Some problems concerning nonstationary currents in dense plasma systems confined by walls

Nonstationary currents are examined in a dense magnetized plasma with 1, in which energy release and heat loss by thermal conduction and radiation are possible. Solutions are found in two limiting cases: ¦f¦ ¦ div (T)¦ and ¦f¦ ¦ div(T)¦ (f is the radiation intensity, is the coefficient of heat conduction, and T is the temperature). In the first case a solution was obtained of some problems of the cooling and heating of a plasma illustrated in part by the evolution in time of the temperature profile in the boundary layer. In the second case an isomorphic solution was found for an arbitrary dependence of the coefficient of heat conduction on the temperature, pressure, and magnetic field.Translated from Zhurnal Prikladnoi Mekhaniki i Tekhnicheskoi Fiziki, No. 1, pp. 3–8, January–February, 1972.The author is grateful to G. I. Budker for formulating the problem.     

Rheology of molten polymers

Summary TheCross equation describes the flow of pseudoplastic liquids in terms of an upper and a lower Newtonian viscosity corresponding to infinite and zero shear, and ₀, and of a third material constant related to the mechanism of rupture of linkages between particles in the intermediate, non-Newtonian flow regime, Calculation of of bulk polymers is important, since it cannot be determined experimentally. The equation was applied to the melt flow data of two low density polyethylenes at three temperatures.Using data in the non-Newtonian region covering 3 decades of shear rate to extrapolate to the zero-shear viscosity resulted in errors amounting to about onethird of the measured ₀ values. The extrapolated upper Newtonian viscosity was found to be independent of temperature within the precision of the data, indicating that it has a small activation energy.The ₀ values were from 100 to 1,400 times larger than the values at the corresponding temperatures.The values of were large compared to the values found for colloidal dispersions and polymer solutions, but decreased with increasing temperature. This shows that shear is the main factor in reducing chain entanglements, but that the contribution of Brownian motion becomes greater at higher temperatures.

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Zusammenfassung Die Gleichung vonCross beschreibt das Fließverhalten von pseudoplastischen Flüssigkeiten durch drei Konstante: Die obereNewtonsche Viskosität (bei sehr hohen Schergeschwindigkeiten), die untereNewtonsche Viskosität ₀ (bei Scherspannung Null), und eine Materialkonstante, die vom Brechen der Bindungen zwischen Partikeln im nicht-Newtonschen Fließbereich abhängt. Die Berechnung von ist wichtig für unverdünnte Polymere, wo man sie nicht messen kann.Die Gleichung wurde auf das Fließverhalten der Schmelzen von zwei handelsüblichen Hochdruckpolyäthylenen bei drei Temperaturen angewandt. Die Werte von ₀, durch Extrapolation von gemessenen scheinbaren Viskositäten im Schergeschwindigkeitsbereich von 10 bis 4000 sec^–1 errechnet, wichen bis 30% von den gemessenen ₀-Werten ab. Die Aktivierungsenergie der war so klein, daß die-Werte bei den drei Temperaturen innerhalb der Genauigkeit der Extrapolation anscheinend gleich waren. Die ₀-Werte waren 100 bis 1400 mal größer als die-Werte.Im Verhältnis zu kolloidalen Dispersionen und verdünnten Polymerlösungen war das der Schmelzen groß, nahm aber mit steigender Temperatur ab. Deshalb wird die Verhakung der Molekülketten hauptsächlich durch Scherbeanspruchung vermindert, aber der Beitrag derBrownschen Bewegung nimmt mit steigender Temperatur zu.

     

Reibungs- und Verschleiß-Messungen im EHD-Kontakt bei allseitig hohem Druck

Zusammenfassung Um bei einem Punktkontakt den Einfluß der EHD-Parameter, _a ,u, F undT einzeln an stets demselben Öl untersuchen zu können, wurde eine unter allseitighohem Druck betriebene VKA-Apparatur konstruiert. Die Anpreßkraft wird durch eine im Autoklaven befindliche hydraulische Presse erzeugt, die Kraft und das Drehmoment innerhalb des Autoklaven gemessen. Der Antrieb erfolgt mit einem 5 kW-Motor über eine selbstabdichtende Wellendurchführung.Die Last, bei der die Vollschmierung zusammenbricht, wird bei linearem Verlauf der log – p-Isothermen in Abhängigkeit von _a undu befriedigend durch die Formel vonArchard undKirk wiedergegeben, wenn für die kritische Filmdicke das 2,09fache der Oberflächenrauhigkeit einer Kugel eingesetzt wird.Bei nichtlinearem (degressivem) Verlauf der log–p-Kurven treten dagegen erhebliche Differenzen auf. Um das Viskositäts-Druckverhalten besser zu berücksichtigen, wird eine Formel aufgestellt, die anstelle von und _a die effektive Viskosität _W bei 2/3 des Hertzschen Maximalwertes enthält. _W wird dabei aus gemessenen – p-Isothermen über eine Formel vonRodermund berechnet.

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Summary To prove separately the influence of the EHD-parameters, _a ,u, F andT on the critical load of a point contact, a VKA tester for use inside a high pressure chamber has been constructed. The hydraulic press, which produces the load, is installed within the autoclave. The uniaxial force and the friction torque is measured inside, too. The drive produced by a 5 KW motor is introduced by a self-sealing shaft bushing.If the pressure behaviour log–p of the oil is a straight line, the load at which the hydrodynamic lubrication breaks down is represented correctly as a function of _a andu by an equation ofArchard andKirk. Thereby the critical film thickness is supposed as 2.09 times greater than the surface roughness.Considerable deviations are found for log – p pressure curves with decreasing incline. To take into account this type of behaviour of the oil a new formula is proposed using the effective viscosity _W at 2/3 of the Hertzian pressureP _max instead of and _{a W} is calculated from the measured – p isotherms by an equation ofRodermund.

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Mit 6 Abbildungen     

Deformation to breaking of deep water gravity waves

The results of laboratory observations of the deformation of deep water gravity waves leading to wave breaking are reported. The specially developed visualization technique which was used is described. A preliminary analysis of the results has led to similar conclusions than recently developed theories. As a main fact, the observed wave breaking appears as the result of, first, a modulational instability which causes the local wave steepness to approach a maximum and, second, a rapidly growing instability leading directly to the breaking.List of symbols L total wave length - H total wave height - crest elevation above still water level - trough depression below still water level - wave steepness =H/L - crest steepness =/L - trough steepness =/L - F ₁ forward horizontal length from zero-upcross point (A) to wave crest - F ₂ backward horizontal length from wave crest to zero-downcross point (B) - crest front steepness =/F ₁ - crest rear steepness =/F ₂ - vertical asymmetry factor=F ₂/F ₁ (describing the wave asymmetry with respect to a vertical axis through the wave crest) - µ horizontal asymmetry factor=/H (describing the wave asymmetry with respect to a horizontal axis: SWL) - T ₀ wavemaker period - L ₀ theoretical wave length of a small amplitude sinusoïdal wave generated at T _inf0 ^sup–1 frequency - ₀ average wave height     

Viscous properties of calcium carbonate filled polymer melts

Summary The viscous properties of calcium carbonate filled polyethylene and polystyrene melts were examined. The relative vircosity _r defined in the previous paper gave an asymtptotic value( _r)_l in the range of the shear stress below 10⁵ dyne/cm².( _r)_l of the calcium carbonate filled system was higher than that of the glass beads or glass balloons filled system at the same volume fraction of the filler. Maron-Pierce equation with ₀ = 0.44 was able to approximate the( _r)_l — relationship. However, it was deduced here that the high value of( _r)_l of calcium carbonyl filled system was due to the apparent increase of and this increase was attributed to the fixed polymer layer formed on the powder particle. By assuming the particle as a sphere with a diameter of 2 µm, the thickness of the fixed polymer layer was estimated as about 0.17 µm. The yield stress estimated from the Casson's plots increased exponentially with.

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Zusammenfassung Es wurden die viskosen Eigenschaften von Polyäthylen-und Polystyrol-Schmelzen untersucht, die mit Kalziumkarbonat-Teilchen gefüllt waren. Für die relative Viskosität _r, wie sie in einer vorangegangenen Veröffentlichung definiert worden war, ergab sich bei Schubspannungen unterhalb 10⁵ dyn/cm² ein asymptotischer Wert( _r)_l. Dieser war bei den mit Kalziumkarbonat gefüllten Schmelzen höher als bei Schmelzen, die bis zur gleichen Volumenkonzentration mit Glaskugeln oder Glasballons gefüllt waren. Die ( _r) _l —-Abhängigkeit ließ sich durch eine Gleichung nachMaron und Pierce mit ₀ = 0,44 beschreiben. Es wurde jedoch geschlossen, daß der hohe( _r)_l-Wert der mit Kalziumkarbonat gefüllten Schmelzen auf eine scheinbare Zunahme von zurückzuführen ist, verursacht durch eine feste Polymerschicht auf der Teilchenoberfläche. Unter Annahme kugelförmiger Teilchen mit einem Durchmesser von 2 µm ließ sich die zugeordnete Schichtdicke zu 0,17 µm abschätzen. Die mittels der Casson-Beziehung geschätzte Fließspannung ergab eine exponentielle-Abhängigkeit.

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With 7 figures and 1 table     

Study of transient and quasi-steady ablation of polytetrafluoroethylene layers

A study of the transient one-dimensional ablation of a PTFE-layer heated by a constant heat flux at the surface and cooled by finite heat transfer at the back is performed using a previously presented analytical model. The influences of various parameters upon the course of ablation are investigated and some limiting cases are discussed. The numerical solution for the quasi-steady ablation is presented by graphs, which are also approximated by correlations for the computation of the coupled boundary layer and PTFE-ablator.

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Instationäre und quasi-stationäre Ablation von PTFE-Schichten

Zusammenfassung Die instationäre, eindimensionale Ablation einer PTFE-Schicht wird untersucht, der ein konstanter Wärmestrom an der Oberfläche zugeführt und ein Kühlstrom durch endlichen Wärmeübergang an der Rückseite abgeführt wird. Dabei wird ein analytisches Modell zugrundegelegt, über das kürzlich berichtet wurde, und verschiedene Einflüsse auf den Ablationsverlauf betrachtet sowie Grenzfälle diskutiert. Die numerische Lösung für quasistationäre Ablation kann Diagrammen entnommen werden. Außerdem werden hierfür Korrelationen angegeben für die simultane Berechnung des PTFE-Ablators mit einer Grenzschicht.

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Nomenclature a thermal diffusivity - c polymer mass fraction: density ratio of the decomposing and the undecomposed material - k coefficient of heat transmission - m ablation rate (ablating mass flux) - q heat flux to the surface - Q dimensionless heat flux - t time - T temperature - x coordinate - x_O initial layer thickness - y₁ (x-)/(-), transformed coordinate - y₂ (x-)/(-), transformed coordinate - penetration bond - phase interface - thermal conductivity of crystalline PTFE at the melting point - layer thickness Indices k coolant - at the phase interface (melting point) - at the surface     

Über die Stabilität viskometrischer Strömungen

Zusammenfassung Die Stabilität der ebenen Couette- und der ebenen Poiseuille-Strömung nicht-newtonscher Fluide wird für kleine Störungen in der viskometrischen Ebene untersucht. Der Einfluß der Relaxationszeit der Störungen wird vernachlässigt. Es wird gezeigt, daß die ebene Couette-Strömung unabhängig von der ReZahl instabil wird, fallsd(N)/d > 4 _>d gilt. Hier bedeuten die Schergeschwindigkeit,N den ersten Normalspannungskoeffizienten, die Viskosität und _d die differentielle Viskosität ( _d =d/d). Das gleiche Kriterium gilt mit den Daten an der Kanalwand auch für die Poiseuille-Strömung. In diesem Fall oszillieren die Eigenfunktionen in einer sehr dünnen, wandnahen Schicht und klingen im Flüssigkeitsinnern sehr rasch ab.

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Summary The stability of plane Couette and plane Poiseuille flow of a non-Newtonian fluid is investigated for small perturbations in the viscometric plane. The influence of the relaxation time of the perturbations is neglected. It is shown that plane Couette flow will become unstable independently of Reynolds number ifd(N)/d > 4 _d holds. Here are the rate of shear velocity,N the first normal stress coefficient, the viscosity and _d the differential viscosity ( _d =d/d). The same criterion holds also for plane Poiseuille flow with the data taken at the wall. In this case the eigenfunctions are oscillating in a very thin layer near the wall and decaying very rapidly in the inner region of the flow field.

Mit 11 Abbildungen     

Das erweiterte Korrespondenzgesetz für die dynamische Idealviskosität und die Idealwärmeleitfähigkeit reiner Stoffe

Zusammenfassung Zur Berechnung der dynamischen Idealviskosität Ideal (T) und der Idealwärmeleitfähigkeit ideal (T) benötigt man die kritische TemperaturT _kr, das kritische spezifische Volum _kr, die MolmasseM, den kritischen Parameter _kr und die molare isochore WärmekapazitätC _v(T). Sowohl das theoretisch, als auch das empirisch abgeleitete erweiterte Korrespondenzgesetz ergeben eine für praktische Zwecke ausreichende Genauigkeit für die Meßwertwiedergabe, die bei den assoziierenden Stoffen und den Quantenstoffen jedoch geringer ist als bei den Normalstoffen.

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The extended correspondence law for the ideal dynamic viscosity and the ideal thermal conductivity of pure substances

For the calculation of the ideal dynamic viscosity Ideal (T) and the ideal thermal conductivity ideal (T) the critical temperatureT _kr, the critical specific volumev _kr, the molecular massM, the critical parameter _kr, and the molar isochoric heat capacityC _v(T) is needed. Not only the theoretically determined but also the empirically determined extended correspondence law gives for practical use a good representation of the measured data, which for the associating substances and the quantum substances is not so good as for the normal substances.

     

Dynamic melt viscoelastic behavior of random copolymers

Summary The viscoelastic properties of 65/35 styrenen-butyl methacrylate random copolymers were determined using the Eccentric Rotating Disks device of the Rheometrics Mechanical Spectrometer. Similar to the behavior observed in homopolymers, an increase in the molecular weight of the copolymer resulted in extension of the rubbery plateau and in a reduction in the terminal region. The dynamic complex viscosity showed onset of non-Newtonian flow at higher frequencies, with the non-Newtonian region increasing with increasing molecular weight.The elastic modulus,G, was dependent upon the frequency,, asG ^1.5 in the terminal region, rather than asG ² observed for polystyrene. The viscous modulus,G, was proportional to the frequency,, asG , similar to what is observed for polystyrene. The dynamic viscosity | ^*| at high frequencies showed a region independent of molecular weight where a power law of | ^*| ^0.9 is applicable, consistent with entanglement models. Thy dynamic viscosity at low frequencies in the Newtonian region is related to molecular weight as |^*| . Using WLF equations, the coefficient of expansion, _f , was obtained that, together with glass transition, showed a negative deviation from the Fox-Flory relationship.

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Zusammenfassung Die viskoelastischen Eigenschaften von statistischen 65/35-Styrol/n-Butyl-Methacrylat-Kopolymeren wurden mit Hilfe einer Maxwell-Rheometer-Anordnung in Verbindung mit dem Mechanischen Spektrometer der Fa. Rheometrics bestimmt. Ähnlich dem bei Homopolymeren beobachteten Verhalten ergab sich auch hier mit wachsendem Molekulargewicht eine Verbreiterung des Kautschuk-Plateaus und eine Verkleinerung des Endbereichs. Die komplexe Viskosität zeigte erst bei höheren Frequenzen das Einsetzen nicht-newtonschen Fließens an, wobei der nichtnewtonsche Bereich mit steigendem Molekulargewicht größer wurde.Der SpeichermodulG ergab sich im Endbereich als proportional zu ^1,5, im Unterschied zu der bei Polystyrol beobachteten Proportionalität mit ². Dagegen war der VerlustmodulG der Frequenz direkt proportional, ähnlich wie es auch bei Polystyrol beobachtet worden war. Die dynamische Viskosität | ^*| zeigte unabhängig vom Molekulargewicht bei hohen Frequenzen einen Bereich, in dem eine Potenz-Beziehung | ^*| ~ ^0,9 herrschte, was auf die Wirkung von Verzweigungen hindeutet. Dagegen galt bei den niedrigen Frequenzen des newtonschen Bereichs|^*| ~ . Mit Hilfe der WLF-Gleichung wurde der Ausdehnungskoeffizient _f bestimmt, der ebenso wie der Glasübergang eine negative Abweichung von der Fox-Flory-Beziehung zeigte.

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With 10 figures and 1 table     

On laminar flow through a uniformly porous pipe

Numerous investigations ([1] and [4–9]) have been made of laminar flow in a uniformly porous circular pipe with constant suction or injection applied at the wall. The object of this paper is to give a complete analysis of the numerical and theoretical solutions of this problem. It is shown that two solutions exist for all values of injection as well as the dual solutions for suction which had been noted by previous investigators. Analytical solutions are derived for large suction and injection; for large suction a viscous layer occurs at the wall while for large injection one solution has a viscous layer at the centre of the channel and the other has no viscous layer anywhere. Approximate analytic solutions are also given for small values of suction and injection.

Nomenclature

General r distance measured radially - z distance measured along axis of pipe - u velocity component in direction of z increasing - v velocity component in direction of r increasing - p pressure - density - coefficient of kinematic viscosity - a radius of pipe - V velocity of suction at the wall - r ²/a ² - R wall or suction Reynolds number, Va/ - f() similarity function defined in (6) - u ₀() eigensolution - U(0) a velocity at z=0 - K an arbitrary constant - B _K Bernoulli numbers Particular Section 5 perturbation parameter, –2/R - ² a constant, –K - x / - g(x) f()/ Section 6 perturbation parameter, –R/2 - ² a constant, –K - g() f() - g _c ()=g() near centre of pipe - * point where g()=0 Section 7 2/R - ² K - t (1–)/ - w(t, ) [1–f(t)]/ - ₀, ₁ constants - g() f()– ₀ - ₀/ - ₀ a constant - * point where f()=0     

Testing viscometric predictions of the internal viscosity model,using dilute viscous theta solutions

A stress-symmetrized internal viscosity (I.V.) model for flexible polymer chains, proposed by Bazua and Williams, is scrutinized for its theoretical predictions of complex viscosity ^* () = – i and non-Newtonian viscosity (), where is frequency and is shear stress. Parameters varied are the number of submolecules,N (i.e., molecular weightM = NM _s ); the hydrodynamic interaction,h ^*; and/f, where andf are the I.V. and friction coefficients of the submolecule. Detailed examination is made of the eigenvalues _p (N, h ^*) and how they can be estimated by various approximations, and property predictions are made for these approximations.Comparisons are made with data from our preceding companion paper, representing intrinsic properties [], [], [] in very viscous theta solutions, so that theoretical foundations of the model are fulfilled. It is found that [ ()] data can be predicted well, but that [ ()] data cannot be matched at high. The latter deficiency is attributed in part to unrealistic predictions of coil deformation in shear.     

Rheologische Messungen an Polypropylenschmelzen

Zusammenfassung An einer Anzahl von Polypropylenproben wurden die Grenzviskositäten [] und dieNewtonschen Schmelzviskositäten ₀ bei 190 °C gemessen; die meisten Proben wurden fraktioniert und die Molekulargewichtsverteilung festgestellt. Die Messung der Schmelzviskosität erfolgte in einem Extrusionsrheometer mit drei Düsen verschiedener Länge. Es wurden Endkorrekturen bestimmt und die Schubspannung entsprechend korrigiert. Für die-M-Beziehung ergibt sich: log ₀=3,69 log¯M _w –11,90.Proben mit sehrenger bzw. weiter Molekulargewichtsverteilung weichen von dieser Beziehung deutlich ab. Eine für die Molekulargewichtsverteilungsbreite besonders empfindliche Größe ist die Steigungskonstante (1/ vs.), die gleichzeitig ein Maß für den Grad des Nicht-Newtonschen Verhaltens der Schmelze darstellt, bzw. ₀ ; diese letzte Größe eignet sich ganz besonders zur Kennzeichnung der Verteilung sowohl für Proben mit besonders enger Verteilung (Fraktionen, Abbauprodukte, Luparen) als auch für den anderen Extremfall (Mischungen).Vorgetragen auf der Arbeitstagung der Sektion Rheologie des Vereins Österreichischer Chemiker am 28. September 1965 in Graz.Die Messungen und experimentellen Arbeiten wurden von FräuleinHeather Furley und HerrnHelmuth Lehner durchgeführt.     

Determination of the steady-state shear viscosity from measurements of the apparent viscosity for some common types of viscometers

Considering a number of model fluids, the relation between the (measurable) apparent viscosity _a and the (true) shear viscosity is studied for some commonly used viscometers, like capillary, slit, plate-plate and concentric cylinders (including the influence of the bottom of the cylinder), as well as for one laboratory type of viscometer. As long as is a purely monotonic function, a shift factor < 1 allows one to deduce from _a . Though in general variable, it frequently suffices for practical purposes to use a constant shift factor (the constant being characteristic of the type of viscometer used). This does not apply to dilute solutions or any fluids with two plateau values for . For plastic fluids, it is shown that Casson or Bingham behavior can — if valid at all — only describe the high shear stress limit of _a .     

On the Ellipticity of the Middle Surface of a Shell and its Application to the Asymptotic Analysis of ‘Membrane’ Shells

We consider a surface S = (), where ² is a bounded, connected, open set with a smooth boundary and : ³ is a smooth map; let () denote the components of the two-dimensional linearized strain tensor of S and let 0 with length 0 > 0. We assume the the norm ,|| ()||0, in the space V0() = { H¹() × H¹() × L²(); = 0 on 0 } is equivalent to the usual product norm on this space. We then establish that this assumption implies that the surface S is uniformly elliptic and that we necessarily have 0 = .     

Flow in porous media II: The governing equations for immiscible,two-phase flow

The Stokes flow of two immiscible fluids through a rigid porous medium is analyzed using the method of volume averaging. The volume-averaged momentum equations, in terms of averaged quantities and spatial deviations, are identical in form to that obtained for single phase flow; however, the solution of the closure problem gives rise to additional terms not found in the traditional treatment of two-phase flow. Qualitative arguments suggest that the nontraditional terms may be important when / is of order one, and order of magnitude analysis indicates that they may be significant in terms of the motion of a fluid at very low volume fractions. The theory contains features that could give rise to hysteresis effects, but in the present form it is restricted to static contact line phenomena.Roman Letters (, = , , and ) A interfacial area of the- interface contained within the macroscopic system, m² - A _e area of entrances and exits for the -phase contained within the macroscopic system, m² - A interfacial area of the- interface contained within the averaging volume, m² - A ^* interfacial area of the- interface contained within a unit cell, m² - A _e ^* area of entrances and exits for the-phase contained within a unit cell, m² - g gravity vector, m²/s - H mean curvature of the- interface, m^–1 - H area average of the mean curvature, m^–1 - H – H , deviation of the mean curvature, m^–1 - I unit tensor - K Darcy's law permeability tensor, m² - K permeability tensor for the-phase, m² - K viscous drag tensor for the-phase equation of motion - K viscous drag tensor for the-phase equation of motion - L characteristic length scale for volume averaged quantities, m - characteristic length scale for the-phase, m - n unit normal vector pointing from the-phase toward the-phase (n = –n ) - p _c p – P , capillary pressure, N/m² - p pressure in the-phase, N/m² - p intrinsic phase average pressure for the-phase, N/m² - p – p , spatial deviation of the pressure in the-phase, N/m² - r ₀ radius of the averaging volume, m - t time, s - v velocity vector for the-phase, m/s - v phase average velocity vector for the-phase, m/s - v intrinsic phase average velocity vector for the-phase, m/s - v – v , spatial deviation of the velocity vector for the-phase, m/s - V averaging volume, m³ - V volume of the-phase contained within the averaging volume, m³ Greek Letters V /V, volume fraction of the-phase - mass density of the-phase, kg/m³ - viscosity of the-phase, Nt/m² - surface tension of the- interface, N/m - viscous stress tensor for the-phase, N/m² - / kinematic viscosity, m²/s     

Fractal-time stochastic processes and dynamic functions of polymeric systems

Dynamic material functions of polymeric systems are calculated via a defect-diffusion model. The random motion of defects is modelled by a fractaltime stochastic process. It is shown that the dynamic functions of polymeric solutions can be approximated by the defect-diffusion process of the mixed type. The relaxation modulus of Kohlrausch type is obtained for a fractal-time defect-diffusion process, and it is shown that this modulus is capable of portraying the dynamic behavior of typical viscoelastic solutions.The Fourier transforms of the Kohlrausch function are calculated to obtain and. A three-parameter model for and is compared with the previous calculations. Experimental measurements for five polymer solutions are compared with model predictions. D rate of deformation tensor - G(t) mechanical relaxation modulus - H relaxation spectrum - I(t) flux of defects - P _n (s) probability of finding a walker ats aftern-steps - P generating function ofP _n (s) - s(t) fraction of surviving defects - , () gamma function (incomplete) - ₀ zero shear viscosity - ^* () complex viscosity - frequency - t _n n-th moment - F[] Fourier transform - f ^* (u) Laplace transform off(t) - , components of ^* - G _f, _f ^* fractional model - G ₃, ₃ ^* three parameter model - complex conjugate ofz - material time derivative ofD     

Comparison between uniaxial and biaxial elongational flow behavior of viscoelastic fluids as predicted by differential constitutive equations

Behavior of polymer melts in biaxial as well as uniaxial elongational flow is studied based on the predictions of three constitutive models (Leonov, Giesekus, and Larson) with single relaxation mode. Transient elongational viscosities in both flows are calculated for three constitutive models, and steady-state elongational viscosities are obtained as functions of strain rates for the Giesekus and the Larson models.Change of elongational flow behavior with adjustable parameter is investigated in each model. Steady-state viscosities _E and _B are obtained for the Leonov model only when the strain-hardening parameter is smaller than the critical value _cr determined in each flow. In this model, uniaxial elongational viscosity _E increases with increasing strain rate , while biaxial elongational viscosity _B decreases with increasing biaxial strain rate _B . The Giesekus model predictions depend on the anisotropy parameter . _E and _B increase with strain rates for small _B while they decrease for large . When is 0.5, _E in increasing, but _B is decreasing. The Larson model predicts strain-softening behavior for both flows when the chain-contraction parameter > 0.5. On the other hand, when is small, the steady-state viscosities of this model show distinct maximum around = _B = 1.0 with relaxation time . The maximum is more prominent in _E than in _B .     

Semi-empirical theory of the viscosity of moderately dilute polymer solutions

The viscosity of moderately dilute polymer solutions is formulated on the postulates that in this concentration region is governed by the domain volume per polymer segment and the noddle effect due to entangling chains. The former is treated semi-molecular theoretically, and the latter entirely phenomenologically. All the parameters involved in the theory can be estimated from appropriate dilute solution data as well as the asymptotic molecular-weight dependence of at different concentrations. It is shown that the theory describes almost quantitatively the experimental data obtained by Hamada and Adam and Delsanti for polystyrene in benzene and cyclohexane. Part of these data reveals the breakdown of the semidilute solution approximation used in the theory.     

Über den Einfluß der veränderlichen Viskosität auf die Stabilität der ebenen Kanalströmung

Zusammenfassung Der Einfluß einer veränderlichen Viskosität auf die Stabilität der ebenen Kanalströmung wird untersucht. Um den Effekt der Viskositätsänderung besonders hervorzuheben, wird ein Materialgesetz ohne Relaxationseigenschaften zugrundegelegt. Außerdem wird nur das Verhalten von ebenen Störungen untersucht. Unter der Ausnutzung der Verwandtschaft der Problemstellung mit dem newtonschen Fall können die Näherungsgleichungen vonC. C. Lin in modifizierter Form übernommen werden. Die Stabilität wird durch die Änderung des Grundprofils infolge der veränderlichen Viskosität und die differentielle Viskosität in der kritischen Schicht bestimmt.

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Summary The influence of shear rate dependent viscosity on the stability of plane channel flow is investigated. In order to demonstrate the effect of the viscosity variation a constitutive model without relaxation properties is choosen. Furthermore only perturbations in the plane of flow are investigated. Since the problem is similar to the newtonian case, the approximate equations ofC. C. Lin can be appropriately modified. The stability depends on the change of the basic profile due to shear rate dependent viscosity and on differential viscosity in the critical layer.

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Liste der wichtigsten Symbole A Dimensionslose Kennzahl: - b Stoffkonstante - h Halbe Kanalhöhe - Druckgradient - Re Reynoldszahl - Re _k Kritische Reynoldszahl - Re _k Kritische Reynoldszahl für ein newtonsches Fluid mit der Viskosität - u _g(y) Grundgeschwindigkeitsprofil - U _M Maximale Geschwindigkeit - Viskosität - Viskosität im zweiten newtonschen Bereich - _D Differentielle Viskosität - Stoffkonstante - _k Kritischer Druckgradient _k = –(dp/dx)_k - _k Kritischer Druckgradient für ein newtonsches Fluid mit der Viskosität - Dichte des Fluids Mit 8 Abbildungen     

Two-phase flow in heterogeneous porous media II: Numerical experiments for flow perpendicular to a stratified system

In this work, we make use of numerical experiments to explore our original theoretical analysis of two-phase flow in heterogeneous porous media (Quintard and Whitaker, 1988). The calculations were carried out with a two-region model of a stratified system, and the parameters were chosen be consistent with practical problems associated with groundwater flows and petroleum reservoir recovery processes. The comparison between theory (the large-scaled averaged equations) and experiment (numerical solution of the local volume averaged equations) has allowed us to identify conditions for which the quasi-static theory is acceptable and conditions for which a dynamic theory must be used. Byquasi-static we mean the following: (1) The local capillary pressure,everywhere in the averaging volume, can be set equal to the large-scale capillary pressure evaluated at the centroid of the averaging volume and (2) the large-scale capillary pressure is given by the difference between the large-scale pressures in the two immiscible phases, and is therefore independent of gravitational effects, flow effects and transient effects. Bydynamic, we simply mean a significant departure from the quasi-static condition, thus dynamic effects can be associated with gravitational effects, flow effects and transient effects. To be more precise about the quasi-static condition we need to refer to the relation between the local capillary pressure and the large-scale capillary pressure derived in Part I (Quintard and Whitaker, 1990). Herep _c ¦_y represents the local capillary pressure evaluated at a positiony relative to the centroid of the large-scale averaging volume, and {p _c }¦_x represents the large-scale capillary pressure evaluated at the centroid.In addition to{p _c } ^c being evaluated at the centroid, all averaged terms on the right-hand side of Equation (1) are evaluated at the centroid. We can now write the equations describing the quasi-static condition as , , This means that the fluids within an averaging volume are distributed according to the capillary pressure-saturation relationwith the capillary pressure held constant. It also means that the large-scale capillary pressure is devoid of any dynamic effects. Both of these conditions represent approximations (see Section 6 in Part I) and one of our main objectives in this paper is to learn something about the efficacy of these approximations. As a secondary objective we want to explore the influence of dynamic effects in terms of our original theory. In that development only the first four terms on the right hand side of Equation (1) appeared in the representation for the local capillary pressure. However, those terms will provide an indication of the influence of dynamic effects on the large-scale capillary pressure and the large-scale permeability tensor, and that information provides valuable guidance for future studies based on the theory presented in Part I.Roman Letters A scalar that maps {}*/t onto - A scalar that maps {}*/t onto - A interfacial area between the -region and the -region contained within, m² - A interfacial area between the -region and the -region contained within, m² - A interfacial area between the -region and the -region contained within, m² - a vector that maps ({}*/t) onto , m - a vector that maps ({}*/t) onto , m - b vector that maps ({p}– g) onto , m - b vector that maps ({p}– g) onto , m - B second order tensor that maps ({p}– g) onto , m² - B second order tensor that maps ({p}– g) onto , m² - c vector that maps ({}*/t) onto , m - c vector that maps ({}*/t) onto , m - C second order tensor that maps ({}*/t) onto , m² - C second order tensor that maps ({}*/t) onto . m² - D third order tensor that maps ( ) onto , m - D third order tensor that maps ( ) onto , m - D second order tensor that maps ( ) onto , m² - D second order tensor that maps ( ) onto , m² - E third order tensor that maps () onto , m - E third order tensor that maps () onto , m - E second order tensor that maps () onto - E second order tensor that maps () onto - p _c =(), capillary pressure relationship in the-region - p _c =(), capillary pressure relationship in the-region - g gravitational vector, m/s² - largest of either or - - - i unit base vector in thex-direction - I unit tensor - K local volume-averaged-phase permeability, m² - K local volume-averaged-phase permeability in the-region, m² - K local volume-averaged-phase permeability in the-region, m² - {K } large-scale intrinsic phase average permeability for the-phase, m² - K –{K }, large-scale spatial deviation for the-phase permeability, m² - K –{K }, large-scale spatial deviation for the-phase permeability in the-region, m² - K –{K }, large-scale spatial deviation for the-phase permeability in the-region, m² - K ^* large-scale permeability for the-phase, m² - L characteristic length associated with local volume-averaged quantities, m - characteristic length associated with large-scale averaged quantities, m - I _i i = 1, 2, 3, lattice vectors for a unit cell, m - l characteristic length associated with the-region, m - ; characteristic length associated with the-region, m - l _H characteristic length associated with a local heterogeneity, m - - n unit normal vector pointing from the-region toward the-region (n =–n ) - n unit normal vector pointing from the-region toward the-region (n =–n ) - p pressure in the-phase, N/m² - p local volume-averaged intrinsic phase average pressure in the-phase, N/m² - {p } large-scale intrinsic phase average pressure in the capillary region of the-phase, N/m² - p local volume-averaged intrinsic phase average pressure for the-phase in the-region, N/m² - p local volume-averaged intrinsic phase average pressure for the-phase in the-region, N/m² - p –{p }, large scale spatial deviation for the-phase pressure, N/m² - p –{p }, large scale spatial deviation for the-phase pressure in the-region, N/m² - p –{p }, large scale spatial deviation for the-phase pressure in the-region, N/m² - P _c p –{p }, capillary pressure, N/m² - {p_c}^c large-scale capillary pressure, N/m² - r ₀ radius of the local averaging volume, m - R ₀ radius of the large-scale averaging volume, m - r position vector, m - , m - S /, local volume-averaged saturation for the-phase - S ^* {}*{}*, large-scale average saturation for the-phaset time, s - t time, s - u , m - U , m² - v -phase velocity vector, m/s - v local volume-averaged phase average velocity for the-phase in the-region, m/s - v local volume-averaged phase average velocity for the-phase in the-region, m/s - {v } large-scale intrinsic phase average velocity for the-phase in the capillary region of the-phase, m/s - {v } large-scale phase average velocity for the-phase in the capillary region of the-phase, m/s - v –{v }, large-scale spatial deviation for the-phase velocity, m/s - v –{v }, large-scale spatial deviation for the-phase velocity in the-region, m/s - v –{v }, large-scale spatial deviation for the-phase velocity in the-region, m/s - V local averaging volume, m³ - V volume of the-phase in, m³ - V large-scale averaging volume, m³ - V capillary region for the-phase within, m³ - V capillary region for the-phase within, m³ - V _c intersection of m³ - V volume of the-region within, m³ - V volume of the-region within, m³ - V () capillary region for the-phase within the-region, m³ - V () capillary region for the-phase within the-region, m³ - V () , region in which the-phase is trapped at the irreducible saturation, m³ - y position vector relative to the centroid of the large-scale averaging volume, m Greek Letters local volume-averaged porosity - local volume-averaged volume fraction for the-phase - local volume-averaged volume fraction for the-phase in the-region - local volume-averaged volume fraction for the-phase in the-region - local volume-averaged volume fraction for the-phase in the-region (This is directly related to the irreducible saturation.) - {} large-scale intrinsic phase average volume fraction for the-phase - {} large-scale phase average volume fraction for the-phase - {}* large-scale spatial average volume fraction for the-phase - –{}, large-scale spatial deviation for the-phase volume fraction - –{}, large-scale spatial deviation for the-phase volume fraction in the-region - –{}, large-scale spatial deviation for the-phase volume fraction in the-region - a generic local volume-averaged quantity associated with the-phase - mass density of the-phase, kg/m³ - mass density of the-phase, kg/m³ - viscosity of the-phase, N s/m² - viscosity of the-phase, N s/m² - interfacial tension of the - phase system, N/m - , N/m - , volume fraction of the-phase capillary (active) region - , volume fraction of the-phase capillary (active) region - , volume fraction of the-region ( + =1) - , volume fraction of the-region ( + =1) - {p }– g, N/m³ - {p }– g, N/m³