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Exit For

The cell is the basis of all electrolysis. The anode admits current into the electrolyte and the cathode serves as a means of exit for the electrical current. The electrical flow provides a definition for electrolysis the flow of current from the anode through the electrolyte and out of the cell through the cathode with ensuing decomposition of the electrolyte, with products being formed at the electrodes. [Pg.521]

The first consideration for establishing a filter system is to determine what frequencies will exit for a given compressor unit ... [Pg.596]

The concentration is continuous at the reactor exit for all values of D and this forces the zero-slope condition of Equation (9.17). The zero-slope condition may also seem counterintuitive, but recall that CSTRs behave in the same way. The reaction stops so the concentration stops changing. [Pg.332]

The inlet-outlet assembly is connected to both a source of argon and a bubbler which serves as exit for the inert gas. Argon is... [Pg.103]

This system produces a steady laminar flow with a flat velocity profile at the burner exit for mean flow velocities up to 5m/s. Velocity fluctuations at the burner outlet are reduced to low levels as v /v< 0.01 on the central axis for free jet injection conditions. The burner is fed with a mixture of methane and air. Experiments-described in what follows are carried out at fixed equivalence ratios. Flow perturbations are produced by the loudspeaker driven by an amplifier, which is fed by a sinusoidal signal s)mthesizer. Velocity perturbations measured by laser doppler velocimetry (LDV) on the burner symmetry axis above the nozzle exit plane are also purely sinusoidal and their spectral... [Pg.82]

The physiological role of the ICOR is not clear and may be heterogeneous in the various tissues. In the thick ascending limb of the loop of Henle this channel appears to serve as the exit for CP at the basal cell pole [16,65,66], This conductive mechanism, therefore, is required for the reabsorption of Na and CP by this segment of the nephron [16]. In the rectal gland of Squalus acanthias a very similar channel is utilized for Na" and CP secretion. In these latter cells the CP-channel is present in the luminal membrane and is controlled by cytosolic cAMP [15,56,71]. It has been claimed that this kind of channel is also responsible for the secretion of CP in the colonic crypt cell, in colonic carcinoma cells and in respiratory epithelial cells [17,19,20,22]. Recent data have cast some doubt on this concept ... [Pg.280]

For example, simple natural ventilation would be appropriate for weak toxicity through inhalation. If the substance is harmful, it would be necessary to place the operation in a ventilation-assisted area. If it is toxic, a well-ventilated fume hood would be required if very toxic, it might be necessary to place the work in an airtight environment under negative pressure, with the atmosphere filtered at the exit. For cases of serious chronic toxicity, telemanipulation devices might be required. [Pg.32]

Differential extractors, in which the phases are continuously in contact in the extractor and are only separated at the exits for example, in packed column extractors. [Pg.617]

The fraction conversion at the CSTR exit for this first-order reaction is given by... [Pg.366]

Finally the two compositions in (4) are graphically similar, and so we discuss only the first. Graph is formed by connecting a query node q a branch node - to two nodes, the entry node e of B and the NULL node p which is the exit for the exit node d of B is directly connected back to q. We can only... [Pg.124]

The frictional loss term F in Equation 4-28 represents the loss of mechanical energy resulting from friction and includes losses resulting from flow through lengths of pipe fittings such as valves, elbows, orifices and pipe entrances and exits. For each frictional device a loss term of the following form is used ... [Pg.121]

In the cobalt-catalyzed Fischer-Tropsch reaction, oxygen is mainly rejected as water and this will generate high partial pressures of water at the reactor exit for fixed-bed reactors. As a consequence of extensive back mixing in slurry reactors,... [Pg.11]

Figure 1. Flow heat of mixing calorimeter (a and b) solutions to be mixed (c) calorimetric block (d) thermopiles for detecting heat flow (e) exit for mixture... Figure 1. Flow heat of mixing calorimeter (a and b) solutions to be mixed (c) calorimetric block (d) thermopiles for detecting heat flow (e) exit for mixture...
Right Histograms of the olg(3II) population vs the iodine-iodine separation at 2 time points. Shown are the first two exits for such points in time that the dissociative population has reached an average intramolecular separation of —4 A (This distance is about the upper limit of the experimental probing window.) [16] The localized nature of the dissociative population is a direct result of the vibrational localization on the parent 6 state, as an exit to the a state occurs only when there is population in the curve-crossing region. [Pg.211]

Determine the efficiency and power output of a regenerative Rankine cycle using steam as the working fluid and a condenser pressure of 80 kPa. The boiler pressure is 3 MPa. The steam leaves the boiler at 400° C. The mass rate of steam flow is 1 kg/sec. The pump efficiency is 85% and the turbine efficiency is 88%. After expansion in the high-pressure turbine to 400 kPa, some of the steam is extracted from the turbine exit for the purpose of heating the feed-water in an open feed-water heater, the rest of the steam is reheated to 400°C and then expanded in the low-pressure turbine to the condenser. The water leaves the open feed-water heater at 400 kPa as saturated liquid. Determine the steam fraction extracted from the turbine exit, cycle efficiency, and net power output of the cycle. [Pg.57]

The time-dependent simulations of free jets discussed here focus on the vortex dynamics and transition to turbulence downstream of the jet exit. For the sake of computational efficiency, the author concentrates on the study of jet flow initialized with laminar conditions with a thin rectangular vortex sheet having slightly rounded-off corner regions and uniform initial momentum thickness [9]. Initial conditions for the simulated jets involve top>-hat initial velocity profiles... [Pg.210]

Figure 18.4 Propane-air premixed flame attached to suction coUar rim for — U2IU1 = 0.0 (a), and to nozzle exit for —U2/U1 = 0.022 (6)... Figure 18.4 Propane-air premixed flame attached to suction coUar rim for — U2IU1 = 0.0 (a), and to nozzle exit for —U2/U1 = 0.022 (6)...
This method involves the measurement of reactant concentrations and temperatures at the reactor exit for various contact times as shown in Fig. 1. [Pg.193]

A 50-ml glass ampoule used for polymerization equipped with a septum with a syringe needle for the inlet of nitrogen and extending below the surface of the reactants and another syringe needle to go above the reactants to act as an exit for the HC1 that is generated in this reaction... [Pg.59]

Fig. 269. Worm drying and mixing machine A — inlet for introduction of dough with a 30% water content, B— water discharge outlet, C— exit for the mass containing... Fig. 269. Worm drying and mixing machine A — inlet for introduction of dough with a 30% water content, B— water discharge outlet, C— exit for the mass containing...
The final structure of the formed cross-link proposed in this article might seem similar to that depicted in the current theory in the aspect that it is not monomeric but polymerized GA, although some differences surely exit for example, unsaturation at a, (3 - position occurs only at locations adjacent to Schiff base imine according to our theory. The most important difference between the two theories would be the timing when GA polymerization occurs. This difference would be crucial when we attempt to control the structure — for example, the chain length — of the formed cross- links in the future. [Pg.128]

The effectiveness factors for the reactions and the components are changing along the length of the reactor. The data above shows the effectiveness factors and rates at the exit. Here the effectiveness factor of a component is computed from the rate of its consumption at the exit. For components which are formed in a single reaction and are not involved in any other reactions, such as styrene, benzene, toluene and carbon dioxide, the effectiveness factor is determined by the effectiveness factor of their reaction, i.e., by the reactions (1) to (3) and (6). Note that for most of the reactions (except for reactions (5)... [Pg.514]


See other pages where Exit For is mentioned: [Pg.345]    [Pg.902]    [Pg.552]    [Pg.1149]    [Pg.550]    [Pg.165]    [Pg.47]    [Pg.330]    [Pg.124]    [Pg.139]    [Pg.78]    [Pg.284]    [Pg.328]    [Pg.53]    [Pg.607]    [Pg.67]    [Pg.120]    [Pg.107]    [Pg.53]    [Pg.160]    [Pg.33]    [Pg.248]    [Pg.6]    [Pg.307]    [Pg.24]    [Pg.177]   
See also in sourсe #XX -- [ Pg.269 ]




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Exit or activation for early retirees and disabled people

Exitation

Exiting

Exits

Requirements for Exits

Safety Features for Exit Routes

Situation 1 Mean Exit Time Between Slices for Neutral Species

Situation 1 Mean Exit Time for Charged Species

Situation 2 Mean Exit Time After Reflection for Neutral Species

The turbine exit condition (for reversible cooled cycles)

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