Abstract:Katedra lńŻyńierji spożywĆzq i Tlvorzylf sziu.znydr d. Radawickr r5/rz 79620 kszalin e.miiL ini.hłlski@lcwfo koszalin Pl Symulacja przemiesz Show more
“…When an extruder operates at a clearance between the discs equal to W s = 3.0 mm, the distance between the points on the trajectories at the maximum point (D M ) can increase 13 times compared to the total length l C (column 3 of Table 1), and at the outlet -D E -it increases about 3 times compared to the total length l C (column 6 of Table 1). This is evidence of the disc's intensive interaction leading to the uncoiling of the polymer chain during its displacement in the disc zone [14].…”
Section: T a B L E 1 Characteristic Parameters Of The Distance Betwee...mentioning
confidence: 95%
“…These fluxes are perpendicular to each other and they create a displacement of the melt's particles in the clearance between the discs along spiral trajectories from the outside diameter towards the outlet (Fig. 3) [14,16].…”
Section: Melt Displacement In the Disc Zonementioning
confidence: 99%
“…The authors have already presented in their papers a model simulating the conditions of polymer chain stretching [14][15][16][17]. Table 1 presents the values of distance between trajectories with respect to the conformative (D M /l K ) and total length (D M /l C ) of the PE polymer chain, and the values of distance between two points of the trajectories on an outlet diameter with respect to the conformative (D E /l K ) and total length (D E /l C ).…”
Section: Simulation Of Polymer Chain Conformation Arranging Condition...mentioning
confidence: 99%
“…If a polymer melt flows in a clearance between the discs, the particles of the melt are subjected to a tension (uncoiling the tangled polymer chain conformation), and then are recoiled in an area of a smaller diame-ter. This second stage -the recoiling of the polymer chains in an extruder clearance between the discs -is revealed as Weissenberg's effect [14].…”
Section: Simulation Of Polymer Chain Conformation Arranging Condition...mentioning
confidence: 99%
“…The authors have implemented an innovative experimental screw-disc extruder (Fig. 1) designed by engineers 845 2014, , 59 nr 11-12 from their department: the diameter of the screw-disc was D = 130 mm and the length of the screw was L = 2D (screw working length L = 260 mm) [12][13][14]. The innovative extruder has a clearance between the movable face of the screw and the conical cover of the extruder.…”
The article presents the results of analysis and research of the disc plasticizing mechanism operation on the mechanical, thermal, and structural properties of extruded material. The analysis of velocity distribution and trajectories of the material's displacement leads to a conclusion that the flow of polymer melt through the clearance between the discs arranges the supermolecular structure and in this way results in an extrudate with improved mechanical properties.
“…When an extruder operates at a clearance between the discs equal to W s = 3.0 mm, the distance between the points on the trajectories at the maximum point (D M ) can increase 13 times compared to the total length l C (column 3 of Table 1), and at the outlet -D E -it increases about 3 times compared to the total length l C (column 6 of Table 1). This is evidence of the disc's intensive interaction leading to the uncoiling of the polymer chain during its displacement in the disc zone [14].…”
Section: T a B L E 1 Characteristic Parameters Of The Distance Betwee...mentioning
confidence: 95%
“…These fluxes are perpendicular to each other and they create a displacement of the melt's particles in the clearance between the discs along spiral trajectories from the outside diameter towards the outlet (Fig. 3) [14,16].…”
Section: Melt Displacement In the Disc Zonementioning
confidence: 99%
“…The authors have already presented in their papers a model simulating the conditions of polymer chain stretching [14][15][16][17]. Table 1 presents the values of distance between trajectories with respect to the conformative (D M /l K ) and total length (D M /l C ) of the PE polymer chain, and the values of distance between two points of the trajectories on an outlet diameter with respect to the conformative (D E /l K ) and total length (D E /l C ).…”
Section: Simulation Of Polymer Chain Conformation Arranging Condition...mentioning
confidence: 99%
“…If a polymer melt flows in a clearance between the discs, the particles of the melt are subjected to a tension (uncoiling the tangled polymer chain conformation), and then are recoiled in an area of a smaller diame-ter. This second stage -the recoiling of the polymer chains in an extruder clearance between the discs -is revealed as Weissenberg's effect [14].…”
Section: Simulation Of Polymer Chain Conformation Arranging Condition...mentioning
confidence: 99%
“…The authors have implemented an innovative experimental screw-disc extruder (Fig. 1) designed by engineers 845 2014, , 59 nr 11-12 from their department: the diameter of the screw-disc was D = 130 mm and the length of the screw was L = 2D (screw working length L = 260 mm) [12][13][14]. The innovative extruder has a clearance between the movable face of the screw and the conical cover of the extruder.…”
The article presents the results of analysis and research of the disc plasticizing mechanism operation on the mechanical, thermal, and structural properties of extruded material. The analysis of velocity distribution and trajectories of the material's displacement leads to a conclusion that the flow of polymer melt through the clearance between the discs arranges the supermolecular structure and in this way results in an extrudate with improved mechanical properties.
Experimental effect of a screw disc clearance size on the homogenisation level and the mechanical properties of extrudate obtained using the mixture of original low density polyethylene (LDPE) and commercial LDPE recyclate were discussed in the present paper. For the purpose of experiments a screw disc extruder was applied. Some tensile tests results and photographs of the extrudate cross-sections obtained at different clearance settings were presented. The results show that the mixing in the conical screw disc zone was carried out more thoroughly than in a helical channel of a single screw extruder. Plasticising in the disc zone of a screw disc extruder makes it possible to obtain extrudate with better properties than in the case of classical extrusion.
The paper presents the summary of research on polymer melt particle motion trajectories in a disc zone of a screw-disk extruder. We analysed two models of its structure, different in levels of taken simplifications. The analysis includes computer simulations of material particle flow and results of experimental tests to determine the properties of the resultant extrudate. Analysis of the results shows that the motion of melt in the disk zone of a screw-disk extruder is a superposition of pressure and dragged streams. The observed trajectories of polymer particles and relations of mechanical properties and elongation of the molecular chain proved the presence of a stretching effect on polymer molecular chains.
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