Low Density Ethylene Polymer Composition for Bubble Stability

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Solution Overview

Problem

Blown film production lines are limited by bubble stability, and existing ethylene-based polymer compositions fail to achieve an optimized balance of melt strength, optical, mechanical, and processing properties, particularly when using LDPE/LLDPE blends, which often result in poor film quality and increased production costs.

Innovation Solution

A composition comprising a first ethylene-based polymer with specific Mw(abs) and MS versus I2 relationships, and a second ethylene-based polymer with controlled melt index, density, and branching, produced through a high-pressure free-radical polymerization process in a tubular reactor, optimizing melt strength and processability while minimizing ultra-high molecular weight fractions that cause gel formation and reduce optical performance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If LDPE with very broad MWD and ultra high molecular weight fraction is used to increase melt strength, then bubble stability and film output are improved, but gel formation occurs and optical performance deteriorates

Engineering Contradiction:
Improvebubble stabilityVSAvoidgel formation
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent extracts and removes the ultra high molecular weight fraction (>10^6 g/mol) from the LDPE molecular weight distribution through controlled polymerization conditions. This eliminates the gel-forming component while retaining the beneficial broad MWD characteristics that provide high melt strength and bubble stability.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent changes the polymerization parameters including operating at lower conversion levels (10-30%), controlling temperature gradients, and adjusting residence time distribution in the reactor system. These parameter changes produce LDPE with broad MWD but without the ultra high molecular weight fraction that causes gels.

Inventive Principle:
Principle #35Parameter changes

2Ease of operation

If LDPE with very broad MWD is used to achieve high melt strength, then processing performance is improved, but optical performance of films is reduced

Engineering Contradiction:
Improveprocessing performanceVSAvoidoptical performance
Core Design Contradiction:
Ease of operationVSIllumination intensity

Solution Approach 1:

The patent optimizes polymerization parameters including temperature profiles, pressure conditions, and catalyst deactivation rates to produce LDPE with broad MWD up to Mw/Mn ≥ 4.0 while controlling the upper molecular weight limit. This achieves the desired processing performance while minimizing optical degradation.

Inventive Principle:
Principle #35Parameter changes

3Strength

If autoclave based reactor systems are used to produce broad MWD LDPE, then high melt strength is achieved, but production costs increase and ultra high molecular weight fraction is formed

Engineering Contradiction:
Improvemelt strengthVSAvoidproduction costs
Core Design Contradiction:
StrengthVSEase of manufacture

Solution Approach 1:

Instead of using traditional autoclave reactors that produce ultra high molecular weight fractions, the patent inverts the approach by using tubular or loop reactors with controlled residence time and conversion levels. This alternative methodology achieves broad MWD and high melt strength without the associated cost penalties and gel formation problems.

Inventive Principle:
Principle #13The other way round (Inversion)

Solution Approach 2:

The patent changes the reactor operation parameters including maintaining lower conversion levels (10-30%), controlling temperature gradients along the reactor, and adjusting monomer feed rates. These parameter changes enable cost-effective production of broad MWD LDPE without ultra high molecular weight fractions.

Inventive Principle:
Principle #35Parameter changes

4Reliability

If LDPE content in blend is increased to improve melt strength, then bubble stability is enhanced, but film performance contribution from LLDPE is reduced

Engineering Contradiction:
Improvebubble stabilityVSAvoidfilm output
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent changes the molecular weight distribution parameters of the LDPE component to achieve maximum melt strength at lower LDPE concentrations. By controlling Mw/Mn ratio and eliminating ultra high molecular weight fractions, the patent enables effective blends with reduced LDPE content, thereby maintaining bubble stability while preserving LLDPE's film-forming properties and productivity.

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 composition enhances bubble stability, increases film output by up to 15% at maximum output rate, improves mechanical and optical properties, and reduces production costs by allowing higher LDPE content without compromising processing performance, leading to films with superior mechanical and shrink performance.

Implementation Method 1

A composition comprising: a) a first ethylene-based polymer, formed by a high pressure, free-radical polymerization process

Methodology Applied
Scientific EffectFree-radical polymerization:

Data Source

PatentEP2999742B1Compositions containing low density ethylene-based polymers with high melt strength and films formed from the same
Publication Date: 2024.02.14 DOW GLOBAL TECHNOLOGIES LLC
  • EP2999742B1 patent drawingFigure 1
  • EP2999742B1 patent drawingFigure 2
  • EP2999742B1 patent drawingFigure 3

AI summary

The invention provides a composition comprising the following: A) a first ethylene-based polymer, formed by a high pressure, free-radical polymerization process, and comprising the following properties: a) a Mw(abs) versus I2 relationship: Mw(abs) < A x [(I2)B], where A = 5.00 x 102 (kg/mole)/(dg/min)B, and B = -0.40; and b) a MS versus I2 relationship: MS ≥ C x [(I2)D], where C = 13.5 cN/(dg/min)D, and D = -0.55, c) a melt index (I2) from greater than 0.9 to 2.5 g/10 min; and B) a second ethylene-based polymer; and wherein the second ethylene-based polymer has a melt index (I2) from 0.1 to 4.0 g/10 min.