Multimodal Polyethylene Catalyst for Stable Multi-Stage Polymerization

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Solution Overview

Problem

Existing metallocene catalysts struggle to produce multimodal polyethylene polymers effectively in multi-stage polymerization processes due to challenges in maintaining stability, activity, and molecular weight control across different reaction conditions, particularly in slurry and gas phases.

Innovation Solution

The use of bridged bis-cyclopentadienyl type metallocene complexes with heterocyclic substituents, such as furanyl moieties, supported on a carrier, which exhibit high activity and comonomer incorporation capabilities, allowing for the production of multimodal polyethylene polymers with controlled molecular weights in both slurry and gas phases.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Stability of the object's composition

If conventional metallocene catalysts are used in multi-stage polymerization, then catalyst stability is improved, but molecular weight control and activity across different phases deteriorates

Engineering Contradiction:
Improvecatalyst stabilityVSAvoidcatalyst activity
Core Design Contradiction:
Stability of the object's compositionVSProductivity

Solution Approach 1:

The patent modifies the catalyst structure by changing parameters such as introducing heterocyclic substituents (furanyl moieties) on the cyclopentadienyl rings and using bridged bis-cyclopentadienyl configurations. These structural parameter changes enable the catalyst to maintain stability while achieving high activity in both slurry and gas phase polymerizations, resolving the contradiction between stability and productivity.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention creates a composite catalyst system combining metallocene complexes with heterocyclic substituents and bridged structures. This composite approach allows the catalyst to exhibit both stability (from the metallocene core) and enhanced activity (from the heterocyclic and bridged modifications), simultaneously satisfying both requirements.

Inventive Principle:
Principle #40Composite materials

2Manufacturing precision

If single site catalysts are used to produce controlled polymer structures, then manufacturing precision is improved, but adaptability to multi-stage processes deteriorates

Engineering Contradiction:
Improvepolymer structure controlVSAvoidmulti-stage process adaptability
Core Design Contradiction:
Manufacturing precisionVSAdaptability or versatility

Solution Approach 1:

The patent designs metallocene catalysts with universal functionality by incorporating heterocyclic substituents and bridged structures that enable the same catalyst system to operate effectively in multiple polymerization stages and phases. The catalyst maintains precise polymer structure control while adapting to different reaction conditions, achieving both manufacturing precision and process adaptability.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Solution Approach 2:

By adjusting catalyst structure parameters (heterocyclic substituents, bridged configurations), the invention creates a single-site catalyst that can adapt to multi-stage processes. The parameter changes enable the catalyst to maintain its single-site characteristics for precise control while gaining the versatility needed for multi-stage operation.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If catalyst activity is increased in gas phase, then productivity is improved, but stability in slurry phase deteriorates

Engineering Contradiction:
Improvegas phase activityVSAvoidslurry phase stability
Core Design Contradiction:
ProductivityVSStability of the object's composition

Solution Approach 1:

The patent employs parameter changes by introducing heterocyclic substituents and bridged structures that differentially enhance catalyst properties. These structural modifications increase gas phase activity while maintaining slurry phase stability, resolving the contradiction between productivity and stability across different phases.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention applies local quality by having different parts of the catalyst structure serve different functions: the metallocene core provides stability in slurry phase, while the heterocyclic substituents and bridged structures enhance gas phase activity. This localized functional differentiation resolves the phase-specific performance contradiction.

Inventive Principle:
Principle #3Local quality

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

These catalysts provide stable kinetic profiles in slurry phase and enhanced activity in gas phase, enabling the production of multimodal polyethylene polymers with high molecular weight and comonomer incorporation, addressing the limitations of previous catalysts in multi-stage processes.

Implementation Method 1

polymerising ethylene and optionally at least one C4-10 alpha olefin comonomer in a first stage in the presence of a metallocene catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS12595325B2Process for the preparation of a multimodal polyethylene
Publication Date: 2026.04.07 BOREALIS AG
  • US12595325B2 patent drawing
  • US12595325B2 patent drawing
  • US12595325B2 patent drawing

AI summary

The invention provides a process for the preparation of a multimodal ethylene polymer in a multistage process in the presence of a catalyst comprising a complex of formula (Ix) wherein each X is a sigma donor ligand; each Het is independently a monocyclic or multicyclic heteroaromatic or heterocyclic group containing at least one heteroatom selected from O, N or S; L is a carbon, silicon or germanium based divalent bridge in which one or two backbone atoms link the ligands; M is Ti, Zr or Hf; each R1 is the same or different and is a linear C1-10 alkyl group, or linear C1-10 alkoxy, each n is 0 to 3; each R2 is the same or different and is a C1-10 alkyl group, C1-10 alkoxy group or —Si(R)3 group; each R is the same or different and is C1-10 alkyl or phenyl group optionally substituted by 1 to 3 C1-6 alkyl groups; and each p is 0 to 3.