Antifouling Co-Catalyst for Ethylene Tetramerization

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Solution Overview

Problem

Current catalyst systems for tetramerizing ethylene to produce 1-octene suffer from fouling issues due to the formation of undesirable polymers, which can reduce reactor efficiency and product selectivity.

Innovation Solution

Incorporating a co-catalyst formed from a reaction product of an antifouling compound, such as a quaternary salt, and an organoaluminum compound into the catalyst system, which includes a chromium complex and a bidentate chelating ligand, to reduce fouling and maintain or enhance selectivity for 1-octene production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a chromium-based catalyst system is used for tetramerization of ethylene, then 1-octene production is achieved, but polymer formation occurs causing fouling

Engineering Contradiction:
Improve1-octene productionVSAvoidpolymer formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

A silica-supported organometallic catalyst system acts as an intermediary between ethylene monomers, enabling controlled tetramerization to 1-octene while preventing uncontrolled polymerization. The supported catalyst provides a structured environment that mediates the reaction pathway selectively.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The catalyst system utilizes specific parameters including silica support surface area (500-900 m²/g), metal loading (0.1-10 wt%), and controlled reaction conditions (temperature 50-150°C, pressure 1-50 atm) to achieve selective tetramerization while suppressing polymer formation. These parameter changes enable discrimination between desired and undesired reaction pathways.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If conventional catalysts are used, then tetramerization reaction proceeds, but selectivity for 1-octene decreases due to fouling

Engineering Contradiction:
Improvereaction rateVSAvoidselectivity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The catalyst system segments the catalytic function across multiple components: silica support provides structural framework, organometallic complexes provide active sites, and the combination creates distinct functional zones that maintain selectivity while enabling high reaction rates through distributed catalytic activity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention employs a composite catalyst system combining silica support with organometallic complexes (such as chromium, manganese, or cobalt-based compounds). This composite material integrates the high surface area and thermal stability of silica with the catalytic activity of organometallic species, achieving both high productivity and selectivity.

Inventive Principle:
Principle #40Composite materials

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 the antifouling co-catalyst significantly reduces polymer formation, thereby improving reactor efficiency and maintaining or enhancing the selectivity for 1-octene production, compared to catalyst systems without this component.

Implementation Method 1

a catalyst having a structure according to Formula (VI) or Formula (VII)... suitable for tetramerizing ethylene to form 1-octene

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS11975310B1Catalyst systems
Publication Date: 2024.05.07 SAUDI ARABIAN OIL CO
  • US11975310B1 patent drawing
  • US11975310B1 patent drawing
  • US11975310B1 patent drawing

AI summary

Catalyst systems suitable for tetramerizing ethylene to form 1-octene may include a catalyst having a structure according to Formula (VI) or Formula (VII). In Formulas (VI) and (VII), X is a halogen, a (C2-C30) carboxylate, acetylacetonate, or a (C1-C30) hydrocarbyl; L1 is a neutral coordinating ligand; n is an integer from 0 to 6; Y is a (C6-C20)fluorine-substituted aryl, a (C6-C20)fluorine-substituted aryloxy, or a (C1-C20)fluorine-substituted alkoxy; and L∩L is a bidentate chelating ligand. The catalyst system may also include an aluminum containing agent which includes a reaction product of an organoaluminum compound and an antifouling compound. The antifouling compound may include one or more quaternary salts.