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Viscosity power loss

Wide range of viscosity ia commercial petroleum oils is illustrated by the representative types listed ia Table 3. Despite this range, the largest proportion of oils are ia the 25-75 mm /s at 40°C viscosity range. Oils ia this range combine generally adequate hydrodynamic load capacity with low power loss, low volatiUty, and satisfactory low temperature properties. [Pg.239]

Viscosity Glassifications. The general ISO iatemational viscosity classification system for iadustrial oils is given ia Table 4 from ASTM D2422 (American National Standard Z11.232). For high speed machines, ISO viscosity-grade 32 turbiae and hydrauHc oils are a common choice. ISO grades 68 and 100 are appHed for more load capacity ia slower speed machines where power loss and temperature rise are less of a question. [Pg.239]

At low frequencies when power losses are low these values are also low but they increase when such frequencies are reached that the dipoles cannot keep in phase. After passing through a peak at some characteristic frequency they fall in value as the frequency further increases. This is because at such high frequencies there is no time for substantial dipole movement and so the power losses are reduced. Because of the dependence of the dipole movement on the internal viscosity, the power factor like the dielectric constant, is strongly dependent on temperature. [Pg.114]

It Is widely thought that the cam and follower contact operates with a degree of surface Interaction for virtually the whole of Its cycle. As an Initial step towards the understanding of surface topography Influences, a rigid surface model for the mixed lubrication of a cam and follower Is developed In this paper. Results are presented to demonstrate the effect of surface roughness and Its distribution upon nominal film thickness, the load carried by the asperities and power loss. The proportion of the total load carried by the asperities and the proportion of power loss associated with asperity contact are detailed. The Influence of lubricant viscosity and camshaft speed upon nominal film thickness during the cycle are also discussed. [Pg.599]

Viscosity. Influences the size of the atomized droplets during injection. Improper viscosity will lead to detonation, power loss, excessive smoke, and unnecessary wear on the injector system. [Pg.998]

Both the shaft power and power losses increase with increasing rotor speed, larger flow rate, higher viscosity, and smaller shear gap. [Pg.481]

The most commonly utilised and versatile lubricants are mineral oils. Viscosity is the main oil characteristic. The effect of oil viscosity grade on bearing operating limits was considered in [7]. From the point of view of minimal power loss and pad temperature thinner oils are recommended at high speeds. Thicker ones are usually used at low speeds to avoid too thin oil films. [Pg.387]

Reply bv the Author The vast majority of the frictional power loss generated by the piston ring pack is viscosity related. As Dr. Taylor quite... [Pg.904]

Power for each Hquid and the soHd phase must be added to get Pp. P, the soHds process power, = T -AN for scroU decanters, where = conveyor torque and AN = differential speed between bowl and conveyor. Pp is the friction power, ie, loss in bearings, seals, gears, belts, and fluid couplings. P, the windage power, = K and fi = viscosity of surrounding gas p = density of gas D = rotor outside diameter N = rpm and K = shape... [Pg.403]

The nature of the liquid to be pumped. For a given throughput, the viscosity largely determines the friction losses and hence the power required. The corrosive nature will determine the material of construction both for the pump and the packing. With suspensions, the clearances in the pump must be large compared with the size of the particles. [Pg.315]

Corresponding expressions for the friction loss in laminar and turbulent flow for non-Newtonian fluids in pipes, for the two simplest (two-parameter) models—the power law and Bingham plastic—can be evaluated in a similar manner. The power law model is very popular for representing the viscosity of a wide variety of non-Newtonian fluids because of its simplicity and versatility. However, extreme care should be exercised in its application, because any application involving extrapolation beyond the range of shear stress (or shear rate) represented by the data used to determine the model parameters can lead to misleading or erroneous results. [Pg.164]

At low frequencies the loss modulus is linear in frequency and the storage modulus is quadratic for both models. As the frequency exceeds the reciprocal of the relaxation time ii the Rouse model approaches a square root dependence on frequency. The Zimm model varies as the 2/3rd power in frequency. At high frequencies there is some experimental evidence that suggests the storage modulus reaches a plateau value. The loss modulus has a linear dependence on frequency with a slope controlled by the solvent viscosity. Hearst and Tschoegl32 have both illustrated how a parameter h can be introduced into a bead spring... [Pg.189]

DILUENT. (I) An ingredient used to reduce the concentration of an active material to achieve a desirable and beneficial effect. Examples are combination of diatomaceous earth with nitroglycerin to term the much less shock-sensitive dynamite addition of sand to cement mixes to improve workability with no serious loss of strength addition of an organic liquid having no solvent power to a paint or lacquer to reduce viscosity and achieve suitable application properties. [Pg.495]


See other pages where Viscosity power loss is mentioned: [Pg.234]    [Pg.69]    [Pg.161]    [Pg.124]    [Pg.69]    [Pg.161]    [Pg.17]    [Pg.221]    [Pg.239]    [Pg.151]    [Pg.63]    [Pg.584]    [Pg.864]    [Pg.333]    [Pg.428]    [Pg.221]    [Pg.250]    [Pg.93]    [Pg.9]    [Pg.37]    [Pg.387]    [Pg.350]    [Pg.201]    [Pg.201]    [Pg.188]    [Pg.214]    [Pg.443]    [Pg.507]    [Pg.403]    [Pg.78]    [Pg.63]    [Pg.30]    [Pg.443]    [Pg.495]    [Pg.169]   
See also in sourсe #XX -- [ Pg.170 ]




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