Zeolite Pentagonal Sheet Morphology Oligomerization

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Solution Overview

Problem

Current oligomerization processes for olefins require high temperature and high pressure conditions, leading to operational complications, poor yield, and catalyst deactivation, making them unsafe and economically unfeasible for industrial applications, particularly in achieving selective dimer and trimer production.

Innovation Solution

A process using a zeolite catalyst with a pentagonal sheet morphology, operating at pressures between 8-20 bars and temperatures between 60-100°C, to selectively produce higher molecular weight oligomers, such as C8 hydrocarbons, while allowing for cost-effective catalyst regeneration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Speed

If high temperature and high pressure conditions are used for oligomerization, then the reaction rate increases, but operational safety deteriorates and catalyst deactivation accelerates

Engineering Contradiction:
Improvereaction rateVSAvoidoperational safety
Core Design Contradiction:
SpeedVSReliability

Solution Approach 1:

The patent changes the reaction parameters from high temperature and high pressure to moderate temperature (60-100°C) and moderate pressure (8-20 bar) conditions. This parameter change maintains adequate reaction rate while significantly improving operational safety and preventing catalyst deactivation, directly resolving the technical contradiction between reaction speed and reliability.

Inventive Principle:
Principle #35Parameter changes

2Speed

If high temperature and high pressure conditions are used for oligomerization, then the reaction proceeds faster, but catalyst activity is lost rapidly

Engineering Contradiction:
Improvereaction rateVSAvoidcatalyst activity duration
Core Design Contradiction:
SpeedVSDuration of action of stationary object

Solution Approach 1:

The patent employs moderate reaction conditions (60-100°C, 8-20 bar) that are gentle enough to preserve catalyst structure and activity over extended periods. This approach maintains sufficient reaction rate while dramatically extending catalyst lifetime, resolving the contradiction between reaction speed and catalyst durability.

Inventive Principle:
Principle #35Parameter changes

3Device complexity

If conventional oligomerization conditions are used, then the process is simpler, but product selectivity for dimers and trimers deteriorates

Engineering Contradiction:
Improveprocess complexityVSAvoidproduct selectivity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent achieves high dimer and trimer selectivity by optimizing reaction parameters (temperature 60-100°C, pressure 8-20 bar) rather than complicating the process equipment. This parameter optimization allows conventional simple equipment to produce highly selective products, resolving the contradiction between process simplicity and product precision.

Inventive Principle:
Principle #35Parameter changes

4Productivity

If zeolite catalysts are used to increase oligomer yield, then productivity improves, but catalyst regeneration becomes expensive and complex

Engineering Contradiction:
Improveoligomer yieldVSAvoidregeneration complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent uses moderate reaction conditions that prevent severe catalyst deactivation, allowing simple thermal regeneration methods to restore catalyst activity. This approach maintains high oligomer yield while avoiding complex and expensive regeneration processes, resolving the contradiction between productivity and regeneration complexity.

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

This approach enables safe, economical, and selective production of higher molecular weight oligomers, improving yield and selectivity for dimerized and trimerized hydrocarbons, specifically C8 hydrocarbons, under milder conditions, thus overcoming the limitations of existing methods.

Implementation Method 1

contacting a feedstock with a zeolite catalyst under conditions of oligomerization at pressure between 8-20 bars and temperature in the range of 60-100° C. to obtain oligomers

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS10647629B2Oligomerization process involving crystalline molecular sieve
Publication Date: 2020.05.12 HINDUSTAN PETROLEUM CORP LTD
  • US10647629B2 patent drawing
  • US10647629B2 patent drawing
  • US10647629B2 patent drawing

AI summary

A process for oligomerization of olefins includes contacting a feedstock with a zeolite catalyst under conditions of oligomerization at pressure between 8-20 bars and temperature in the range of 60-100° C. to obtain oligomers, wherein, the zeolite catalyst has a pentagonal sheet morphology.