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Material estimated effective properties

A large number of mathematic functions exist for the characterization of the effective properties of a material mixture composed of different states, in terms of only their properties and volume fractions. Some can give determinate values for the estimated effective properties others may suggest a range through upper and lower bounds. A common understanding is that the rule of mixture and the inverse rule of mixture define the upper and lower bounds of the estimated effective properties. [Pg.45]

It is possible, however, to estimate effects on fire hazard in a particular scenario by simpler means. In some cases, an adequate choice of fire properties can be made. Then, the combination of test results into a matrix form, or into a single parameter, can indicate, even if only semi-quantitatively, the effect of varying a particular material or fire protection measure on fire hazard. [Pg.474]

The Maxwell model can also guide the selection of a proper polymer material for a selected zeolite at a given volume fraction for a target separation. For most cases, however, the Maxwell model cannot be applied to guide the selection of polymer or zeolite materials for making new mixed-matrix membranes due to the lack of permeabihty and selectivity information for most of the pure zeolite materials. In addition, although this Maxwell model is well-understood and accepted as a simple and effective tool for estimating mixed-matrix membrane properties, sometimes it needs to be modified to estimate the properties of some non-ideal mixed-matrix membranes. [Pg.336]

From these equations, the thermal stress profile through the thickness of the multi-layered material with a compositional profile can be calculated. If E and aA T vary continuously with z, o is continuous too. Because, the effective properties change as functions of the position in an FGM material, it is necessary to estimate the local composite properties as functions of... [Pg.586]

Kinetic theory was formulated to model the conversion degree of a material from one state to another. At each temperature, a FRP material can be considered as a mixture of materials in different states, with changing mechanical properties. The content of each state varies with temperature, thus the composite material shows temperature-dependent properties. If the quantity of material in each state is known and a probabilistic distribution function accounting the contribution from each material state to the effective properties of the mixture is available, the mechanical properties of the mixture can be estimated over the whole temperature range. [Pg.36]

This concept is applied in Chapters 4 and 5 that describe the temperature-dependent thermophysical and mechanical properties of FRP composite materials subjected to elevated temperature and fire. In Chapter 3, however, the estimation of the effective properties of a material mixture through a distribution function of its individual components (in different material states) is introduced first. [Pg.36]

A fundamental way is to interpret this problem from a probabilistic point of view. It is understandable that, for the state i with the mechanical property P, the probability of finding the value P at some point x within the unit volume is equal to its volume fraction Vj, this volume fraction therefore reflects the contribution of the individual mechanical property Pj to the effective mechanical property of the mixture. In this chapter, the volume fraction of each material state wiU be first estimated based on the results from Chapter 2. Different probabihstic distribution functions will then be introduced in Section 3.3, and the resulting estimation of effective properties will be presented in Section 3.4. [Pg.39]

Because an FRP composite material passes through different states when subjected to elevated temperature and fire, it may be considered to be a mixture of materials in different states at a certain time and temperature. To estimate the effective properties of a mixture material as a function of the properties and volume fractions of its individual states they have been intensively investigated for a long time. Because of the complexity of this problem, a statistical point of view may be helpful, that is, the probabihty of the property of a material state to be observed is represented by its volume fraction. The volume fractions of the materials in... [Pg.44]

Table 1 demonstrates the elFeet of OHm x on gel time (tgei) for PUs based on individual polyols with/= 2, 3 and 5.5. Both 1,4-dihydroxybutane (1,4-DHB) and polypropylene glycol (PPG) are linem diols (f = 2), however, of different backbone length and OHi dex (Table 1). Consequently, when cmed imder the same conditions (e.g., at 115 °C), their respeetive gel times were foimd to be drastically different 10 s vs. 680 s. The role of the backbone length was also evident in the distinct physical properties of these materials, estimated via Shore D hardness H) 87 vs. 53. A similm effect of the OHi dex on the cming kinetics and physical property was also observed for pairs of f= 3 polypropylene-oxide based polyether and /= 5.5 sucrose-based polyols (Table 1). Table 1 demonstrates the elFeet of OHm x on gel time (tgei) for PUs based on individual polyols with/= 2, 3 and 5.5. Both 1,4-dihydroxybutane (1,4-DHB) and polypropylene glycol (PPG) are linem diols (f = 2), however, of different backbone length and OHi dex (Table 1). Consequently, when cmed imder the same conditions (e.g., at 115 °C), their respeetive gel times were foimd to be drastically different 10 s vs. 680 s. The role of the backbone length was also evident in the distinct physical properties of these materials, estimated via Shore D hardness H) 87 vs. 53. A similm effect of the OHi dex on the cming kinetics and physical property was also observed for pairs of f= 3 polypropylene-oxide based polyether and /= 5.5 sucrose-based polyols (Table 1).
It is assumed that process conditions and physical properties are known and the following are known or specified tube outside diameter D, tube geometrical arrangement (unit cell), shell inside diameter D shell outer tube limit baffle cut 4, baffle spacing and number of sealing strips N,. The effective tube length between tube sheets L may be either specified or calculated after the heat-transfer coefficient has been determined. If additional specific information (e.g., tube-baffle clearance) is available, the exact values (instead of estimates) of certain parameters may be used in the calculation with some improvement in accuracy. To complete the rating, it is necessary to know also the tube material and wall thickness or inside diameter. [Pg.1037]

Polyethylene s simplicity of structure has made it one of the most thoroughly studied polymeric materials. With an estimated demand of close to 109 billion pounds in 2000 of the homopolymer and various copolymers of polyethylene,24 it is by far the world s highest volume synthetic macromolecule. Therefore, it is still pertinent to study its structure-property relationships, thermal behavior, morphology, and effects of adding branches and functional groups to the polymer backbone. [Pg.445]


See other pages where Material estimated effective properties is mentioned: [Pg.43]    [Pg.86]    [Pg.30]    [Pg.185]    [Pg.5]    [Pg.51]    [Pg.2038]    [Pg.349]    [Pg.5]    [Pg.181]    [Pg.490]    [Pg.690]    [Pg.7281]    [Pg.7334]    [Pg.264]    [Pg.215]    [Pg.257]    [Pg.172]    [Pg.191]    [Pg.19]    [Pg.85]    [Pg.520]    [Pg.507]    [Pg.191]    [Pg.357]    [Pg.426]    [Pg.270]    [Pg.163]    [Pg.314]    [Pg.563]    [Pg.66]    [Pg.484]    [Pg.97]    [Pg.98]    [Pg.11]    [Pg.81]    [Pg.156]    [Pg.347]   
See also in sourсe #XX -- [ Pg.44 ]




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