Process of Forming Nano-Composites and Nano-Porous Non-Wovens

a technology of nano-porous non-wovens and composite materials, which is applied in the field of nano-composites and nano-porous non-wovens, can solve the problems of limited mechanical properties

Inactive Publication Date: 2012-03-29
MILLIKEN & CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology allows two different types of plastics together into one composite material with very small fibers called microfibrils or fused silica (SiO2) particles dispersed throughout it. These tiny fiber bundles can be used alone without being mixed up again when needed. By doing this we create stronger materials made from these mixtures compared to traditional methods like adding fillings or reinforcing agents during manufacturing processes.

Problems solved by technology

This patented technology describes how adding nanofibrils can improve various technical characteristics like reducing weights while maintaining good air permeabilities. These fibers also enhance certain aspects of these products by providing them with specific functions when combined into composite structures.

Method used

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  • Process of Forming Nano-Composites and Nano-Porous Non-Wovens
  • Process of Forming Nano-Composites and Nano-Porous Non-Wovens
  • Process of Forming Nano-Composites and Nano-Porous Non-Wovens

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0086]The first polymer was Homopolymer Polypropylene (HPP), obtained in granule form from Lyondell Basell as Pro-fax 6301 and had a melt flow of 12 g / 10 min (230° C., ASTMD 1238). The granule HPP was pelletized using a twin screw extruder Prism TSE 16TC. The second polymer was Cyrtal Polystyrene (PS), obtained in pellet form from Total Petrochemicals as PS 500 and had a melt flow of 14 g / 10 min (200° C., ASTMD 1238). The PS and HPP pellets were premixed in a mixer at a weight ratio of 80 / 20. The mixture was fed into a co-rotating 16 mm twin-screw extruder, Prism TSE 16TC. The feed rate was 150 g min−1 and the screw speed was 92 rpm. Barrel temperature profiles were 225, 255, 245, 240, and 235° C. The blend was extruded through a rod die where the extrudate was subject to an extensional force that was sufficient to generate nanofibrillar structure. The extrudate was cooled in a water bath at the die exit and collected after passing through a pelletizer. The pellets were the first

example 2

[0090]Example 2 was carried out with the same materials and process of Example 1, except that the consolidation temperature was 340° F. This consolidation temperature was 20° F. higher the melting point of HPP.

[0091]The morphology of the etched nano-composite article was observed using a SEM (FIG. 11A—1000× and FIG. 11B—10000×) represent the top view of the etched films. The nanofibers melted and fused into sheet like structure during consolidation and the nanofibers were destroyed. This consolidation temperature (at the given pressure and long resonance time) was proven to be too high to produce a nano-porous structure.

example 3

[0092]Example 3 was carried out with the same materials and process of Example 1, except that the consolidation temperature was 280° F. This consolidation temperature was 40° F. lower the melting point of HPP.

[0093]The morphology of the etched nano-composite article was observed using a SEM (FIG. 12A—1000×, FIG. 12B—10000×) represent the top view of the etched films. The nanofibers in the film were loosely connected and the film was very fragile to handle during testing indicating that less than 70% of the nanofibers were bonded to other nanofibers. This combination of consolidation temperature, pressure and resonance time was proven to be too low to produce nano-porous non-woven with good physical strength.

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Abstract

A process for forming a nano-composite including mixing a first and second thermoplastic polymer in a molten state forming a molten polymer blend. The second polymer is soluble in a first solvent and the first polymer is insoluble in the first solvent. The first polymer forms discontinuous regions in the second polymer. Next, the polymer blend is subjected to extensional flow, shear stress, and heat forming nanofibers where less than about 30% by volume of the nanofibers are bonded to other nanofibers.
Next the polymer blend with nanofibers is cooled and the first intermediate is formed into a pre-consolidation formation. The pre-consolidation formation is then consolidated causing nanofiber movement, randomization, and at least 70% by volume of the nanofibers to fuse to other nanofibers. According to one aspect, the second intermediate is then subjected to the first solvent to the dissolving away at least a portion of the second polymer.

Description

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Claims

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Application Information

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Owner MILLIKEN & CO
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