Elsevier

Polymer

Volume 45, Issue 18, 19 August 2004, Pages 6123-6131
Polymer

Polymer crosslinking controlled by release of catalyst encapsulated in polycarbonate micro-spheres

https://doi.org/10.1016/j.polymer.2004.06.064Get rights and content

Abstract

EVA crosslinking by ester–silane exchange reaction, controlled by catalyst released from polycarbonate micro-particles, was studied from rheological experiments. Firstly, dibutyltin dilaurate in polycarbonate (PC) (DBTDL) catalyst was encapsulated in polycarbonate micro-particles by an emulsion process. These PC micro-particles have a trimodal size distribution with a mean diameter around 25 μm. Furthermore, scanning electronic microscopy analysis revealed that the DBTDL catalyst is homogeneously dispersed in PC micro-particles. This was verified by DSC experiments which showed a Tg equal to 72 °C for the DBTL micro-particles. Secondly, the deformation and break-up studies of PC micro-particles in molten EVA matrix showed that PC micro-particles can only break up in EVA matrix of high molecular weight (EVA28-03) and for temperatures higher than 200 °C. Thirdly, rheological experiments showed that the crosslink reaction is controlled by the diffusion rate of DBTDL from PC micro-particles. However, this diffusion rate was observed to be independent on either the temperature or the PC micro-particles size.

Introduction

A polymer, in its amorphous state, undergoing a chemical crosslinking process, is converted from a viscoelastic liquid into a viscoelastic solid. Properties changes are more dramatic near the liquid–gel transition [1]. Generally, chemical modifications in reactive polymer processing may cause important changes in the rheological behavior and as a consequence in the flowing of the polymers. For example mixing and shaping operations require sufficient molecular mobility, which vanishes when the chain motions slow down near the gel point. Consequently, the mixing (and shaping) and the reactive step must be separated by using formulations temporally dormant. This is mainly the case of the crosslinking reactions when they are used on a tailoring line of crosslinked materials.

On the other hand, a new interchange reaction ester-alkoxysilane in presence of dibutyltin oxide (DBTO) as catalyst and its application to ethylene-co-vinylacetate (EVA) crosslinking was previously reported [2]. This reaction takes place in the range of temperatures 100–250 °C only in presence of DBTO as efficient catalyst. However, this reaction must be well controlled (kinetics, side reactions) in order to separate the mixing and reactive processes. This is particularly true in a twin-screw extruder process. Indeed, the melt temperature may greatly overtake the check temperature due to the viscous dissipation phenomenon. As the ester exchange reaction does not take place without any catalyst, one way to control the reaction of crosslinking is to encapsulate the catalyst in polymer micro-spheres as controlled release system.

This paper is devoted to the study of EVA crosslinking by ester–silane exchange reaction controlled by catalyst release from PC micro-spheres. It is divided into the following parts: In the first part, we will describe the preparation and characterisation of PC micro-spheres containing dibutyltin dilaurate (DBTDL). DBTDL was chosen instead of DBTO as catalyst for the exchange reaction because DBTO is a powder and DBTDL is a liquid at room temperature. Consequently DBTDL is more suitable for its encapsulation by an emulsion process. Following this, we will study the deformation of molten PC micro-spheres embedded in molten EVA matrix in order to understand the mechanism of catalyst release at high temperature (T≥180 °C). In the last part, we will study from rheological experiments EVA crosslinking by the exchange ester–silane reaction catalysed by free or released DBTDL from PC micro-spheres.

Section snippets

Preparation

Methylene chloride (+99%), dibutyltin dilaurate (98%) and polyvinylalcohol, 88% hydrolysed, Mw=22,000 g/mol were supplied by Aldrich (+99%). Polycarbonate (PC) is supplied by Bayer (Makrolon 2658) in pellet form. PC is an amorphous polymer with a Tg equal to 145 °C.

Micro-particles are prepared in a Sovirel reactor of 500 mL equipped with an impeller stirrer. 1.7 g of dibutyltin dilaurate and 3.2 g of polycarbonate were dissolved in 80 mL of methylene chloride. The solution was then rapidly poured in

Optical shear device

Melt blends of EVA and PC micro-particles (PC in very diluted conditions) were observed, in quiescent state or during shear, using a Leitz Orthoplan microscope (transmission) with 20× lens coupled with a Linkam CSS-450 high temperature stage. The sample was held in the gap between the two quartz windows and was sheared by rotating the bottom plate by a precision stepping motor, while the top plate remained stationary. The sample consists in a sandwich of two EVA films between which PC

Materials and method

EVA copolymers, tetraalkoxysilane (TPOS) and DBTDL or PC micro-spheres were mixed in the melt with a Haake plasticorder equipped with an internal mixer (Rheomix 600). The concentration in alkoxide groups in EVA was expressed by the VA/OR molar ratio corresponding to the vinyl acetate (VA) units over alkoxide groups (OR) from TPOS. For the present study, we used VA/OR=2. One concentration in DBTDL catalyst was used (1 wt% of DBTDL relatively to EVA/TPOS reactants). For catalyst release system,

Conclusion

The exchange reaction between ester and alkoxy silane catalysed by DBTDL was investigated in order to crosslink EVA copolymers. The scope of this paper was to control the crosslinking kinetics by controlled release of the catalyst from PC micro-spheres. The main conclusions of the present paper are the following:

DBTDL catalyst was encapsulated in polycarbonate micro-particles by an emulsion process. The amount of encapsulated catalyst in the micro-particles was determined to be around 27 wt%.

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