2013
DOI: 10.4028/www.scientific.net/amm.315.861
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Mechanical Behavior of Polyurethane Composite Foams from Kenaf Fiber and Recycled Tire Rubber Particles

Abstract: In the present work polyurethane foams containing various content loadings of kenaf fiber and recycled tire rubber particulates were prepared and studied, with the objective of developing alternative composite rigid foams. The influence of the filler content on the foam microstructure and its physical and mechanical behavior has been studied for three different polyurethane resin densities. Microstructural observation on fracture surface of composites was carried out using scanning electron microscopy. It has … Show more

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Cited by 10 publications
(9 citation statements)
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“…The density of kenaf is 1.62 g/cm³, which is higher than EFB (1.52 g/cm³) (Anuar et al 2018). Subramaniyan et al (2013) reported that the density of the filler affects the density of the foam. The foam filled with kenaf had a higher density than the one filled with EFB.…”
Section: Foam Densitymentioning
confidence: 82%
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“…The density of kenaf is 1.62 g/cm³, which is higher than EFB (1.52 g/cm³) (Anuar et al 2018). Subramaniyan et al (2013) reported that the density of the filler affects the density of the foam. The foam filled with kenaf had a higher density than the one filled with EFB.…”
Section: Foam Densitymentioning
confidence: 82%
“…The stem and bark of the kenaf have distinct qualities and can be used in various products, for example, car accessories, animal feed, biofuels, and paper-based products (Ismai et al 2011). Kenaf has been established in Malaysia as a new industrial crop with high potential for product development (Subramaniyan et al 2013).…”
Section: Introductionmentioning
confidence: 99%
“…As shown in Figure 2(a), the rHDPE pellets were introduced through the main feeder (zone 1), while the RR particles (35,50,65, and 80 wt.%) were introduced via a side-stuffer located in zone 4 of the extruder to limit thermal degradation. Then, different concentrations of RR particles (15,30,45, and 60 wt.%) were dry-blended with RTF (20 wt.%) after being oven-dried at 70°C for 12 h. Again, the rHDPE was fed to the extruder in the first zone (main feed), while the RR/RTF mixtures were fed via the side feeder (zone 4). The processing temperature was fixed at 175°C with a screw speed of 120 r/min and a flow rate of 4 kg/h.…”
Section: Processingmentioning
confidence: 99%
“…Again, the materials were cooled in a water bath and pelletized. Then, these pellets (RR/MAPE masterbatch) were introduced in the main feeder at different concentrations (15,30,45, and 60 wt.%) along with rHDPE (65, 50, 35, and 20 wt.%) in a second extrusion step, while the RTF (20 wt.%) was introduced via the side-stuffer located at zone 4. All the formulations with codes are presented in Table 2.…”
Section: Processingmentioning
confidence: 99%
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