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Yield Taylor factor

But we want the tensile yield strength, A tensile stress a creates a shear stress in the material that has a maximum value of t = a/2. (We show this in Chapter 11 where we resolve the tensile stress onto planes within the material.) To calculate cr from t,, we combine the Taylor factor with the resolution factor to give... [Pg.109]

This equation is similar to the HP relation Eq. (4.18a) and, in order to make it equivalent in terms of the yield stress, ffy, under tension, Ty is multiplied by the Taylor factor, M, to obtain Eq. (4.18a) as ... [Pg.337]

If we take these effects into account, the Schmid factor has to be replaced in a polycrystalline material by another number, the Taylor factor M. For a face-centred cubic material, M takes a value of 3.1 [34]. The relation between the critical resolved shear stress Tcrit and the yield strength measured in uniaxial tension ap thus is... [Pg.183]

This value of the Taylor factor has also been confirmed experimentally. Throughout section 6.4, we will use the Taylor factor to calculate the influence of strengthening mechanisms, which affect the critical shear stress, on the uniaxially measured yield strength. [Pg.183]

Use the von Mises yield criterion to decide whether the material yields Can you decide which of the two results is correct Justify your answer In experiments on single crystals, the yield strength of the slip systems was determined as Tc- i = 60 MPa. Use the von Mises yield criterion to check whether a significant amount of slip systems in the polycrystal is activated at the stress value given The Taylor factor is M = 3.1. Calculate the stress deviator a for the given stress state ... [Pg.411]

The described method can generate a first-order backward or a first-order forward difference scheme depending whether 0 = 0 or 0 = 1 is used. For 9 = 0.5, the method yields a second order accurate central difference scheme, however, other considerations such as the stability of numerical calculations should be taken into account. Stability analysis for this class of time stepping methods can only be carried out for simple cases where the coefficient matrix in Equation (2.106) is symmetric and positive-definite (i.e. self-adjoint problems Zienkiewicz and Taylor, 1994). Obviously, this will not be the case in most types of engineering flow problems. In practice, therefore, selection of appropriate values of 6 and time increment At is usually based on trial and error. Factors such as the nature of non-linearity of physical parameters and the type of elements used in the spatial discretization usually influence the selection of the values of 0 and At in a problem. [Pg.66]

Hawke, J.C., Taylor, M.W. 1995. Influence of nutritional factors on the yield, composition and physical properties of milk fat. In, Advanced Dairy Chemistry. 2 Lipids. 2nd edn (P.F. Fox, ed.), pp. 37-88, Chapman and Hall, London. [Pg.37]

We have already discussed the basics of dispersion, noting how decreased dispersion improves resolution and sensitivity in separation applications [61], and also yields improved dynamics for concentration and purification applications [4], However, there are some key differences to consider when comparing focusing techniques such as TGF with other techniques. We describe the basics of TGF theory, implementation details, and the modifications to Taylor dispersion required for TGF. Finally, we present tips for empirical optimization of TGF preconcentration factors and resolution. [Pg.1103]

Apart from the factors mentioned above formation of inhibitors during pretreatment, for example, furfural and 5-hydroxymethylfurfural (HMF), carboxylic acids, ketones, phenolics, and aldehydes, affects the subsequent processes. The chemistry and the effect of these inhibitors are well studied (Taylor et al 2012). Effective pretreatment methods to reduce the inhibitor concentration, and to improve the sugar yields, are presently being researched. [Pg.53]

Iftheprobability of decay (q= 1 — p) is small (e.g., in the given case it is onlyO.l), then the factor ln(l/p) can be expanded into a Taylor series, yielding a probabilistic interpretation for the decay constant 1 ... [Pg.425]

Next, the factor e is expanded in a Taylor series and the integration carried out term by term the first two terms yield the approximation... [Pg.716]

SC-CO2 promises shorter extraction times, no chemical residue and a safer operating environment as a replacement for -hexane extraction (Sahena et al., 2009). Several studies have shown that oil yields using SC-CO2 are on par with solvent extraction and this is a crucial factor if SC-CO2 is to be competitive economically with solvent extraction (Taylor et al., 1993 Perrut, 2000 Bozan and Temelli, 2002 Bravi et al., 2002 Lu et al., 2007 Ixtaina et al., 2010 Li et al., 2010). The SC-CO2 extractions which were reviewed earlier were conducted using temperature, pressure and solvent flow rates which are readily attainable in commercial-scale systems. Many studies have been conducted on pilot-scale equipment and the extraction of valuable materials from solid substrates by means of SC-CO2 has been carried out on a commercial scale for more than 25 years (Brunner, 2005). [Pg.161]

In order to avoid electron avalanches which are induced by holes accelerated into the opposite direction and which would result in additional background noise, the amplification factor for holes must be kept considerably smaller than for electrons. This is achieved by a specially taylored layer structure which yields a sawtooth-like graded band-gap dependence AEg(x) in the field direction x (Fig.4.89c,d). In an external field this structure results in an amplification factor M which is 50 t 100 times larger for electrons than for holes [4.110]. [Pg.198]


See other pages where Yield Taylor factor is mentioned: [Pg.109]    [Pg.110]    [Pg.62]    [Pg.157]    [Pg.80]    [Pg.187]    [Pg.97]    [Pg.245]    [Pg.204]    [Pg.33]    [Pg.175]    [Pg.293]    [Pg.151]    [Pg.123]    [Pg.61]    [Pg.147]    [Pg.22]    [Pg.1289]   


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Yield factor

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