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Journal articles on the topic 'Elongational flow'

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Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

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1

Kugler, Susanne Katrin, Argha Protim Dey, Sandra Saad, Camilo Cruz, Armin Kech, and Tim Osswald. "A Flow-Dependent Fiber Orientation Model." Journal of Composites Science 4, no. 3 (July 22, 2020): 96. http://dx.doi.org/10.3390/jcs4030096.

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The mechanical performance of fiber reinforced polymers is dependent on the process-induced fiber orientation. In this work, we focus on the prediction of the fiber orientation in an injection-molded short fiber reinforced thermoplastic part using an original multi-scale modeling approach. A particle-based model developed for shear flows is extended to elongational flows. This mechanistic model for elongational flows is validated using an experiment, which was conducted for a long fiber reinforced polymer. The influence of several fiber descriptors and fluid viscosity on fiber orientation under elongational flow is studied at the micro-scale. Based on this sensitivity analysis, a common parameter set for a continuum-based fiber orientation macroscopic model is defined under elongational flow. We then develop a novel flow-dependent macroscopic fiber orientation, which takes into consideration the effect of both elongational and shear flow on the fiber orientation evolution during the filling of a mold cavity. The model is objective and shows better performance in comparison to state-of-the-art fiber orientation models when compared to μCT-based fiber orientation measurements for several industrial parts. The model is implemented using the simulation software Autodesk Moldflow Insight Scandium® 2019.

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2

KOYAMA, Kiyohito, and Osamu ISHIZUKA. "Elongational Flow of Polymer Melt." Nihon Reoroji Gakkaishi(Journal of the Society of Rheology, Japan) 13, no. 3 (1985): 93–100. http://dx.doi.org/10.1678/rheology1973.13.3_93.

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3

Evans, J. R. G., and J. Greener. "Elongational flow processing of ceramics." Journal of Materials Processing Technology 96, no. 1-3 (November 1999): 143–50. http://dx.doi.org/10.1016/s0924-0136(99)00325-8.

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4

Kim, Hwan Chul, Ajit Pendse, and John R. Collier. "Polymer melt lubricated elongational flow." Journal of Rheology 38, no. 4 (July 1994): 831–45. http://dx.doi.org/10.1122/1.550595.

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5

Rabin, Y. "Polymer conformation in elongational flow." Journal of Chemical Physics 88, no. 6 (March 15, 1988): 4014–17. http://dx.doi.org/10.1063/1.453853.

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6

Kaye, A. "Convected coordinates and elongational flow." Journal of Non-Newtonian Fluid Mechanics 40, no. 1 (July 1991): 55–77. http://dx.doi.org/10.1016/0377-0257(91)87026-t.

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7

Varchanis, Stylianos, Simon J. Haward, Cameron C. Hopkins, Alexandros Syrakos, Amy Q. Shen, Yannis Dimakopoulos, and John Tsamopoulos. "Transition between solid and liquid state of yield-stress fluids under purely extensional deformations." Proceedings of the National Academy of Sciences 117, no. 23 (May 20, 2020): 12611–17. http://dx.doi.org/10.1073/pnas.1922242117.

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We report experimental microfluidic measurements and theoretical modeling of elastoviscoplastic materials under steady, planar elongation. Employing a theory that allows the solid state to deform, we predict the yielding and flow dynamics of such complex materials in pure extensional flows. We find a significant deviation of the ratio of the elongational to the shear yield stress from the standard value predicted by ideal viscoplastic theory, which is attributed to the normal stresses that develop in the solid state prior to yielding. Our results show that the yield strain of the material governs the transition dynamics from the solid state to the liquid state. Finally, given the difficulties of quantifying the stress field in such materials under elongational flow conditions, we identify a simple scaling law that enables the determination of the elongational yield stress from experimentally measured velocity fields.

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8

Rabin, Yitzhak, Frank S. Henyey, and Dennis B. Creamer. "Flow modification by polymers in strong elongational flows." Journal of Chemical Physics 85, no. 8 (October 15, 1986): 4696–701. http://dx.doi.org/10.1063/1.451744.

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9

Todd, B. D., and Peter J. Daivis. "Elongational viscosities from nonequilibrium molecular dynamics simulations of oscillatory elongational flow." Journal of Chemical Physics 107, no. 5 (August 1997): 1617–24. http://dx.doi.org/10.1063/1.474512.

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10

Münstedt, Helmut. "Recoverable Extensional Flow of Polymer Melts and Its Relevance for Processing." Polymers 12, no. 7 (July 8, 2020): 1512. http://dx.doi.org/10.3390/polym12071512.

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While the uniaxial elongational viscosity is widely investigated, and its relevance for processing is described in the literature, much less has been published on the recoverable extensional flow of polymer melts. This paper presents a short overview of the dependencies of the recoverable elongation on the molecular structure of a polymer, and on some experimental parameters. Its main focus lies on the discussion of processing operations and applications that are largely affected by the elastic components of elongational flow. The recoverable portions of stretched films are considered, and the exploitation of the shrinkage of films, due to the recovery of frozen recoverable deformations, and its role for applications are addressed. The analysis of measurements of velocity fields in the entry region of a slit die and results on the determination of the recoverable elongation from uniaxial experiments, according to the literature, lead to the conclusion of dominant elastic extensions. Considering these facts, the assumptions for Cogswell’s widely used method of determining elongational viscosities under processing conditions from entrance flow are not realistic. As examples of a direct application of extrudate swell from short dies for processing, pelletizing and fused deposition modelling within additive manufacturing are addressed. The special features of extrudate swell from short dies, and uniaxial recoverable elongation for a polymer filled with rigid particles in comparison to an immiscible polymer blend, are presented and discussed.

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11

Hunkeler, D., T. Q. Nguyen, and H. H. Kausch. "Polymer solutions under elongational flow: 1. Birefringence characterization of transient and stagnation point elongational flows." Polymer 37, no. 19 (1996): 4257–69. http://dx.doi.org/10.1016/0032-3861(96)00290-x.

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12

Swartjes, F. H. M., G. W. M. Peters, S. Rastogi, and H. E. H. Meijer. "Stress Induced Crystallization in Elongational Flow." International Polymer Processing 18, no. 1 (March 2003): 53–66. http://dx.doi.org/10.3139/217.1719.

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13

Gompper, G., and D. M. Kroll. "Floppy fluid vesicles in elongational flow." Physical Review Letters 71, no. 7 (August 16, 1993): 1111–14. http://dx.doi.org/10.1103/physrevlett.71.1111.

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14

Darinskii, A. A., and O. V. Borisov. "Polyelectrolyte Molecule in an Elongational Flow." Europhysics Letters (EPL) 29, no. 5 (February 10, 1995): 365–70. http://dx.doi.org/10.1209/0295-5075/29/5/003.

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15

Neumann, Richard M. "Polymer stretching in an elongational flow." Journal of Chemical Physics 110, no. 15 (April 15, 1999): 7513–15. http://dx.doi.org/10.1063/1.478653.

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16

Kolitawong, Chanyut. "Rheology properties of elongational flow experiments." Journal of Applied Science 18, no. 2 (December 3, 2019): 116–40. http://dx.doi.org/10.14416/j.appsci.2019.09.002.

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17

Turner, D. M., and M. J. Bennett. "Shear and elongational flow in rubber." Journal of Applied Polymer Science 50 (1992): 65–77. http://dx.doi.org/10.1002/app.1992.070500007.

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18

Raphaelides, Stylianos N., and Anastasia Gioldasi. "Elongational flow studies of set yogurt." Journal of Food Engineering 70, no. 4 (October 2005): 538–45. http://dx.doi.org/10.1016/j.jfoodeng.2004.10.008.

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19

Lee, Won Ki, Hyotaek Lim, and Eun Young Kim. "Nanostructured Change of SIS (Styrene-Isoprene-Styrene) Triblock Copolymer by Elongational Flow." Journal of Nanoscience and Nanotechnology 8, no. 9 (September 1, 2008): 4771–74. http://dx.doi.org/10.1166/jnn.2008.ic12.

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Elongation deformation was conducted on a polystyrene-block-polyisoprene-block-polystyrene (SIS) triblock copolymer which contains cylindrical microdomains composed of polystyrene block chains in matrix of polyisoprene block chains. The extensional flow behavior of this deformation triblock copolymer melt, which exhibits a cylindrical phase, has been examined by using elongational deformation with εo between 0.1 and 1.0 s−1 at different temperatures. The structures related to various condition of elongational flow deformation has been determined from SAXS patterns by considering separately changes in the single particle scattering, which influence the scattering patterns. The TEM and SAXS data of the samples show that the cylindrical PS-domain was deformed along the direction of elongation. It also shows that the cylindrical microdomains are micronecked and deformed with various strain rates.

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20

Foster, Kylie M., Dimitrios V. Papavassiliou, and Edgar A. O’Rear. "Elongational Stresses and Cells." Cells 10, no. 9 (September 8, 2021): 2352. http://dx.doi.org/10.3390/cells10092352.

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Fluid forces and their effects on cells have been researched for quite some time, especially in the realm of biology and medicine. Shear forces have been the primary emphasis, often attributed as being the main source of cell deformation/damage in devices like prosthetic heart valves and artificial organs. Less well understood and studied are extensional stresses which are often found in such devices, in bioreactors, and in normal blood circulation. Several microfluidic channels utilizing hyperbolic, abrupt, or tapered constrictions and cross-flow geometries, have been used to isolate the effects of extensional flow. Under such flow cell deformations, erythrocytes, leukocytes, and a variety of other cell types have been examined. Results suggest that extensional stresses cause larger deformation than shear stresses of the same magnitude. This has further implications in assessing cell injury from mechanical forces in artificial organs and bioreactors. The cells’ greater sensitivity to extensional stress has found utility in mechanophenotyping devices, which have been successfully used to identify pathologies that affect cell deformability. Further application outside of biology includes disrupting cells for increased food product stability and harvesting macromolecules for biofuel. The effects of extensional stresses on cells remains an area meriting further study.

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21

Maiti, P., M. Okamoto, and T. Kotaka. "Elongational flow birefringence of ethylene–tetracyclododecene copolymer." Polymer 42, no. 8 (April 2001): 3939–42. http://dx.doi.org/10.1016/s0032-3861(00)00796-5.

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22

Rauwendaal, Chris. "New dispersive mixers based on elongational flow." Plastics, Additives and Compounding 1, no. 4 (August 1999): 21–23. http://dx.doi.org/10.1016/s1464-391x(99)80106-8.

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23

Li, L., T. Masuda, and M. Takahashi. "Elongational flow behavior of ABS polymer melts." Journal of Rheology 34, no. 1 (January 1990): 103–16. http://dx.doi.org/10.1122/1.550112.

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24

Perkins, T. T. "Single Polymer Dynamics in an Elongational Flow." Science 276, no. 5321 (June 27, 1997): 2016–21. http://dx.doi.org/10.1126/science.276.5321.2016.

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25

Hagen, Thomas, and Michael Renardy. "Eigenvalue Asymptotics in Non-isothermal Elongational Flow." Journal of Mathematical Analysis and Applications 252, no. 1 (December 2000): 431–43. http://dx.doi.org/10.1006/jmaa.2000.7089.

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26

Besio, G. J., R. K. Prud'homme, and J. B. Benziger. "Effect of elongational flow on polymer adsorption." Macromolecules 21, no. 4 (July 1988): 1070–74. http://dx.doi.org/10.1021/ma00182a038.

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27

Prud'homme, Robert K., and Gregory G. Warr. "Elongational Flow of Solutions of Rodlike Micelles." Langmuir 10, no. 10 (October 1994): 3419–26. http://dx.doi.org/10.1021/la00022a010.

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28

Bayer, R. K., F. J. Balt� Calleja, E. L�pez Cabarcos, H. G. Zachiviann, A. Paulsen, F. Br�ning, and W. Meins. "Properties of elongational flow injection moulded polyethylene." Journal of Materials Science 24, no. 7 (July 1989): 2643–52. http://dx.doi.org/10.1007/bf01174539.

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29

Farinato, R. S. "Elongational flow birefringence of poly(styrene sulphonate)." Polymer 29, no. 1 (January 1988): 160–67. http://dx.doi.org/10.1016/0032-3861(88)90216-9.

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30

Kotaka, Tadao, Akira Kojima, and Masami Okamoto. "Elongational flow opto-rheometry for polymer melts." Rheologica Acta 36, no. 6 (1997): 646–56. http://dx.doi.org/10.1007/bf00367361.

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31

Darinskii, A. A., and M. G. Saphiannikova. "Kinetics of polymer chains in elongational flow." Journal of Non-Crystalline Solids 172-174 (September 1994): 932–34. http://dx.doi.org/10.1016/0022-3093(94)90601-7.

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32

Hayakawa, Ichiro, Chiaki Hayashi, Naoki Sasaki, and Kunio Hikichi. "Elongational flow studies of hinged rodlike molecules." Journal of Applied Polymer Science 61, no. 10 (September 6, 1996): 1731–35. http://dx.doi.org/10.1002/(sici)1097-4628(19960906)61:10<1731::aid-app13>3.0.co;2-5.

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33

Zhou, Hong, Lynda Wilson, and Hongyun Wang. "On the Equilibria of the Extended Nematic Polymers under Elongational Flow." Abstract and Applied Analysis 2007 (2007): 1–15. http://dx.doi.org/10.1155/2007/36267.

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We classify the equilibrium solutions of the Smoluchowski equation for dipolar (extended) rigid nematic polymers under imposed elongational flow. The Smoluchowski equation couples the Maier-Saupe short-range interaction, dipole-dipole interaction, and an external elongational flow. We show that all stable equilibria of rigid, dipolar rod dispersions under imposed uniaxial elongational flow field are axisymmetric. This finding of axisymmetry significantly simplifies any procedure of obtaining experimentally observable equilibria.

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34

Chow, A., A. Keller, A. J. Mueller, and J. A. Odell. "Entanglements in polymer solutions under elongational flow: a combined study of chain stretching, flow velocimetry and elongational viscosity." Macromolecules 21, no. 1 (January 1988): 250–56. http://dx.doi.org/10.1021/ma00179a048.

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35

Phan-Thien, N., and B. Caswell. "A nearly-elongational flow analysis of the fibre spinning flow." Journal of Non-Newtonian Fluid Mechanics 21, no. 2 (January 1986): 225–34. http://dx.doi.org/10.1016/0377-0257(86)80037-4.

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36

Hariadi, Rizal F., Erik Winfree, and Bernard Yurke. "Determining hydrodynamic forces in bursting bubbles using DNA nanotube mechanics." Proceedings of the National Academy of Sciences 112, no. 45 (October 26, 2015): E6086—E6095. http://dx.doi.org/10.1073/pnas.1424673112.

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Quantifying the mechanical forces produced by fluid flows within the ocean is critical to understanding the ocean’s environmental phenomena. Such forces may have been instrumental in the origin of life by driving a primitive form of self-replication through fragmentation. Among the intense sources of hydrodynamic shear encountered in the ocean are breaking waves and the bursting bubbles produced by such waves. On a microscopic scale, one expects the surface-tension–driven flows produced during bubble rupture to exhibit particularly high velocity gradients due to the small size scales and masses involved. However, little work has examined the strength of shear flow rates in commonly encountered ocean conditions. By using DNA nanotubes as a novel fluid flow sensor, we investigate the elongational rates generated in bursting films within aqueous bubble foams using both laboratory buffer and ocean water. To characterize the elongational rate distribution associated with a bursting bubble, we introduce the concept of a fragmentation volume and measure its form as a function of elongational flow rate. We find that substantial volumes experience surprisingly large flow rates: during the bursting of a bubble having an air volume of 10 mm3, elongational rates at least as large as ϵ˙=1.0×108 s−1 are generated in a fragmentation volume of ∼2×10−6μL. The determination of the elongational strain rate distribution is essential for assessing how effectively fluid motion within bursting bubbles at the ocean surface can shear microscopic particles and microorganisms, and could have driven the self-replication of a protobiont.

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37

Diogo, A. C. "On the behaviour of the elongational viscosity of a nematic polymer in elongational flow." Makromolekulare Chemie. Macromolecular Symposia 20-21, no. 1 (July 1988): 329–34. http://dx.doi.org/10.1002/masy.19880200136.

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38

Stefanescu, Eduard A., Simioan Petrovan, William H. Daly, and Ioan I. Negulescu. "Elongational Rheology of Polymer/Clay Dispersions: Determination of Orientational Extent in Elongational Flow Processes." Macromolecular Materials and Engineering 293, no. 4 (April 14, 2008): 303–9. http://dx.doi.org/10.1002/mame.200700371.

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39

Chen, Xiaochuan, Xiaotong Wang, Changlin Cao, Zhongke Yuan, Dingshan Yu, Fei Li, and Xudong Chen. "Elongational Flow Field Processed Ultrahigh Molecular Weight Polyethylene/Polypropylene Blends with Distinct Interlayer Phase for Enhanced Tribological Properties." Polymers 13, no. 12 (June 10, 2021): 1933. http://dx.doi.org/10.3390/polym13121933.

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Herein, we produced a series of ultrahigh molecular weight polyethylene/polypropylene (UHMWPE/PP) blends by elongational-flow-field dominated eccentric rotor extruder (ERE) and shear-flow-field dominated twin screw extruder (TSE) respectively and presented a detailed comparative study on microstructures and tribological properties of UHMWPE/PP by different processing modes. Compared with the shear flow field in TSE, the elongational flow field in ERE facilitates the dispersion of PP in the UHMWPE matrix and promotes the interdiffusion of UHMWPE and PP molecular chains. For the first time, we discovered the presence of the interlayer phase in blends with different processing modes by using Raman mapping inspection. The elongational flow field introduces strong interaction to enable excellent compatibility of UHMWPE and PP and induces more pronounced interlayer phase with respect to the shear flow field, eventually endowing UHMWPE/PP with improved wear resistance. The optimized UHMWPE/PP (85/15) blend processed by ERE displayed higher tensile strength (25.3 MPa), higher elongation at break (341.77%) and lower wear loss of ERE-85/15 (1.5 mg) compared to the blend created by TSE. By systematically investigating the microstructures and mechanical properties of blends, we found that with increased content of PP, the wear mechanism of blends varies from abrasive wear, fatigue wear, to adhesion wear as the dominant mechanism for two processing modes.

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40

Kotaka, T., Akira Kojima, and Masami Okamoto. "Elongational flow opto-rheometry for polymer melts 1. Construction of an elongational flow opto-rheometer and some preliminary results." Rheologica Acta 36, no. 6 (December 17, 1997): 646–56. http://dx.doi.org/10.1007/s003970050080.

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41

Liu, Wei Feng, Jin Ping Qu, Shi Kui Jia, and Yong Qing Zhao. "Study on Mechanical Properties and Phase Morphology of Thermoplastic Polyurethane/Polypropylene Blends Prepared with Vane Extruder." Advanced Materials Research 600 (November 2012): 256–60. http://dx.doi.org/10.4028/www.scientific.net/amr.600.256.

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Thermoplastic polyurethane (TPU)/polypropylene (PP) blends with different weight ratios were prepared in a novel vane extruder generating global and dynamic elongational flow. The results indicated that the addition of TPU elastomer to PP significantly improved the mechanical properties of the blends. From the SEM micrographs it could be clearly observed dispersed TPU deformed to be fibers by the effect of elongational flow. Meanwhile the results observed from DSC curves revealed apparent partial miscibility of the blends and enhanced crystallization ability of PP due to the influence of elongational flow

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42

YAMAMOTO, Satoru, and Takaaki MATSUOKA. "Computer Simulation of Fiber Orientation in Elongational Flow." Seikei-Kakou 11, no. 6 (1999): 510–16. http://dx.doi.org/10.4325/seikeikakou.11.510.

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43

KOBAYASHI, Masatoshi, Jun-ichi TAKIMOTO, and Kiyohito KOYAMA. "Orientation Distribution of Whiskers under Uniaxial Elongational Flow." Seikei-Kakou 7, no. 9 (1995): 590–94. http://dx.doi.org/10.4325/seikeikakou.7.590.

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44

Ferguson, J., N. E. Hudson, B. C. H. Warren, and A. Tomatarian. "Phase changes during elongational flow of polymer solutions." Nature 325, no. 6101 (January 1987): 234–36. http://dx.doi.org/10.1038/325234a0.

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45

OKAMOTO, Masami. "Structure Development of Polymeric Liquids under Elongational Flow." KOBUNSHI RONBUNSHU 56, no. 8 (1999): 508–23. http://dx.doi.org/10.1295/koron.56.508.

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46

khalil, Mouhamad, Pascal hébraud, Ali Mcheik, Houssein Mortada, Hassan Lakis, and Tayssir Hamieh. "Elongational Flow-induced Crystallization in Polypropylene/Talc Nanocomposites." Physics Procedia 55 (2014): 259–64. http://dx.doi.org/10.1016/j.phpro.2014.07.074.

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47

Revenu, Pascale, Jacques Guillet, and Christian Carrot. "Elongational flow of polyethylenes in isothermal melt spinning." Journal of Rheology 37, no. 6 (November 1993): 1041–56. http://dx.doi.org/10.1122/1.550408.

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48

Hingmann, R., and B. L. Marczinke. "Shear and elongational flow properties of polypropylene meltsa)." Journal of Rheology 38, no. 3 (May 1994): 573–87. http://dx.doi.org/10.1122/1.550475.

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49

Greener, J., and J. R. G. Evans. "Uniaxial elongational flow of particle-filled polymer melts." Journal of Rheology 42, no. 3 (May 1998): 697–709. http://dx.doi.org/10.1122/1.550947.

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50

Bhattacharjee, Somendra M., Glenn H. Fredrickson, and Eugene Helfand. "Phase separation of polymer solutions in elongational flow." Journal of Chemical Physics 90, no. 6 (March 15, 1989): 3305–17. http://dx.doi.org/10.1063/1.455885.

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