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Primary properties density

In Chapter 16, we studied the so-called primary properties, which I defined as those that could be obtained by direct calculation from the electron density (or equivalently the wavefunction). We also touched on derivative or gradient properties. It is now time to mm our attention to those properties that measure the response of a system to an external field. In the language of Boys and Cook, these are the induced properties. [Pg.282]

For laminar flow, the characteristic time of the fluid phase Tf can be deflned as the ratio between a characteristic velocity Uf and a characteristic dimension L. For example, in the case of channel flows confined within two parallel plates, L can be taken equal to the distance between the plates, whereas Uf can be the friction velocity. Another common choice is to base this calculation on the viscous scale, by dividing the kinematic viscosity of the fluid phase by the friction velocity squared. For turbulent flow, Tf is usually assumed to be the Kolmogorov time scale in the fluid phase. The dusty-gas model can be applied only when the particle relaxation time tends to zero (i.e. Stp 1). Under these conditions, Eq. (5.105) yields fluid flow. This typically happens when particles are very small and/or the continuous phase is highly viscous and/or the disperse-to-primary-phase density ratio is very small. The dusty-gas model assumes that there is only one particle velocity field, which is identical to that of the fluid. With this approach, preferential accumulation and segregation effects are clearly not predicted since particles are transported as scalars in the continuous phase. If the system is very dilute (one-way coupling), the properties of the continuous phase (i.e. density and viscosity) are assumed to be equal to those of the fluid. If the solid-particle concentration starts to have an influence on the fluid phase (two-way coupling), a modified density and viscosity for the continuous phase are generally introduced in Eq. (4.92). [Pg.179]

Techniques for isolating myelin from the peripheral and central nervous systems exist and usually include homogenization of tissue in isotonic sucrose solutions followed by discontinuous density centrifugation. Because of its high lipid content, myelin has an intrinsically low specific gravity and forms large vesicles in aqueous solutions. The large vesicular size and low density are the two primary properties of myelin that are utilized for its isolation. [Pg.106]

The primary properties of interest are, compressibility factor, relative density (or more specifically relative molar mass) and heating value. In the following discussion, we examine definitions, misconceptions, recommended calculation procedures, shortcut approximations and sources of imcertainty. [Pg.6]

In latter years polyurethane elastomers have tended to be used due to their ability to be processed as liquids examples are the RIM process, sprayable and spreadable non-solvent coatings. Also polyurethane elastomers are now widely used in automobile floor mats of various types where bulk and high density are the primary properties needed to give sound absorption and reduced in cab noise levels such products are... [Pg.390]

Particle characterization, i.e. the description of the primary properties of particles in a particulate system, underlies all work in particle technology. Primary particle properties such as the particle size distribution, particle shape, density, surface properties and others, together with the primary properties of the liquid (viscosity and density) and also with the concentration and the state of dispersion, govern the other, secondary properties such as the settling velocities of the particles, the permeability of a bed or the specific resistance of a filter cake. Knowledge of these properties is vital in the design and operation of equipment for solid-liquid separation. [Pg.30]

In this article, we review the historical development of steam tables and then describe the current international standards as maintained by the International Association forthe Properties of Waterand Steam (lAPWS). While the primary focus of steam tables (and therefore of this article) is thermodynamic properties (density, enthalpy, entropy, etc.), other properties (such as viscosity, thermal conductivity, and dielectric constant) are also of some importance and will be mentioned briefly. [Pg.306]

Part III of the book discusses different properties of fibers. Fiber properties ean be classified into primaiy and secondary properties. Primary properties are those that fibers must possess so they can be converted into useful products. Examples of primary properties are aspect ratio, strength, flexibility, cohesiveness, and uniformity. Secondary properties are those that are desirable and can improve consumer satisfaction with the end-products made from the fibers. Secondary properties include, but are not hmited to physical shape, density, modulus, elongation, elastic recovery, resilience, thermal properties, electrical properties, color and optical properties, moisture regain, resistance to chemical and environmental conditions, resistance to biological organisms, and resistance to insects. Chapter 14 provides an introduction to these primary and secondary properties. [Pg.4]

The products could be classified as a function of various criteria physical properties (in particular, volatility), the way they are created (primary distillation or conversion). Nevertheless, the classification most relevant to this discussion is linked to the end product use LPG, premium gasoline, kerosene and diesel oil, medium and heavy fuels, specialty products like solvents, lubricants, and asphalts. Indeed, the product specifications are generally related to the end use. Traditionally, they have to do with specific properties octane number for premium gasoline, cetane number for diesel oil as well as overall physical properties such as density, distillation curves and viscosity. [Pg.483]

Oxidizers. The characteristics of the oxidizer affect the baUistic and mechanical properties of a composite propellant as well as the processibihty. Oxidizers are selected to provide the best combination of available oxygen, high density, low heat of formation, and maximum gas volume in reaction with binders. Increases in oxidizer content increase the density, the adiabatic flame temperature, and the specific impulse of a propellant up to a maximum. The most commonly used inorganic oxidizer in both composite and nitroceUulose-based rocket propellant is ammonium perchlorate. The primary combustion products of an ammonium perchlorate propellant and a polymeric binder containing C, H, and O are CO2, H2, O2, and HCl. Ammonium nitrate has been used in slow burning propellants, and where a smokeless exhaust is requited. Nitramines such as RDX and HMX have also been used where maximum energy is essential. [Pg.39]

Specific gravity is the most critical of the characteristics in Table 3. It is governed by ash content of the material, is the primary deterrninant of bulk density, along with particle size and shape, and is related to specific heat and other thermal properties. Specific gravity governs the porosity or fractional void volume of the waste material, ie. [Pg.53]

Each isomer has its individual set of physical and chemical properties however, these properties are similar (Table 6). The fundamental chemical reactions for pentanes are sulfonation to form sulfonic acids, chlorination to form chlorides, nitration to form nitropentanes, oxidation to form various compounds, and cracking to form free radicals. Many of these reactions are used to produce intermediates for the manufacture of industrial chemicals. Generally the reactivity increases from a primary to a secondary to a tertiary hydrogen (37). Other properties available but not Hsted are given in equations for heat capacity and viscosity (34), and saturated Hquid density (36). [Pg.403]


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