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Mean surface residence time

IN SSITKA, Np and the mean surface residence time of these most active reaction intermediates (xp) are determined. After a step-change between two reactant streams containing different isotopes of a reactant without disturbing other reaction conditions or reaction (as long as an H2/D2 switch is not used), the distributions of isotopically labeled products are monitored using a mass spectrometer. Tp is first determined by integration of the normalized isotopic transient of a product relative to an inert tracer (usually Ar) that delineates gas phase hold-up (see Figure 1 for the case of methanation). Np is then calculated from... [Pg.322]

Fig. 7. Experimental determination of the mean surface-residence time in the presence of interparticle readsorption. Fig. 7. Experimental determination of the mean surface-residence time in the presence of interparticle readsorption.
SSITKA experiments can be performed in plug flow or mixed flow reactors. This approach was proposed by Happel et al. [18] and further developed by Beimett [19], Biloen [20], and Shaimon and Goodwin [21]. In these experiments a step change or pulsed input is induced in the isotopic label of one reactant in the reactant flow. The total concentration of labeled plus non-labeled reactants, adsorbates, and products is maintained at steady state under isothermal and isobaric conditions. The reactor effluent species are then monitored versus time. The mean surface residence time and abundance of adsorbed surfece... [Pg.237]

Product readsorption at reactive sites can lead to substantial contributions to the transient response, lowering the measured activity and reaction rate. Product readsorption at nonreactive sites will also inflate the measurement of surfece intermediates leading to the observed product and overestimate the mean surface residence time. Effects of product readsorption can be addressed by decreasing the bed length or increasing the space velocity. [Pg.237]

A fraction of the total runoff from the continents to oceans passes through freshwater lakes. From the data on global volume, surface and drainage basin area, and mean water residence time for freshwater lakes, a mean linear rate of flow through lakes is... [Pg.513]

Scavenged type Trace metals such as Al, Co, Ce, and Bi, show surface enrichment and depletion in deep waters, in contrast to the opposite trend in nutrient types. These elements are highly particle-reactive and are rapidly removed from the water column by sinking particulate matter and/or by scavenging at the sediment-water interface. Their mean oceanic residence times are short (<10 -10 years). Interoceanic variations in their concentration can be large (e.g., Atlantic/Pacific concentration ratio 40 for Al) depending on kinetic balance between supply and removal for the specific basins. [Pg.10]

Reynolds number (ND Vm) diffusion time =Dal/kt (s) reaction time , see equation (15.25) (s) vessel diameter (m) superficial gas velocity (m/s) dispersion volume (m ) liquid volume without gassing (m ) number of mixed zones in loop CfA-CLA (moles/m ) gas hold-up per unit dispersion volume liquid hold-up per unit dispersion volume gas volumetric recirculation rate per unit gas feed rate mean liquid circulation time (s) mean liquid residence time (s) liquid viscosity (Pa s) gas viscosity (Pa s) liquid density (kg/m ) gas density (kg/m ) surface tension (N/m) yield stress (Pa)... [Pg.361]

At the top feed liquid flows downward as a thin film by gravitational force, by means of a highspeed rotor film thickness is equalized and the surface is constantly renewed. Z 0.5-0.6 m (heated length), d = 0.15-1.7 m (outer diameter), heating area A 0.1-25 m, operating pressure down to ca 1 mbar, mean solution residence time 10-60 s, rotor speed ca. 1000 revolutions/min, film thickness 0.1-1 mm, final solution viscosity ca. 20-200 Pa-s, k = 500-1800 W/(m k) at concentration of aqueous solutions, evaporation rate ca. 80-1000 kg/h water, to calculate heat transfer see [7.21]... [Pg.505]

Problems can consist in the chemical and colloidal stabihty, eg upon oral administration, and in the low permeation through cellular membranes. For this reason vesicles are mostly administered parenterally, ie intravenously, subcutaneously, or intramuscularly. Their tissue specificity is first confined to the cells of the reticuloendothelial system which recognizes them as foreign microparticles and transports them to liver and spleen. Their biodistribution can be regulated by surface modification, eg by placing PEO stealth systems) or monoclonal antibodies site-specific targeting) to the vesicle smface. By this means their residence time and bioavailablity can be increased (211). [Pg.6361]

Poet et al. (1972) estimated tropospheric aerosol residence times ranging from 1.59 to 13 days (average 5.4 days) when based on the Bi/ °Pb activity ratios and from 11 to 77 days (average 24 days) when based on the 2i°Po/ °Pb activity ratios for 20 measurements of aerosol samplings carried out in surface air during a 4 1/2-year period at Boulder, Colorado (40°01 N, 105°17 W). They concluded that a mean tropospheric residence time of about 4 days could be applied for aerosol particles in the lower troposphere and about a week for aerosol particles in precipitation. They also found that the mean aerosol residence time increases with altitude within the troposphere by less than a factor of 3 (Moore et al., 1973). [Pg.76]

In 1973, a multistage surface-fermentation process was patented in Japan for the production of acetic acid (42) eight surface fermenters were connected in series and arranged in such a way that the mash passed slowly through the series without disturbing the film of yAcetobacter on the surface of the medium. This equipment is reported to produce vinegar of 5% acidity and 0.22% alcohol with a mean residency time in the tanks of 22 h. [Pg.409]

The residence time or contact time discussed in the preceding section is a simple average. Hyman (H21) pointed out that the residence time of any one gas molecule could vary widely from the mean because of the tortuous paths followed by the gas bubbles from the gas inlet to the surface. Knowledge of gas residence time is important for design purposes and is necessary for an understanding of the behavior of gas-liquid dispersions (W5). Relatively little experimental effort has been devoted to this area. [Pg.314]

At high temperatures desorption prevails, implying that the coverages of all species are small and that the surface is nearly empty. This does not mean that the reaction can not take place, but the residence time of any species on the surface before it desorbs or reacts is short. Since the surface is nearly empty, we can set 6 1 and obtain ... [Pg.67]

Catalysts and their carriers are provided in micro channels by various means and in various geometric forms. In a simple variant, the catalyst itself constitutes the micro-reactor construction material without need for any carrier [2-A], In this case, however, the catalyst surface area equals that of the reactor wall and hence is comparatively low. Accordingly, applications are typically restricted to either fast reactions or processing at low flow rates for slow reactions (to enhance the residence time). [Pg.258]

What became evident was that interactions between adsorbed particles can also exert an influence on their surface mobility and therefore the residence time at a particular site. The mean residence time of an isolated oxygen adatom at the Ru(0001) surface varies from 60 to 220 ms when a second oxygen adatom is located two lattice constants a0 apart from the first but only 13 ms when the... [Pg.65]

These are similar to stabilization ponds except that oxygen is added by mechanical surface aerators. This cuts the residence time of the water by 80%. It also means that the depth of the lagoons can be increased to 18 ft (5.5 m) and aerobic conditions can be maintained. The surface aerator power level is usually between 0.008 and 0.06 hp/1,000 gal (0.0002-0.016 hp/m3). This is not enough power to keep all the solids in solution. To do that would require 0.05-0.1 hp/1,000 gal (0.013-0.026 hp/m3).33... [Pg.447]

In soils, lead concentrates in organic-rich surface horizons (NRCC 1973). In one instance, only 17 mg of soluble Pb/kg was found in soils 3 days after the addition of 2784 mg of lead (as lead nitrate)/kg (NRCC 1973). The estimated residence time of lead in soils is about 20 years complete turnover in topsoil is expected every few decades (Nriagu 1978a). In forest litter, however, the mean residence time of lead is lengthy estimates range from 220 years (Turner et al. 1985) to more than 500 years (Friedland and Johnson 1985). [Pg.246]


See other pages where Mean surface residence time is mentioned: [Pg.189]    [Pg.54]    [Pg.189]    [Pg.54]    [Pg.6]    [Pg.100]    [Pg.48]    [Pg.898]    [Pg.2441]    [Pg.308]    [Pg.2422]    [Pg.47]    [Pg.73]    [Pg.533]    [Pg.687]    [Pg.15]    [Pg.126]    [Pg.189]    [Pg.43]    [Pg.211]    [Pg.705]    [Pg.218]    [Pg.75]    [Pg.255]    [Pg.652]    [Pg.33]    [Pg.131]    [Pg.148]    [Pg.59]    [Pg.483]    [Pg.54]    [Pg.378]    [Pg.1653]    [Pg.42]    [Pg.568]   
See also in sourсe #XX -- [ Pg.189 , Pg.195 ]




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