Multi-Component Catalyst System for Single-Zone Heterophasic Copolymer Production

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Solution Overview

Problem

Current processes for forming propylene-based impact copolymers with improved impact properties require multiple reactors, resulting in high capital and operating costs, necessitating a more efficient single reaction zone process.

Innovation Solution

A multi-component catalyst system comprising a first catalyst component, such as a Ziegler-Natta or metallocene catalyst, and a second catalyst component with enhanced ethylene response, capable of forming heterophasic copolymers with controlled xylene solubles levels, is introduced into a single reaction zone with propylene and ethylene monomers to produce polymers with improved impact properties.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Strength

If multiple reactors are used to form propylene-based impact copolymers, then impact properties are improved, but capital and operating costs increase

Engineering Contradiction:
Improveimpact propertiesVSAvoidnumber of reactors
Core Design Contradiction:
StrengthVSDevice complexity

Solution Approach 1:

The patent combines multiple catalyst systems with different functionalities into a single reactor system. The first catalyst system forms the propylene homopolymer matrix while the second catalyst system simultaneously incorporates ethylene to create heterophasic copolymer structures, achieving impact improvement without requiring separate reactor trains.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The invention uses composite catalyst systems where multiple catalyst components work together to produce polymers with complex microstructures. The combination of catalysts enables formation of heterophasic copolymers with controlled morphology and composition, achieving properties previously requiring multiple processing steps.

Inventive Principle:
Principle #40Composite materials

2Device complexity

If a single reaction zone is used, then capital and operating costs are reduced, but control over polymer composition and properties becomes more difficult

Engineering Contradiction:
Improvenumber of reactorsVSAvoidcontrol over polymer composition
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

Different regions of the single reactor are optimized for different functions through the use of multiple catalyst systems with spatially distributed activities. The first catalyst zone predominately forms propylene homopolymer while the second catalyst zone simultaneously creates ethylene incorporation zones, achieving compositional control within a single reaction zone.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent controls polymer composition by varying parameters such as monomer feed ratios, temperature gradients, and catalyst activation conditions within the single reactor. These parameter changes enable precise control over the heterophasic copolymer structure and xylene solubles content despite the simplified reactor configuration.

Inventive Principle:
Principle #35Parameter changes

3Strength

If xylene solubles content is increased, then impact properties improve, but melting point consistency may be affected

Engineering Contradiction:
Improveimpact propertiesVSAvoidmelting point consistency
Core Design Contradiction:
StrengthVSStability of the object's composition

Solution Approach 1:

The dual-catalyst system creates localized regions with different polymer characteristics within the same product batch. The first catalyst produces isotactic propylene regions maintaining high melting points, while the second catalyst creates heterophasic copolymer regions with higher xylene solubles content and improved impact properties, achieving both goals simultaneously.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The resulting polymer is a composite structure at the molecular level, combining homopolymer and copolymer phases within the same material. This composite architecture allows the material to exhibit both high melting point (from the homopolymer matrix) and improved impact strength (from the heterophasic copolymer phases).

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 multi-component catalyst system enables the formation of heterophasic copolymers with enhanced impact properties in a single reaction zone, reducing costs and maintaining consistent melting points while increasing xylene solubles levels, comparable to those produced in series reactors.

Implementation Method 1

A multi-component catalyst system comprising a first catalyst component, such as a Ziegler-Natta or metallocene catalyst, and a second catalyst component with enhanced ethylene response

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS8759243B2Multi-component catalyst systems and polymerization processes for forming in-situ heterophasic copolymers and/or varying the xylene solubles content of polyolefins
Publication Date: 2014.06.24 FINA TECH INC
  • US8759243B2 patent drawing

AI summary

Embodiments of the invention generally include multi-component catalyst systems, polymerization processes and heterophasic copolymers formed by the processes. The multi-component catalyst system generally includes a first catalyst component selected from Ziegler-Natta catalyst systems including a diether internal electron donor and a metallocene catalyst represented by the general formula XCpACpBMAn, wherein X is a structural bridge, CpA and CpB each denote a cyclopentadienyl group or derivatives thereof, each being the same or different and which may be either substituted or unsubstituted, M is a transition metal and A is an alkyl, hydrocarbyl or halogen group and n is an integer between 0 and 4. The multi-component catalyst system further includes a second catalyst component generally represented by the formula XCpACpBMAn, wherein X is a structural bridge, CpA and CpB each denote a cyclopentadienyl group or derivatives thereof, each being the same or different and which may be either substituted or unsubstituted, M is a transition metal and A is an alkyl, hydrocarbyl or halogen group and n is an integer between 0 and 4 and wherein the second catalyst component exhibits a higher ethylene response than the first catalyst component.