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  • 1
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Industrial and engineering chemistry 5 (1966), S. 253-259 
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Industrial and engineering chemistry 5 (1966), S. 243-252 
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Industrial and engineering chemistry 6 (1967), S. 388-393 
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
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  • 4
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Industrial & engineering chemistry 51 (1959), S. 874-878 
    ISSN: 1520-5045
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 5
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Industrial and engineering chemistry 2 (1963), S. 143-149 
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Type of Medium: Electronic Resource
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  • 6
    Electronic Resource
    Electronic Resource
    Springer
    Rheologica acta 17 (1978), S. 595-605 
    ISSN: 1435-1528
    Source: Springer Online Journal Archives 1860-2000
    Topics: Chemistry and Pharmacology , Physics
    Description / Table of Contents: Summary A review of the different possibilities for formulating viscoelastic models or theories is given. In steady shear flow such theories allow one to interrelate the various viscometric parameters for a given polymer. The relaxation time model proposed byBogue was chosen because of its relative simplicity. With this choice no independent parameter is introduced into the theory. In the original model an “effective” relaxation time, based on an integration of the strain rate history, was used. In the present work, a generalized averaging mode for the relaxation time is proposed to allow nonsteady deformation histories and non-isothermal temperature histories to be analysed. The advantage of the new mode becomes clear when either isothermal or non-isothermal stress relaxation following isothermal steady state flow is considered. The effect of the steady shear persists into the relaxation period even though no shear is being imposed then. The relaxation times and moduli for a high density polyethylene were determined and used to calculate the isothermal shear stress relaxation following cessation of steady state shear flow. The calculated results are in good agreement with the experimental data ofMenges and coworkers (50, 51).
    Notes: Zusammenfassung Es wird ein Überblick über die Struktur der viskoelastischen Modelltheorien vom Integral-Typ gegeben. Anhand der stationären einfachen Scherströmung wird gezeigt, daß sich alle viskosimetrischen Größen eines Kunststoffes im Rahmen einer solchen Theorie miteinander verknüpfen lassen. Zur Ausarbeitung eines Modells wählen wir wegen ihrer Einfachheit die Boguesche Relaxationszeit. Im Rahmen unserer Untersuchungen stellen wir fest, daß mit der Wahl dieser Relaxationszeit kein unabhängiger Parameter in die Modelltheorie eingeführt wird. Um auch instationäre Strömungsvorgänge analysieren zu können, wird eine neue mittlere Relaxationszeit definiert. Für isotherme Strömungen führt diese Mittelwertbildung zum selben Resultat wie mit einer gemittelten zweiten Invarianten des Deformationsgeschwindigkeitstensors. Der Vorteil dieser Mittelwertbildung zeigt sich deutlich bei der nicht-isothermen Spannungsrelaxation nach stationärer isothermer Scherströmung. In den dafür abgeleiteten Gleichungen ist auch weiterhin ein Einfluß der Deformationsgeschwindigkeit bzw. des Schergradienten enthalten. Schließlich werden noch Relaxationszeiten und -moduln eines Polyäthylens hoher Dichte bestimmt und daraus anschließend die isotherme Relaxation der Schubspannung nach einer stationären Scherströmung berechnet. Die erzielte Übereinstimmung mit den experimentellen Ergebnissen vonMenges und Mitarbeitern (50, 51) ist gut.
    Type of Medium: Electronic Resource
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  • 7
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Journal of Applied Polymer Science 25 (1980), S. 575-588 
    ISSN: 0021-8995
    Keywords: Chemistry ; Polymer and Materials Science
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Mechanical Engineering, Materials Science, Production Engineering, Mining and Metallurgy, Traffic Engineering, Precision Mechanics , Physics
    Notes: As part of a continuing study of nonisothermal rheology (meaning the simultaneous application of strain and temperature changes), we here consider the behavior of polystyrene near the glass transition temperature Tg. In particular, we measured the increase of the apparent Tg as the cooling rate is increased from 0.003 to 4.5°C/sec. This change (up to 16°C increase) has both practical and theoretical implications. For enhancing the mechanical properties of a glassy product, one desires maximum orientation (stress) just prior to quenching; the optimum deformation/temperature strategy for maximizing stress is affected by the level of Tg. By using a nonisothermal strategy we were able to produce higher frozen-in orientations, and thus higher mechanical properties, than have been previously reported. For a theoretical understanding of the rubbery state just prior to quenching, we used the generalized time-temperature superposition of our prior work; we found that a modified shift factor of the form aT(T,TRg), where TRg refers to a rate-dependent Tg, gives an improved fit to data but is not by itself adequate.
    Additional Material: 14 Ill.
    Type of Medium: Electronic Resource
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  • 8
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 16 (1970), S. 53-57 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An explicit, four-constant model for viscosity and normal stresses in simple shear has been developed by simplifying the integral theory of Bernstein, Kearsley, and Zapas. In essence the procedure involves curve-fitting the linear relaxation spectrum. The four constants appear also in equations for the stress distribution and for pressure drop in accelerative flow between flat plates; flow along rays is assumed. The equations reduce to second-order theory and to Newtonian theory as a Deborah number becomes small. Comparison of the predicted stress distributions with previously published stress birefringent data shows good agreement; because of the low shear rates, however, the check is not demonstrating very strong departures from the second-order asymptote. Certain other theoretical results, including pressure drop predictions, are also noted.
    Additional Material: 5 Ill.
    Type of Medium: Electronic Resource
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  • 9
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 10 (1964), S. 723-727 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Velocity profiles and friction factors of non-Newtonian fluids in turbulent pipe flow can be displayed with the semiempirical forms developed for Newtonian fluids in which the apparent viscosity evaluated at the wall shear stress is used.Friction factors and velocity profiles were obtained for a dilute and a concentration aqueous thoria suspension and compared with the Newtonian correlations and with previous data obtained from widely different non-Newtonian fluids including a viscoelastic fluid. A relationship is shown between the decrease of the friction factor and the change in the velocity distribution towards a more laminar profile.A generalized method of deriving the friction factor-Reynolds number plot from the velocity profile based on the von Kármán relationship for Newtonian fluids is derived and compared with the data.
    Additional Material: 7 Ill.
    Type of Medium: Electronic Resource
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  • 10
    Electronic Resource
    Electronic Resource
    Hoboken, NJ : Wiley-Blackwell
    AIChE Journal 11 (1965), S. 1026-1032 
    ISSN: 0001-1541
    Keywords: Chemistry ; Chemical Engineering
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Chemistry and Pharmacology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Birefringent studies have been carried out on a viscoelastic fluid (polystyrene in Aroclor) flowing in straight, converging, and diverging channels, for the purpose of obtaining point-by-point stress data (the shear stress and the difference in normal stresses). A preliminary analysis in terms of the Coleman-Noll second order theory for viscoelastic fluids shows good agreement.
    Additional Material: 12 Ill.
    Type of Medium: Electronic Resource
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