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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Maoult, Yannick Le
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Topics
Publications (37/37 displayed)
- 2022Numerical Simulation of Recycled PET Preforms Infrared Heating Including Force Convection Effect in the Industrial ISBM Ovens
- 2022Infrared heating modeling of recycled PET preforms in injection stretch blow molding processcitations
- 2021Effect of oxidation on spectral and integrated emissivity of Ti-6Al-4V alloy at high temperaturescitations
- 2018On the thermal sensitivity and resolution of a YSZ:Er 3+ /YSZ:Eu 3+ fluorescent thermal history sensorcitations
- 2018The role of microcrystalline structure on optical scattering characteristics of semi-crystalline thermoplastics and the accuracy of numerical input for IR-heating modelingcitations
- 2017A non-invasive experimental approach for surface temperature measurements on semi-crystalline thermoplasticscitations
- 2017Industrial applications of the superplastic forming by using Infra-Red heatercitations
- 2017Novel erbia-yttria co-doped zirconia fluorescent thermal history sensorcitations
- 2016Experimental analysis on the coupled effect between thermo-optical properties and microstructure of semi-crystalline thermoplasticscitations
- 2016Infrared welding process on composite: Effect of interdiffusion at the welding interfacecitations
- 2016Infrared radiation applied to polymer processescitations
- 2016Titanium Superplastic Forming by Aurock: A Complete Integrated Solution from CAD File to Final Part
- 2016Identification of the temperature dependent relation between thermo-optical properties and morphology of semi-crystalline thermoplastics for thermoforming process
- 2016Effect of the developed temperature field on the molecular interdiffusion at the interface in infrared welding of polycarbonate compositescitations
- 2016Infrared Radiation applied to Blow Molding and thermoforming
- 2014Optimized sol–gel thermal barrier coatings for long-term cyclic oxidation lifecitations
- 2014Feasibility of luminescent multilayer sol-gel thermal barrier coating manufacturing for future applications in through-thickness temperature gradient sensingcitations
- 2013Innovative Superplastic Forming Based on In-Situ Infra-Red Sheet Heatingcitations
- 2012Superplastic forming of AZ31 magnesium alloy with controlled microstructurecitations
- 2011Infrared heating stage simulation of semi-transparent media (PET) using ray tracing methodcitations
- 2011Simulations of an Infrared Composite Curing Processcitations
- 2011Infrared curing simulations of liquid composites moldingcitations
- 2010Oxidation and spallation of FeCrAl alloys and thermal barrier coatings: in situ investigation under controlled temperature gradientcitations
- 2010Evolution de la microstructure et influence de la pollution atmosphérique lors de la mise en oeuvre d'une résine thermodurcissable
- 2010Advances in the field of new smart thermal barrier coatings
- 2008Direct obervations and analysis of the spallation of alumina scales grown on PM2000 alloycitations
- 2008TOWARDS SUPERPLASTIC FORMING OF AZ31 MAGNESIUM ALLOY WITH CONTROLLED MICROSTRUCTURE
- 2007Measurement of thermal contact resistance between the mold and the polymer for the stretch-blow molding processcitations
- 2004Experimental and numerical infrared heating of thermoplastic sheet during thermoforming process
- 20043D finite element modeling of the blow molding process
- 2003Heat conditioning modelling of thermoforming process: comparison with experiments
- 2003Modelling of infrared heating of thermoplastic sheet used in thermoforming processcitations
- 2002Infrared Heating Modeling of Thermoplastic Sheets in Thermoforming Process
- 2001Comparison between a numerical model and an experimental approach of preform infrared radiative heating-recent results
- 2001Recent Issues In Preform Radiative Heating Modelling
- 2001Comparison Between a Numerical Model and an Experimental Approach of Preform Infrared Radiative Heating – Recent Results
- 2000Analysis of influent parameters during infrared radiative heating of PET preform
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document
Analysis of influent parameters during infrared radiative heating of PET preform
Abstract
The processing parameters during radiative heating of PET preform are: The number of infrared heaters N h ,The temperature T i of each infrared heater L i=1, N hThe heating time t h ,The cooling time t c ,The coordinate vector x i=1,N h of each infrared heater L i=1, N h , The heat transfer coefficient h c between cooling air and PET preform. In previous papers [1,2], the spectral emissivity and directivity of different halogen lamps (Philips 300-700W electric nominal power made of a coiled tungsten filament, contained in a quartz tubular enclosure and a diffuse reflector made of a ceramic coating) have been reported. Recent measurements using a 0.6-25 m thermopile sensor on similar halogen lamps of 1000W (used in an industrial oven of injection-blow moulding machine) have been processed. The maximum temperature of the tungsten filament is 2400 K. As shown in fig. 1, these infrared heaters exhibit a slightly different behaviour from a lambertian source (diffuse radiation) due to the reflector. The average discrepancy is about 8 %. In order to take into account the participation of the diffuse reflector in the amount of the incident radiation, a coefficient of efficacy k rf is introduced. Fig. 2 shows the experimental setup that has been developed in order to measure the surface temperature distribution (front face and back face), when a PET sheet is heating using previous infrared heaters. An 880 LW AGEMA infrared camera (8-12 m bandwidth) is used to measure the spatial and transient temperature distribution. The surface dimension of the PET sheet is 20cm 20cm cm and the thickness is 1.5 mm. A 3D control-volume model has been developed for computing radiative heat transfer during the infrared heating stage. The sheet-shape domain sketched in fig. 3 is discretised into cubic elements, called control-volumes [3]. The energy equation including radiative transfer integrated over each control volume V e x y z and over the time from t to t t leads to: