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            "title": "Effects of temperature on the flow of copolymer melts",
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            "abstractNote": "The temperature dependent flow behaviour of copolymers is useful for obtaining the monomolecular melt, which is essential for processing in order to get the defect free copolymer products. Melt flow index is shown to be useful in depicting the temperature dependence of copolymer melts and in estimation of their flow activation energy. The three copolymer systems included are styrene-butadiene-styrene (SBS), ethyl vinyl acetate (EVA) and a liquid crystalline copolyester based on hydroxybenzoic acid-polyethylene terephthalate (HBA-PET) respectively. The observed behaviour indicates a significant degree of retention of physical network structure below the cross-over point in a MFI-temperature−1 plot",
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                    "tag": "activation energy"
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                    "tag": "block copolymers"
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                    "tag": "copolymer melts"
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            "title": "A simplistic route to viscous heat estimations in polymer processing",
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            "abstractNote": "Plastics have been highly successful in replacing such conventional materials as metals, glass, and wood in a wide variety of applications due to their special property advantages such as high strength-to-weight ratio, corrosion resistance, versatility of part design, and ease of fabrication. The various plastic products are formed by processing polymers by one of the number of available techniques such as injection molding, compression molding, blow molding, profile extrusion, and sheet extrusion followed by stamping or thermoforming. In all these processes, the molten polymer is subjected to a wide range of shear rates and temperatures. During deformation, viscous heat is dissipated due to the friction between the highly viscous polymer melt and the various parts of the processing equipment that it comes in contact with. The viscous heat dissipated leads to a temperature rise, resulting in an offset of the setting of the extruder temperature profile with respect to throughput rate or screw speed. For all high output rate operations, it is essential to know the viscous heat generated in order to appropriately design the conventional extruder screw so as to minimize the temperature increase in the process of plastication and to optimize the extruder temperature profile with respect to the throughput rate or screw speed. Viscous heat estimation is also critical when processing heat- sensitive polymers so as to maintain the melt temperature well below the degradation point.",
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            "title": "A new method for the determination of flow activation energy of polymer melt",
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            "abstractNote": "A method based on the melt flow index rather than the conventional zero shear viscosity is suggested to estimate the activation energy for viscous flow of polymer melts. The method is particularly attractive due to its simplicity and because all the conditions for its derivation fit rather well within the validity range of applicability of the Arrhenius type equation relating viscosity and temperature. Values of activation energy for viscous flow using the suggested technique are calculated for a number of polymers falling within the olefinic, styrenic, cellulosic, and engineering thermoplastic groups.",
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            "abstractNote": "A review of the developments in the field of heat transfer in non-Newtonian fluids flowing through porous media. The chapter focuses on non-Newtonian-fluid heat transfer in porous media and reviews the existing literature, the number of citations in which has rapidly grown reaching a sizable number on the topic. The existing body of information covers most of the relevant Darcy and non-Darcy situations in boundary layer and confined flows. Heat transfer in porous media is of great pragmatic importance in a wide variety of scientific and engineering applications, as can be seen from some of the applications summarized in the chapter. The chapter presents pure Darcy natural-convection boundary-layer problem for flow past an isothermal vertical flat plate, a nonisothermal smooth surface of arbitrary shape, and a nonuniform horizontal flat plate embedded in a porous medium saturated with an Ostwald-de Waele power-law fluid. The problem of pure Darcy natural-convection boundary-layer flow past an isothermal vertical flat plate embedded in a porous medium saturated with a Herschel-Bulkley fluid—namely, a pseudoplastic fluid with yield stress is discussed. The problem of pure Darcy natural-convection boundary-layer flow past an isothermal vertical flat plate embedded in a porous medium saturated with an elastic Boger fluid with constant viscosity is discussed. The chapter presents pure Darcy mixed-convection boundary-layer problem for flow past an isothermal vertical flat plate and a nonisothermal smooth surface of arbitrary shape embedded in a porous medium saturated with an Ostwald-de Waele power-law fluid. The problem of pure Darcy mixed-convection boundary-layer flow past an isothermal vertical flat plate embedded in a porous medium saturated with an elastic Boger fluid with constant viscosity is presented. The chapter presents some more additional topics on steady-state convection. Nonsteady state convections based on pure Darcy regime are discussed.",
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                    "firstName": "A.V.",
                    "lastName": "Shenoy"
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            "abstractNote": "There have been many attempts in the literature to develop analogies for momentum, heat and mass transfer to drag reducing fluids; however, none have considered the presence of a pressure gradient when formulating the analogies. In the present work, a momentum/heat transfer analogy has been developed under the influence of small pressure gradient for drag reducing fluids using the Nakayama et al. (1984) solution methodology for Newtonian fluids. The results of the present analysis have been found to compare well with existing theoretical expressions.De nombreuses idées ont été publiées pour établir des analogies entre les transferts de quantité de mouvement, de chaleur et de matière pour les fluides de réduction de traǐnée. Cependant, aucune ne considère la présence d'un gradient de pression dans la formulation des analogies. Dans cet article, nous établissons une analogie entre le transfert de quantité de mouvement et le transfert de chaleur sous l'influence d'un faible gradient de pression pour les fluides de réduction de traǐnée en utilisant la méthodologie de résolution de Nakayama et al. (1984) pour les fluides newtoniens. Nous avons trouvé que les résultats de notre analyse se comparent bien aux expressions théoriques existantes.",
            "publicationTitle": "International Journal of Heat and Mass Transfer",
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                    "tag": "momentum transfer"
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            "abstractNote": "There have been many attempts in the literature to develop analogies for momentum, heat and mass transfer to drag reducing fluids; however, none have considered the presence of a pressure gradient when formulating the analogies. In the present work, a momentum/heat transfer analogy has been developed under the influence of small pressure gradient for drag reducing fluids using the Nakayama et al. (1984) solution methodology for Newtonian fluids. The results of the present analysis have been found to compare well with existing theoretical expressions.De nombreuses idées ont été publiées pour établir des analogies entre les transferts de quantité de mouvement, de chaleur et de matière pour les fluides de réduction de traǐnée. Cependant, aucune ne considère la présence d'un gradient de pression dans la formulation des analogies. Dans cet article, nous établissons une analogie entre le transfert de quantité de mouvement et le transfert de chaleur sous l'influence d'un faible gradient de pression pour les fluides de réduction de traǐnée en utilisant la méthodologie de résolution de Nakayama et al. (1984) pour les fluides newtoniens. Nous avons trouvé que les résultats de notre analyse se comparent bien aux expressions théoriques existantes.",
            "publicationTitle": "The Canadian Journal of Chemical Engineering",
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            "creators": [
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                    "firstName": "A. V.",
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            "abstractNote": "A theoretical analysis of laminar natural convection heat transfer from a slender vertical cone to a power-law fluid has been done by the approximate integral method. Assuming unequal thermal and momentum boundary layer thicknesses, and using the appropriate boundary and compatibility conditions, a “similar” solution of the boundary layer equations has been obtained for high Prandtl numbers. Due to lack of experimental data for power-law fluids, a comparison of the predictions of the present analysis has been done with the experimental data available for Newtonian fluids and good agreement has been found. On a fait, au moyen de la méthode intégrale approchée, une analyse théorique du transfert de chaleur par convection naturelle laminaire, entre un cǒne vertical effilé et un fluide obéissant à la loi de puissance. En supposant des épaisseurs inégales pour les couches limites relatives au transfert de chaleur et de quantité de mouvement, et en employant des conditions limites ainsi que des conditions de compatibilité appropriées, on a obtenu une solution “semblable” des équations relatives aux couches limites pour des nombres de Prandtl élevés. Par suite du manque de données expérimentales sur les fluides qui obéissent à la loi de puissance, on a comparé les prévisions de l'analyse précitée avec les résultats expérimentaux qui sont disponibles dans le cas des fluides newtoniens et l'on a trouvé qu'il y avait une bonne concordance.",
            "publicationTitle": "The Canadian Journal of Chemical Engineering",
            "publisher": "",
            "place": "",
            "date": "12/1983",
            "volume": "61",
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            "date": "10/1994",
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            "title": "Forced convection heat transfer to an elastic fluid of constant viscosity flowing through a channel filled with a Brinkman-Darcy porous medium",
            "creators": [
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                    "firstName": "A. V.",
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            "abstractNote": "An analysis is presented of fully developed flow and heat transfer in a channel confined by two parallel walls subjected to uniform heat flux in a highly porous medium saturated with an elastic fluid of constant viscosity. The Brinkman-extended Darcy model is used for studying the effect of the boundary viscous frictional drag on the heat transfer characteristics. The approximate integral method is employed to obtain a solution.Die Untersuchung bezieht sich auf die voll ausgebildete Strmung und den Wrmebergang in einem von zwei parallelen Wnden begrenzten Kanal bei konstantem Wrmeflu am Rande. Der Kanalraum wird von einem hochporsem Medium ausgefllt, das mit einem elastischen Fluid konstanter Zhigkeit getrnkt ist. Der Einflu des Reibungswiderstandes an den Kanalgrenzen auf das Wrmebertragungsverhalten wird mit Hilfe des von Brinkman erweiterten Darcy-Transportgesetzes ermittelt. Die Lsung erfolgte unter Anwendung eines nherungsweisen gltigen Integralverfahrens",
            "publicationTitle": "W�rme- und Stoff�bertragung",
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            "date": "5/1993",
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            "title": "Forced convection heat transfer through boundary layers in non-Newtonian fluids",
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                    "firstName": "A.",
                    "lastName": "Nakayama"
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            "abstractNote": "A theoretical analysis is proposed for the forced convective heat transfer from external surfaces immersed in non-Newtonian fluids of the   power-law model.   The   integral  method    previously introduced for  Newtonian fluids has  been successfully extended to the  non-Newtonian fluids over  a flat  plate  and  a wedge  of an arbitrary included  angle.  The  integral momentum and  energy  equations are  transformed into  a pair  of characteristic equations, which  can  readily be solved  for  the velocity  shape factor and  boundary layer  thickness ratio, once the exponents in the expressions for the power-law model,  Falkner-Skan free  stream velocity  and  wall  temperature variation are  specified.  It has been  also  found  that  a  closed-form asymptotic expression derived   under  the  assumption of large  Prandtl  number, is valid  practically for  all  power  law  fluids,  hence,  can  be  used  for  a  speed  and accurate  estimation  of  the  local   heat   transfer  to  non- Newtonian  fluids.  The   agreement of the predicted results and exact solutions appears to be excellent. Discussions further extend to the case of uniform heat flux.",
            "publicationTitle": "Trans. Japan Soc. Mech. Engrs",
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            "date": "1985",
            "volume": "851",
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            "pages": "2026",
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                    "tag": "boundary layer flow"
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                    "tag": "forced convection"
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                    "tag": "heat transfer"
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            "title": "Forced convection heat transfer from axisymmetric bodies to non-Newtonian fluids",
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                    "firstName": "A. V.",
                    "lastName": "Shenoy"
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            "abstractNote": "A theoretical analysis for forced convection heat transfer from axisymmetric bodies immersed in non-Newtonian power-law fluids has been performed. Results for the velocity shape factor, local friction coefficient, and the Nusselt number are presented for different values of Prandtl number and the power-law index. The local friction coefficient results are compared with available experimental data and it is shown that asymptotic expressions suffice to get accurate predictions of heat transfer at low and high Prandtl numbers.On a effectué une analyse théorique pour le transfert de chaleur par convection forcée à partir de corps à symétrie axiale immergés dans les fluides non-newtoniens de type loi de puissance. Les résultats obtenus pour le facteur de forme de vitesse, le coefficient de friction local et le nombre de Nusselt, sont présentés pour différentes valeurs du nombre de Prandtl et de l'indice de la loi de puissance. Les résultats du coefficient de friction local sont comparés avec les données expérimentales disponibles et on montre que les expressions asymptotiques suffisent pour obtenir des prédictions précises du transfert de chaleur pour des nombres de Prandtl grands ou petits.",
            "publicationTitle": "The Canadian Journal of Chemical Engineering",
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            "pages": "680-686",
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                    "firstName": "A. V.",
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            "abstractNote": "The effect of buoyancy on the heat transfer during upward turbulent flow of drag reducing fluids in vertical tubes has been theoretically analyzed. A criteria has been established for limiting the decrease in heat transfer to less than 5% for fluids of varying drag reducing ability. The final expression for quantitative evaluation of natural convection effect on forced convection could be applied to upward as well as downward turbulent flow of drag-reducing fluids merely by a change in sign of the controlling term.Es wird der Einflu des Auftriebes auf den Wrmebergang bei turbulenter Aufwrtsstrmung von widerstandsreduzierenden Fluiden in vertikalen Rohren theoretisch analysiert. Dabei wird ein Kriterium fr die Begrenzung der Abnahme des Wrmebergangs auf weniger als 5% fr Fluide unterschiedlicher Widerstandsverringerung aufgestellt. Die endgltige mathematische Formulierung fr die quantitative Beschreibung des Einflusses der natrlichen Konvektion auf die erzwungene Konvektion konnte sowohl auf Aufwrts-als auch auf Abwrtsstrmung eines Fluids mit vermindertem Strmungswiderstand einfach dadurch angewandt werden, da man ein Vorzeichen in dem die Strmung bestimmenden Term ndert.",
            "publicationTitle": "Warme- und Stoff�bertragung",
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            "title": "Darcy natural, forced and mixed convection heat transfer from an isothermal vertical flat plate embedded in a porous medium saturated with an elastic fluid of constant viscosity",
            "creators": [
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                    "firstName": "A.V.",
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            "abstractNote": "The governing equation for Darcy flow of elastic fluids with constant viscosity has been derived from first principles and presented for the first time in the literature. The problem of Darcy natural, forced and mixed convection from an isothermal vertical flat plate within a porous medium saturated with an elastic fluid of constant viscosity has been solved using the approximate integral method and similarity solutions have been obtained. The results have been compared for the limiting cases with exact solutions existing in the literature and found to agree within a maximum error bound.",
            "publicationTitle": "International Journal of Engineering Science",
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            "date": "4/1992",
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            "pages": "455-467",
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            "DOI": "10.1016/0020-7225(92)90037-H",
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                    "tag": "Darcy forced convection"
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                    "tag": "constant viscosity"
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            "abstractNote": "The governing equation for Darcy-Forchheimer flow of non-Newtonian inelastic power-law fluid through porous media has been derived from first principles. Using this equation, the problem of Darcy-Forchheimer natural, forced, and mixed convection within the porous media saturated with a power-law fluid has been solved using the approximate integral method. It is observed that a similarity solution exists specifically for only the case of an isothermal vertical flat plate embedded in the porous media. The results based on the approximate method, when compared with existing exact solutions show an agreement of within a maximum error bound of 2.5%.",
            "publicationTitle": "Transport in Porous Media",
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            "date": "6/1993",
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            "pages": "219-241",
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