Overview
ABSTRACT
Calendering is mainly applied to PVC for manufacturing sheets or films. After describing the basics of the process, PVC formulations are presented as well as the different stages of their gelation and the calendering process itself. The different devices controlling the thickness and its uniformity are described. Models of increasing complexity predict calendering forces, polymer heating and sheet thickness as a function of the rheology of the material and the processing parameters. These models make it possible to understand the occurrence of defects and to optimize operating conditions to avoid them. The specific case of post extrusion calendering is finally presented.
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Read the articleAUTHORS
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Jean-François AGASSANT: Civil engineer from the École des Mines. Doctor of Science - Professor Emeritus at the École Nationale Supérieure des Mines de Paris, Paris, France
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Robert HINAULT: Engineer, ENSCR (National School of Chemistry of Rennes) - Former Technical Director of Taraflex, Tarare, France
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Isabelle VIAL: Engineer, Doctorate from INSA Lyon - Director of Materials R&D at Gerflor, Tarare, France
INTRODUCTION
Calendering is a process for manufacturing polymer sheets (> 100 µm) or films (< 100 µm) by crushing the molten plastic mass between several heated, mechanically driven cylinders. This technology is very old; a US patent (No. 16) from 1836 claims the calendering of rubber. Calendering developed in conjunction with PVC (polyvinyl chloride) from the 1940s onwards. Even today, PVC remains the polymer most commonly processed by calendering, although other polymers can also be calendered: elastomers, elastomer alloys (e.g., Santoprene, Alcryn), thermoplastic polyurethane, chlorinated polyethylene, chlorosulfonated polyethylene (e.g., Hypalon), and certain polyolefin polymers (low-density polyethylene (LDPE), ethylene-propylene copolymers, ethylene vinyl acetate (EVA), polypropylene (PP), etc.).
Compared to extrusion blow molding and flat die extrusion processes, which also produce thermoplastic films and sheets, calendering differs in the following ways:
a much higher level of investment, typically by a factor of 20;
Very high throughput rates: from 2 t/h to 6 t/h depending on whether rigid PVC or filled plasticized PVC is being processed. These figures are 3 to 4 times higher than those obtained by flat die extrusion and 2 to 3 times higher than by extrusion blow molding.
large widths: 5,000 mm without stretching for sheets, or with stretching for films. These widths are comparable to those obtained by extrusion blow molding;
very good quality films and sheets, i.e., flatness, profile, surface finish, dimensional stability;
a narrower range of thicknesses (50 µm for rigid PVC to 1.3 mm for filled plasticized PVC) than in extrusion (10 µm in extrusion blow molding or flat die extrusion plus stretching to 2 mm for flat die extrusion).
It can therefore be said that calendering and extrusion complement each other: calendering is well suited to large-scale production runs where both quality and throughput are required; extrusion, which can be easily scaled to the size of the production run, is particularly sought after for its versatility (virtually all thermoplastic polymers can be extruded).
Annual PVC consumption in Western Europe is approximately 4.3 million tons (according to IHS Markit 2022). Calendering accounts for approximately 17% of all PVC conversion processes, with the main markets for calendered products being floor and roof coverings, conveyor belts, films for leather goods, automotive, packaging, textile coatings, etc.
In this article, we will focus primarily on PVC calendering. We will show how the process can...
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KEYWORDS
PVC | calander | gelation | post extrusion calendering | process modeling
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