Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Separator direct interception

An aerosol with particles in the micron size range flows around a smooth solid sphere a few millimeters in diameter. At sufficiently high Reynolds numbers, a laminar boundary layer develop.s over the sphere from the stagnation point up to an angle of about 110 at which. separation takes place. The removal of particles by direct interception can be calculated from the velocity distribution over the forward. surface of the sphere, up to 90 from the forward stagnation point (Fig. 4.P4). [Pg.122]

Clarification processes are normally used to separate the suspended cells from a fluid stream primarily by direct interception and sieving, where the particles are caught in or on the surface of the filter medium. In addition, some liquid filters removal capabilities can be achieved or enhanced by charge effects, in which case they may retain some molecules by adsorption. ... [Pg.49]

Suspended solids are separated from fluids via three mechanisms inertial impaction, differential interception, and direct interception. [Pg.218]

A surface or screen filter is one in which all pores rest on a single plane, which therefore depends largely upon direct interception to separate particles from a fluid. Only a few filters on the market today, for example, woven wire mesh, woven cloth, and certain membrane filters, qualify as surface filters. [Pg.223]

Operation. The absolute separator is a multistage device utilizing all of the forces employed in mechanical separation—gravity, centrifugal force, inertial impaction, direct interception, and Brownian diffusion. [Pg.684]

Fuel cells are electrochemical systems that convert the energy of a fuel directly into electric power. The design of a fuel cell is based on the key components an anode, to which the fuel is supplied a cathode, to which the oxidant is supplied and an electrolyte, which permits the flow of ions (but no electrons and reactants) from anode to cathode. The net chemical reaction is exactly the same as if the fuel was burned, but by spatially separating the reactants, the fuel cell intercepts the stream of electrons that spontaneously flow from the reducer (fuel) to the oxidant (oxygen) and diverts it for use in an external circuit. [Pg.298]

E) Normal means 1 atm (760 mm Hg) pressure. Boiling occurs at a temperature at which the substance s vapor pressure becomes equal to the pressure above its surface. On this phase diagram, at 1 atm pressure, there is no intercept on a line separating the liquid phase from the gas phase. In other words, carbon dioxide cannot be liquefied at 1 atm pressure. It is in the liquid form only under very high pressures. At 1.0 atm pressure, solid C02 will sublime — that is, go directly to the gas phase. [Pg.374]

The overall process, illustrated in Scheme 10.4, intercepts the racemate (2) by crystallization from heptane. After separation of the enantiomers using the MCC process, the radafaxine free base is converted to the desired salt directly on treatment with anhydrous HCl. Any mixed fractions from the MCC separation are combined with the epimerized R,R)-enantiomer and fresh racemate for processing, hence generating further radafaxine free base for conversion to the hydrochloride salt. These results were subsequently confirmed in a Proof of Concept study performed on the medium- to large-scale in-house MCC equipment prior to scale-up. [Pg.211]

Na(3p) emission via a separate experiment, where we monitored the Na(3p) signal resulting from the direct 2-photon excitation of the Na(3d) state. The direct w + a>2 contribution was accounted for by measuring the Na(3p) signal at different co, + co2 intensities. Because we saturate the one photon coi resonance, the dependence of the o>i + a>2 process was found to be linear in the u>2 intensity. Hence, determining the slope and intercept of this linear dependence allowed us to subtract out its contribution at the experimental to and C02 intensities. [Pg.290]

In a spray drier the raw material slurry is nebulized. Hot air is blown into the spray drier tower In the opposite direction. The moisture from the droplets of the nebulized slurry evaporates and the product of this drying process, the spray dry granulate, consists of little soft balls of nearly equal size. Together with the air, granulate can also be drained off. After that it is intercepted in a so-called cyclone separator. [Pg.134]

Assumptions Base area is smooth and no direct self-radiation is intercepted by the base surface separating medium behveen surfaces is nonabsorbing emissivity is equal to absorptivity... [Pg.583]

Consider radiative interchange between two finite black surface area elements Ai and A2 separated by a transparent medium. Since they are black, the surfaces emit isotropically and totally absorb all incident radiant energy. It is desired to compute the fraction of radiant energy, per unit emissive power 1, leaving Ai in all directions which is intercepted and absorbed by A2. The required quantity is defined as the direct view factor and is assigned the notation F12. Since the net radiant energy interchange Q12 = AiFi jEi between surfaces... [Pg.706]

Local Exhaust Ventilation. Local exhaust ventilation is designed to intercept the flammable atmosphere at the source of release and directs it into a system where air is safely separated from the fuel. Correctly designed local exhaust ventilation systems could be very effective in limiting the spread of dust cloud atmospheres beyond the source of release. Local exhaust ventilation is generally less expensive to run than dilution ventilation because less air is used. [Pg.790]

The major difficulty in the analysis of chromatographic data is separating the axial dispersion and mass-transfer contributions since, except for gaseous systems at very low flow rates, the axial dispersion coefficient (Dl) is velocity dependent. For liquid systems Dl varies essentially linearly with velocity so a plot of HETP vs. superficial velocity (ev) should be linear with the mass-transfer resistance directly related to the slope (Fig. 6). For gaseous systems at a high Reynolds number this same plot can be used, but in the low Reynolds number region a plot oiH/v vs. 1 /v may be more convenient since in this region Dl is essentially constant and the intercept thus yields the mass-transfer resistance [43-45]. [Pg.59]


See other pages where Separator direct interception is mentioned: [Pg.324]    [Pg.393]    [Pg.452]    [Pg.393]    [Pg.495]    [Pg.178]    [Pg.220]    [Pg.600]    [Pg.13]    [Pg.182]    [Pg.433]    [Pg.712]    [Pg.117]    [Pg.306]    [Pg.197]    [Pg.129]    [Pg.735]    [Pg.171]    [Pg.1148]    [Pg.368]    [Pg.20]    [Pg.330]    [Pg.540]    [Pg.843]    [Pg.145]    [Pg.153]    [Pg.703]    [Pg.64]    [Pg.190]    [Pg.255]   
See also in sourсe #XX -- [ Pg.215 ]




SEARCH



Intercept

© 2024 chempedia.info