Acceleration centrifugal

Equation 12 shows that 2 can be expressed as the product of a mean sedimentation area (2 7Z r l) and the G level (co r /s), and therefore reflects the increased sedimentation rate expected through a defined area having centrifugal acceleration instead of gravity. 

Centripetal and Centrifugal Acceleration A centripetal body force is required to sustain a body of mass moving along a curve tra-jec tory. The force acts perpendicular to the direction of motion and is directed radially inward. The centripetal acceleration, which follows the same direction as the force, is given by the kinematic relationship ... 

G-Level Centrifugal acceleration G is measured in multiples of earth gravity g ... 

Vortex formation is a condition that arises from centrifugal acceleration acting on gravitational acceleration. The circular motion of the entire contents of the tank predominates over the flow of the liquid from the impeller. Flow orientation thus is important not only in cases of noticeable vortex formation, but... 

Cyclone collectors are popularly used both for particle removal and for particle sampling (Fig. 13.1). The separation process of a cyclone relies on the centrifugal accelerations that are produced when particle-laden fluid experi-... 

A widely used type of dust-collection equipment is the cyclone separator. A cyclone is essentially a settling chamber in which gravitational acceleration is replaced by centrifugal acceleration. Dust-laden air or gas enters a cylindrical or conical chamber tangentially at one or more points and leaves through a central opening. The dust particles, by virtue of their inertia, tend to move toward the outside separator wall from where they are... 

Sl is the laminar flame speed g the centrifugal acceleration k the thermal diffusivity of the mixture... 

After detachment of the flame from the wall and reduction of its width, three zones develop in the vessel parallel to each other a flame and burned gas zone and two zones (adjacent to the sidewalls), where no flame is present and where the gas temperatures are lower than behind the flame. All this happens in a field of very high centrifugal acceleration, which induces a free convection movement of the flame and the product zone behind it toward the... 

After detachment of the flame from the walls, the narrow ever-diminishing hot product zone behind the flame moves owing to the free convection in the centrifugal acceleration field toward the axis of rotation, with a speed scaling with circumferential velocity at the flame location, which reduces the observed flame speed to very low values, and in some cases negative ones. 

In Chapter 6.4, J. Chomiak and J. Jarosinski discuss the mechanism of flame propagation and quenching in a rofating cylindrical vessel. They explain the observed phenomenon of quenching in ferms of the formation of fhe so-called Ekman layers, which are responsible for the detachment of flames from the walls and the reduction of fheir width. Reduction of the flame speed with increasing angular velocity of rofation is explained in terms of free convection effects driven by centrifugal acceleration. 

Fig. 5. Estimated minimum fluidization velocity vs. centrifugal acceleration...

Fig. 6 shows the FFT spectrum for calculated bed pressure drop fluctuations at various centrifugal accelerations. The excess gas velocity, defined by (Uo-U ,, was set at 0.5 m/s. Here, 1 G means numerical result of particle fluidization behavior in a conventional fluidized bed. In Fig. 6, the power spectrum density function has typical peak in each centrifugal acceleration. However, as centrifugal acceleration increased, typical peak shifted to high frequency region. Therefore, it is considered that periods of bubble generation and eruption are shorter, and bubble velocity is faster at hi er centrifugal acceleration. 

Fig. 7 shows temporal changes in the degree of particle mixing, M, at various centrifugal accelerations. The degree of particle mixing, M, is defined as the following equation ... 

HSCCC is attracting attention based on its high separation scale, 100% recovery of sample, and mild operating conditions. It is a chromatographic separation process based on the partition coefficients of different analytes in two immiscible solvent systems (mobile phase and stationary phase) subjected to a centrifugal acceleration field. 

The spinning procedure starts with the positioning phase. The speed is increased slowly, increasing the centrifugal acceleration on the washing until at approximately 100 rpm it is all spread completely around the drum wall, distributed as evenly as possible. Normally an imbalance will have developed at this stage. 

Ultracentrifuge the tubes at 84,000 for 17 h in a swing rotor (Hitachi, RPS27-2, Tokyo, Japan). Note that at the beginning and end of centrifugation, acceleration and deceleration rates should be low so as not to disturb the gradient of the tubes. 

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