WO3/MCM-48 Catalyst for 1-Butene Isomerization

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Solution Overview

Problem

Conventional isomerization catalysts for producing 1-butene from 2-butene-containing feedstocks are inefficient, resulting in low conversion rates and yields, especially when operating at elevated temperatures, which cannot meet the growing demand for 1-butene.

Innovation Solution

A method involving a MCM-48 catalyst with WO3 incorporated into its silica framework, used at reactor temperatures between 150° C. and 350° C. to enhance the isomerization of 2-butene to 1-butene, promoting increased catalytic activity and yield while avoiding metathesis reactions that convert 1-butene to propene.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional isomerization catalysts are used to produce 1-butene from 2-butene, then the process can operate at elevated temperatures, but the conversion rate and yield of 1-butene are low

Engineering Contradiction:
Improve1-butene yieldVSAvoidconversion rate
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent changes the operating temperature parameter from conventional elevated temperatures to a specific range of 150-350°C, which optimizes the catalytic activity for 2-butene conversion to 1-butene while maintaining high yield and conversion rate

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent uses a composite catalyst system consisting of MCM-48 zeolite combined with WO3 (tungsten oxide) deposited on the zeolite surface. This composite material synergistically combines the acidic sites of MCM-48 with the catalytic properties of WO3 to achieve high conversion and yield at lower temperatures

Inventive Principle:
Principle #40Composite materials

2Productivity

If conventional isomerization catalysts are used, then the process is simple, but the catalytic activity at temperatures below 350°C is insufficient

Engineering Contradiction:
Improvecatalytic activityVSAvoidreactor temperature
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent modifies the temperature parameter by operating in the 150-350°C range rather than conventional higher temperatures, while the WO3/MCM-48 catalyst system maintains high catalytic activity at these lower temperatures, thus resolving the contradiction between temperature and activity

Inventive Principle:
Principle #35Parameter changes

3Speed

If higher temperatures are used for isomerization, then the reaction rate increases, but metathesis reactions occur that convert 1-butene to propene

Engineering Contradiction:
Improvereaction rateVSAvoidmetathesis reaction
Core Design Contradiction:
SpeedVSObject-generated harmful factors

Solution Approach 1:

The patent controls the temperature parameter within 150-350°C, which is sufficient to achieve high reaction rates for isomerization while being low enough to prevent metathesis reactions that would convert 1-butene to propene, thus resolving the contradiction between reaction rate and harmful side reactions

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 use of WO3/MCM-48 catalyst at reduced temperatures significantly increases the conversion of 2-butene to 1-butene, achieving higher yields and maintaining thermal stability, thus addressing the inefficiencies of conventional catalysts and meeting the demand for 1-butene production.

Implementation Method 1

contacting the hydrocarbon feed with the isomerization catalyst in the reactor at a temperature from 150° C. to 350° C. to produce an isomerization reaction effluent comprising 1-butene

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS11319263B1Methods for low temperature production of 1-butene
Publication Date: 2022.05.03 SAUDI ARABIAN OIL CO
  • US11319263B1 patent drawing
  • US11319263B1 patent drawing
  • US11319263B1 patent drawing

AI summary

Methods of producing 1-butene from a 2-butene-containing feedstock include feeding a hydrocarbon feed comprising 2-butene to a reactor, the reactor containing an isomerization catalyst and contacting the hydrocarbon feed with the isomerization catalyst in the reactor at a temperature from 150° C. to 350° C. to produce an isomerization reaction effluent comprising 1-butene. Further, the isomerization catalyst comprises a MCM-48 catalyst with WO3 incorporated into a silica framework of the MCM-48 catalyst.