or more additional elements deposited therewith, on a carrier, typically an alpha-alumina carrier. The olefin is reacted with oxygen to form an olefin oxide.

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

a catalyst comprising a silver component and a high-selectivity dopant deposited on a fluoride-mineralized carrier

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 3

The olefin oxide may be reacted with water to form a 1,2-diol

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Implementation Method 4

with an alcohol to form a 1,2-diol ether, or with an amine to form an alkanolamine

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Data Source

PatentUS7528270B2Process for the production of an olefin oxide, a 1, 2-diol, a 1,2-diol ether, or an alkanolamine
Publication Date: 2009.05.05 SHELL USA INC
  • US7528270B2 patent drawing

AI summary

A process is provided for the epoxidation of an olefin comprising the steps of: contacting a feed comprising an olefin and oxygen with a catalyst comprising a silver component and a high-selectivity dopant deposited on a fluoride-mineralized carrier; and producing a product mix comprising an olefin oxide, wherein the concentration of carbon dioxide in the feed is less than about 2 mole-%, relative to the total feed.