STATISTIC MODELING OF THE CREEP BEHAVIOR OF METAL MATRIX COMPOSITES BASED ON FINITE ELEMENT ANALYSIS

ＩｎｔｒｏｄｕｃｔｉｏｎＴｈｅｃｒｅｅｐｂｅｈａｖｉｏｒｏｆｓｈｏｒｔｆｉｂｅｒｒｅｉｎｆｏｒｃｅＭｅｔａｌＭａｔｒｉｘＣｏｍｐｏｓｉｔｅｓ (ＭＭＣｓ)ｄｅｐｅｎｄｓｏｎｔｈｅｆｏｌｌｏｗｉｎｇｆａｃｔｏｒｓ,ｓｕｃｈａｓｔｈｅｃｒｅｅｐｐｒｏｐｅｒｔｙｏｆｔｈｅｍａｔｒｉｘ ,ｅｌａｓｔｉｃａｎｄｆｒａｃｔｕｒｅｓｐｒｏｐｅｒｔｉｅｓｏｆｔｈｅｆｉｂｅｒ,ｇｅｏｍｅｔｒｉｃｐａｒａｍｅｔｅｒｓｏｆｔｈｅｆｉｂｅｒｓ,ａｒｒａｎｇｅｍｅｎｔｏｆｔｈｅｆｉｂｅｒｓａｎｄｔｈｅｐｒｏｐｅｒｔｙｏｆｔｈｅｆ…     

THE TRANSIENT ELLIPTIC FLOW OF POWER-LAW FLUID IN FRACTAL POROUS MEDIA

1　ＴｈｅＦｌｏｗＭｏｄｅｌｏｆＰｏｗｅｒ＿ＬａｗＦｌｕｉｄｉｎＲａｄｉｃａｌＦｒａｃｔａｌＲｅｓｅｒｖｏｉｒＴｈｅｔｒａｎｓｉｅｎｔｆｌｏｗｏｆｐｏｗｅｒ＿ｌａｗｆｌｕｉｄｉｎｒａｄｉｃａｌｆｒａｃｔａｌｒｅｓｅｒｖｏｉｒｉｓｓｔｕｄｉｅｄｉｎＲｅｆ.[1 ] ,ａｎｄａｎａｌｙｔｉｃａｌｓｏｌｕｔｉｏｎｏｆＬａｐｌａｃｅｓｐａｃｅｉｓｄｅｒｉｖｅｄ .ＩｎＲｅｆ.[2 ] ,ｔｈｅｔｒａｎｓｉｅｎｔｅｌｌｉｐｔｉｃａｌｆｌｏｗｉｓｒｅｓｅａｒｃｈｅｄｏｎｍｏｄｅｌｏｆｅｘｐａｎｄｉｎｇｒｅｃｔａｎｇｌｅ .Ｔ…     

ANALYSIS OF THE LOCALIZATION OF DAMAGE AND THE COMPLETE STRESS-STRAIN RELATION FOR MESOSCOPIC HETEROGENEOUS ROCK UNDER UNIAXIAL TENSILE LOADING

The mechanical behavior of rock under uniaxial tensile loading is different from that of rock under compressive loads. A micromechanics-based model was proposed for mesoscopic heterogeneous brittle rock undergoing irreversible changes of their microscopic structures due to microcrack growth. The complete stress-strain relation including linear elasticity, nonlinear hardening, rapid stress drop and strain softening was obtained. The influence of all microcracks with different sizes and orientations were introduced into the constitutive relation by using the probability density function describing the distribution of orientations and the probability density function describing the distribution of sizes. The influence of Weibull distribution describing the distribution of orientations and Rayleigh function describing the distribution of sizes on the constitutive relation were researched. Theoretical predictions have shown to be consistent with the experimental results.     

Purely elastic interfacial instabilities in superposed flow of polymeric fluids

Purely elastic interfacial stability of superposed plane Poiseuille flow of polymeric liquids has been investigated utilizing both asymptotic and numerical techniques. It is shown that these instabilities are caused by an unfavorable jump in the first normal stress difference across the fluid interface. To determine the significance of these instabilities in finite experimental geometries, a comparison between the maximum growth rates of purely elastic instabilities with instabilities driven primarily by a viscosity or a combined viscosity and elasticity difference is made. Based on this comparison, it is shown that purely elastic interfacial instabilities can play a major role in superposed flow of polymeric liquids in finite experimental geometries.     

On some nearly viscometric flows of viscoelastic liquids

Superposition of oscillatory shear imposed from the boundary and through pressure gradient oscillations and simple shear is investigated. The integral fluid with fading memory shows flow enhancement effects due to the nonlinear structure. Closed-form expressions for the change in the mass transport rate are given at the lowest significant order in the perturbation algorithm. The elasticity of the liquid plays as important a role in determining the enhancement as does the shear dependent viscosity. Coupling of shear thinning and elasticity may produce sharp increases in the flow rate. The interaction of oscillatory shear components may generate a steady flow, either longitudinal or orthogonal, resulting in increases in flow rates akin to resonance, and due to frequency cancellation, even in the absence of a mean gradient. An algorithm to determine the constitutive functions of the integral fluid of order three is outlined.Nomenclature A _n Rivlin-Ericksen tensor of order . - A _k Non-oscillatory component of the first order linear viscoelastic oscillatory velocity field induced by the kth wave in the pressure gradient - d Half the gap between the plates - e _x, e _z Unit vectors in the longitudinal and orthogonal directions, respectively - G(s) Relaxation modulus - G History of the deformation - Stress response functional - I() Enhancement defined as the ratio of the frequency dependent part of the discharge to the frequencyindependent part of it at the third order - I ^*() Enhancement defined as the ratio of the increase in discharge due to oscillations to the total discharge without the oscillations - k Power index in the relaxation modulus G(s) - k _i ^–1 Relaxation times in the Maxwell representation of the quadratic shear relaxation modulus (s ₁, s ₂) - m _i ^–1, n _i ^–1 Relaxation times in the Maxwell representations of the constitutive functions ₁(s ₁,s ₂,s ₃) and ₄ (s ₁, s ₂,s ₃), respectively - P Constant longitudinal pressure gradient - p Pressure field - _mx ,⁽³⁾ _nz ,⁽³⁾ Mean volume transport rates at the third order in the longitudinal and orthogonal directions, respectively - ₀,⁽³⁾, ₁,⁽³⁾ Frequency independent and dependent volume transport rates, respectively, at the third order - s = t- Difference between present and past times t and      

Heat-transfer characteristics from a bundle of horizontal tubes immersed in aggregative fluidized bed

Experiments were performed to study the effect of air fluidization velocity, particle diameter, tube diameter, and pitch between tubes on heat-transfer coefficient for a bundle of horizontal tubes immersed in an aggregative fluidized bed. Not only horizontal but also vertical distributions of the heat-transfer coefficients within the bundle were also extensively determined. The heat-transfer coefficient and its maximum value were found to be dependent on the particle diameter, the air fluidization velocity, and the gap between the tubes in the bundle. The proposed correlation for the maximum heat-transfer coefficient was in good agreement with the present results.     

Beitrag zur Rohrströmung kompressibler Fluide mit Reibung und Wärmeübergang

Übersicht Die Strömung eines kompressiblen Fluids aus einem Druckkessel durch ein Rohr konstanten Kreisquerschnitts und mit konstanter Wandtemperatur, in dem Wandreibung wirksam ist, wird nach der Stromfadentheorie untersucht. Gegeben sind der Druck im Kessel und am Ende der Rohrleitung sowie die Temperatur der Rohrwand und im Kessel. Als Wärmeübergangshypothese wird die Reynolds-Analogie benutzt. Die Wandreibung wird durch die Rohrreibungszahl beschrieben. Die sich ergebende Differentialgleichung und das Eigenwertproblem für die Eintrittsmachzahl wird numerisch gelöst in Abhängigkeit von der dimensionslosen Rohrlänge für Austrittsmachzahlen 1. Eine analytische Näherungslösung für kleine Eintrittsmachzahlen und eine asymptotische Entwicklung für große Rohrlängen wird angegeben. Es zeigt sich, daß der Wärmeübergangsprozeß relativ schnell abgeschlossen ist und die End-Machzahl, der Druckverlustfaktor sowie das kritische Druckverhältnis vom Wärmeübergang fast unabhängig sind.

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A note on the viscous pipe flow of a compressible fluid with heat transfer

Summary The flow of a compressible fluid from a pressure reservoir through a pipe with constant circular cross-section and constant pipe-wall temperature has been investigated by means of one-dimensional theory with wall-friction taken into account. The initial stagnation pressure and temperature, the pipe wall temperature and the pipe exit pressure are assumed to be given. The heat transfer is assumed to follow the Reynolds analogy, while wall friction is taken into account by the pipe friction coefficient. The resulting differential equation and the corresponding eigenvalue problem for the inlet Mach number have been solved numerically as function of the dimensionless pipe-length for exit Mach numbers 1. An analytic approximation for small pipe inlet Mach numbers and an asymptotic expansion for large pipe-lengths have been derived. It is found that the heat transfer is restricted to a relatively small distance past the inlet. The final Mach number, the pressure loss factor as well as the critical pressure ratio is approximately independent of any heat transfer.