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Science of Industrial Processes – Polymer Morphology and Fibre Reinforcement Mechanisms

Preface

Polymer Morphology means the way polymer chains are arranged in the solid state. The simplest three variable characterisation is:

  • Degree of crystallinity among the chains
  • Proportion of orientation among the chains not in crystals
  • Direction of the orientation

Wood is a natural material with highly oriented chains, which give it its well-known directional properties. Thermoplastic polyester is a familiar textile fibre in which both the non-crystalline and crystalline fractions are deliberately oriented along the thread-line to confer strength which can, if required, exceed that of drawn steel.

Glass fibres play the same role in polymers whose chains are not so easily oriented in preferred directions. In glass reinforced plastics (GRP) the desired orientation is often achieved by weaving glass mats[1], placing them in a mould and spreading a short chain polymer[2] over and into them. The polymer chains are then caused to link up by the action of thermally activated catalyst dissolved among them[3]. In this form the material is no longer “plastic” despite its common name of GRP.

When carbon fibres are used instead of glass, and “epoxy” resins are used instead of polyester[4] resins, you get the standard forms of carbon fibre composites used in racing cars, aircraft, golf clubs and tennis rackets[5].

When glass (or carbon) fibres are used with mainly saturated polymer chains, polypropylene and nylon for instance, they are usually in short lengths by comparison with the principal dimensions of the artefact which is to be fabricated, so that they are not seen on the artefact’s surface and succeed in penetrating into its crevices.

One of the two biggest challenges in manufacturing mouldings and extrusions has been to ensure that the discrete fibres are oriented in the directions of greatest stress when the artefact is put into use. In pipe extrusions, discrete fibres will orient naturally in the direction of extrusion, i.e. along the pipe axis, whereas the greatest stress in a pipe under internal pressure is circumferential, i.e. at right angles to the extrusion direction. Overcoming this problem has been the focus of the SAFIRE© technology. Many of the papers listed in the panel are concerned with the fundamental science of the SAFIRE technology, a key result of which is the touch equation.

TouchFormula

The second of the two biggest challenges is to ensure that the glass or carbon fibres actually contact the host polymers at the molecular level. Ways of ensuring this are also part of the SAFIRE technology, but as discussed in the papers opposite, they are dependent on the chemistry of wetting, developed in the 1980s by BP Chemicals among others.

References

[1] As found in home and car repair kits.

[2] Usually referred to as resin.

[3] Microwaves have proved an effective replacement for normal heating.

[4] These so called “unsaturated” polyesters are quite distinct from the thermoplastic polyesters used to make textile fibres.

[5] Carbon fibre is not as strong as glass fibre for a given cross-section, but it is stiffer than glass, a desirable property in the above applications.

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A Mechanism for Observed Reaction Rate Enhancement in a Microwave Applicator based on the concept of a Non-Equilibrated Temperature Reaction (NETR)

Paper to the 39th International Symposium of the Society for the Advancement of Material and Process Engineering (SAMPE), 11th-14th April 1994.

S F Bush with J M Methven

Abstract

There is much published evidence that certain chemical reactions proceed faster when heated in a microwave applicator than when heated in a conventional oven or press. Recent work in this laboratory on the pultrusion of polyester/glass fibre rods indicates a reaction rate enhancement of about ten times. To account for these observations this paper considers reactions in which one of the reactants has a significantly higher dielectric loss factor than the others.

Two cases are considered. One is the peroxide initiator system relevant to pultrusion and the other a bimolecular reaction relevant to epoxy systems. It is shown that a necessary condition for rate enhancement is that a key reaction step proceeds at least as fast as thermal equilibration by collision, and that this condition is likely to have been fulfilled in the pultrusion case. Under this condition the high loss species (the peroxide in the case of pultrusion) has, in effect a non-equilibrated temperature (NET significantly above (ΔT) that of the bulk of the material (T). For the bimolecular reaction the analysis shows that the rate of a non equilibrated temperature reaction (NETR) would be enhanced by up to 20 times for a reaction with ΔT of some tens of degrees, a bulk temperature T of 400K and activation energy of 150kJ/mol.

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