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Kinematics cylindrical

Returning to Staudinger s derivation, it must be revised on two grounds. First the kinematics of motion is three rather than two-dimensional and the hydrodynamic volume spherical rather than cylindrical, i.e. 3. The detailed calculation for thin ellipsoidal particles (13) shows an approximate proportionality of the intrinsic viscosity with M1 7, a considerable difference from eq. (1) for large M. [Pg.49]

Hydrazine has been studied extensively for use in monopropellant thrusters for space flights of long duration. Thrusters are used or altitude control of communication satellites. Here the decomposition of hydrazine over a packed bed of alumina-supported iridium catalyst is of interest. " In a proposed study, a 2% hydrazine in 98% helium mixture is to be passed over a packed bed of cylindrical particles 0.25 cm in diameter and 0.5 cm in length at a gas-phase velocity of 15m/s and a temperature of 750 K. The kinematic viscosity of helium at this temperature is 4.5 X 10 nF/s. The hydrazine decomposition reaction is believed to be externally mass transfer-limited under these conditions. If the packed bed is 0.05 m in length, what conversion can be expected Assume isothermal operation. [Pg.711]

It turns out that two fictitious forces occur in the momentum equation when written in cylindrical coordinates. The term pmeVrlr is an effective force in the 0-direction when there is flow in both the r- and 0-directions. The term pvg jr gives the effective force in the r-direction resulting from fluid motion in the 0-direction. These terms do not represent the familiar Coriolis and centrifugal forces due to the earth s rotation. Instead, they arise automatically on transformation of the momentum equations from Cartesian to cylindrical coordinates and are thus not added on physical grounds (kinematics). Nevertheless, the pv /r term is sometimes referred to as a Coriolis force and the pv gjr term is often called a centrifugal force. It is thus important to distinguish between the different types of fictitious forces. [Pg.724]

The DE (3-95) is identical in form to the familiar heat equation for radial conduction of heat in a circular cylindrical geometry. Thus we see that the evolution in time of the steady Poiseuille velocity profile is completely analogous to the conduction of heat starting with an initial parabolic temperature profile -(1 - r2)/4. In our problem, the final steady velocity profile is established by diffusion of momentum from the wall of the tube so that the initial profile for w eventually evolves to the asymptotic value uT - 0 as 1 oo. The characteristic time scale for any diffusion process (whether it is molecular diffusion, heat conduction, or the present process) is (f y cli fl iisivity ), where tc is the characteristic distance over which diffusion occurs. In the present process, tc = R and the kinematic viscosity v plays the role of the diffusivity so that... [Pg.137]

For the impeller used in these experiment, with cylindrical arms, C d = 1 for Re = OOrd/v > 400 where V is the kinematic viscosity. Averaging the power over the mass occupied by the impeller and substituting Cd = 1 results in ... [Pg.338]

External cylindrical lapping is used to process external surfaces of cylindrical parts. Therefore, the workpieces are moxmted radially on a workpiece holder on a two-face machine, whereby the parts scroll with an eccentric motion between the lapping disks. This process is used to reach very high shape precision, required, for instance, for jet needles in injection pumps. Cylindrical lapping of drilled holes is realized with cylindrical bushes, which describe rotating and lifting movements. Because of this kinematic, high surface qualities are reached, which are unable to be accomplished by other processes (Paulmann 1991). [Pg.735]

Cylindrical Coordinate Robots One of the earliest industrial robots belongs to the cylindrical coordinate robot class. Its kinematic structure is shown in Fig. lb. The arm consists of two orthogonal linear links placed on a rotating base. In comparison to Cartesian robots, this configuration offers a much larger work volume relative to the mechanical structure of the arm. The control system needed for linear path control is slightly more complex than for the Cartesian robots (Fig. 2). [Pg.1069]

The present research deals with a kinematical model of the DSG operation that, innovatively, accoimts for the cylindrical workpiece rotation inside the accommodation slot into the carrier. Trajectories for representative points located on the end surfaces of the workpieces are simulated. Theoretical conclusions on surface finish of the groimd components and on wear of active surface of the wheel were drawn. [Pg.264]

Ford viscosity cups n. A series of three cylindrical cups with conical bottoms, differing only in the diameters of the orifices at the apexes of the cones, each cup having a capacity of about 100 ml. From the time or efflux, the sample volume and the orifice diameter, the kinematic viscosity of a liquid may be estimated. ASTM test D 1200 (Section 06.01) describes the Ford cup procedures to be used with paints and varnishes. [Pg.431]

Feng has used a general treatment of Taylor-Melcher for stable part of electrospinning jets by one dimensional equations for mass, charge, and momentum. In this model a cylindrical fluid element is used to show electrospinning jet kinematic measurements [10]. [Pg.197]

Rotating Figure 7.102 screw j. g cylindrical system in two kinematic conditions... [Pg.413]

The centrifugal flows considered in this chapter are those dominated by rotatioa The azimuthal component of the velocity is preponderant, that is, Ur ue and Uz Ue in the cylindrical coordinate system. In such a configuration, the flow tends to become two-dimensional in a plane perpendicular to the Oz axis. The Ur and Ue components of the velocity are quasi-independent from coordinate z. The proof of this property goes beyond the scope of this chapter. Our goal is to describe the centrifugation of solid particles in a rotating flow. We simply choose to consider steady-state axisymmetric fluid flows, whose velocity and pressure fields possess the following kinematic characteristics ... [Pg.363]

Other elements of the model are the linear main spring (ks), the damper (c) and the linear translational (Kix, Kiy, Kiz, K6x, Key, Kez, Ktx, K y, K z) and torsional (Tix, Tiy, Tiz, Tex, Tey, Tez, Ttx, T y, T z) stiffness parameters of the rubber bushings that attach the suspension to the car body. These stiffness values are listed in Table 3. The model also includes a spherical joint, a slider joint and two cylindrical joints which apply the kinematic constraints of the suspension design. The end of travel snubbers were not modeled in this study. [Pg.220]

Figure 2.1 shows a schematic diagram of the experimental apparatus. The cylindrical vessel made of stainless steel had an inner diameter D of 20.4 cm and a height H of 30.0 cm. Wood s metal (commercial name U-alloy 70, melting temperature 70°C) was melted in it to a depth, //l, of 15.0cm. The bath temperature was kept at 105 1°C using a thermo-controller. The physical properties of the molten Wood s metal are as follows density ps = 9.56 g/cm, kinematic viscosity Vs = 0.341 mm /s, and surface tension a = 460mN/m. [Pg.20]

In the previous expression,/and Xe indicate the jet cross-sectional area (ni ) and longitudinal length, respectively, /Xe corresponding therefore to the volume D is the vapor diffusion coefficient in air Re is the Reynolds number relevant for a cylindrical object moving in air along the direction of its longitudinal axis with air kinematic viscosity, given by the air... [Pg.119]


See other pages where Kinematics cylindrical is mentioned: [Pg.245]    [Pg.616]    [Pg.343]    [Pg.210]    [Pg.426]    [Pg.13]    [Pg.143]    [Pg.405]    [Pg.786]    [Pg.239]    [Pg.240]    [Pg.215]    [Pg.571]    [Pg.571]    [Pg.735]    [Pg.1130]    [Pg.15]    [Pg.415]    [Pg.53]    [Pg.497]    [Pg.16]    [Pg.258]    [Pg.104]    [Pg.199]    [Pg.430]    [Pg.3760]   
See also in sourсe #XX -- [ Pg.104 ]




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