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Highest steady state

It is noted that Mo/DM is the best performing catalyst with the highest steady state activity and lowest deactivation rate. The deactivation rate is the lowest even under the influence of intense acid-catalyzed side reactions known to produce coke, i.e. oligomerization of styrene and cracking of ethylbenzene. Obviously, the high surface area and high connectivity of the support have played a determining role in the catalytic reaction. The effects they exert can be looked at in two ways ... [Pg.21]

It is seen from these measurements that the highest steady state temperature rise is about 27°C when 100 volt sinusoidal voltage is applied across the 2 mm gap where the liquid sample is deposited. The time required for the steady state temperature to decay to 1/3 of its initial value after the applied voltage is turned off is seen to be 20 seconds to 1 minute. [Pg.263]

Fig. 13.23 Calculated contours of iso-strain rate in the shoulder region of a plastically stretching bar, as an analog of the actively deforming base of a craze fibril. The central zone of thickness ad having the highest plastic-strain rate and the highest steady-state content of liquid-like material acts as a preferential conduit for the penetration of plasticizing diluent (from Argon (1999) courtesy of Wiley). Fig. 13.23 Calculated contours of iso-strain rate in the shoulder region of a plastically stretching bar, as an analog of the actively deforming base of a craze fibril. The central zone of thickness ad having the highest plastic-strain rate and the highest steady-state content of liquid-like material acts as a preferential conduit for the penetration of plasticizing diluent (from Argon (1999) courtesy of Wiley).
Thermal conduction in the solid phase is a key factor, as already mentioned in section 1.2.4. The heat conduction process is accounted for by Fourier s law in the heat balance equation which is thus a second order partial differential equation. An efficient numerical technique is required to avoid "numerical conduction" because the solid temperature gradient is very sharp at the light-off point (see section 3.1). There is no study of Ais numerical problem in the literature. However, Eigenberger (1972) studied the consequences of heat conduction on steady-state multiplicity. He showed that the conduction process is responsible for a reduction of the number of steady state solutions. In the example studied by Eigenberger, the steady-state solution is close to the "highest steady state" (i.e., steady state with the temperature maximum close to reactor inlet) without conduction because "the temperature maximum moves to the front of the reactor, driven by the backward conduction of heat". [Pg.556]

Because protein samples are actually ampholytes, when samples are loaded onto the gel and a current is appHed, the compounds migrate through the gel until they come to their isoelectric point where they reach a steady state. This technique measures an intrinsic physicochemical parameter of the protein, the pi, and therefore does not depend on the mode of sample appHcation. The highest sample load of any electrophoretic technique may be used, however, sample load affects the final position of a component band if the load is extremely high, ie, high enough to titrate the gradient ampholytes or distort the local electric field. [Pg.181]

In practice, carbon limited chemostat cultures are used to estimate the P/O quotient These conditions are used because they favour the most efficient conversion of the carbon substrate into cellular material, ie the highest efficiency of energy conservation. The steady state respiration rate (qo,) is measured as a function of dilution rate (specific growth rate) and Yq can be obtained from the reciprocal of the slope of the plot. qo, is also known as the metabolic quotient for oxygen or the specific rate of oxygen consumption. [Pg.50]

Transdermal nicotine is available in a variety of formulations and dosing schedules (e.g., 15 mg/l6 hours 7, 14, and 21 mg/24 hours and 11 and 22 mg/ 24 hours) (Cinciprinni and McClure 1998). Peak nicotine concentrations for the various systems are reached 2-6 hours after application, and steady state conditions occur 2—3 days after continued patch use (Henningfield 1995). The highest-dose patch (i.e., 21 or 22 mg/24 hours or 15 mg/l6 hours) delivers approximately 0.9 mg of nicotine per hour transdermally (Henningfield... [Pg.319]

CO conversions over Au/Ce02 catalyst were measured in the dry and wet condition as shown in Fig. 1. Similar to other supported gold catalysts, Au/Ce02 catalyst showed higher CO conversions in the presence of water vapor than in the absence of it at the same temperature. Catalytic activities for CO oxidation over Au/Ce02 catalysts prepared at different calcinations temperature were compared in the dry and wet condition as shown in Fig. 2. Au/Ce02 catalyst calcined at 473 K showed the highest initial CO conversion in the absence of water vapor. However, the CO conversion decreased steadily and reached a steady-state value over this catalyst. [Pg.322]

As illustrated in Fig. 1, the activated carbon displays the highest conversion and selectivity among all the catalysts during the initial reaction period, however, its catalytic activity continues to decrease during the reaction, which is probably caused by coke deposition in the micropores. By contrast, the reaction over the CNF composites treated in air and HN03 can reach a pseudo-steady state after about 200 min. Similiar transient state is also observed on the CNFs and the untreated composite. Table 3 collects the kinetic results after 300 min on stream over catalysts tested for the ODE, in which the activity is referred to the BET surface area. The air-treated composite gives the highest conversion and styrene selectivity at steady state. [Pg.723]

This interpretation of the experimental data is supported by the differences observed in the deactivation patterns and carbon contents after test, since one notorious effect of Hjp is the capacity to diminish the deactivation caused by coke deposition on the active sites [21,22]. This is supposed to be due to a reaction with the coke precursors, very likely a hydrogenolysis. In pure silica-aluminas, where no source of spillover is present, no special protection against deactivation should be observed. Indeed, the silica-aluminas lose most of their activity (about 80%) before reaching the steady-state and present the highest carbon contents after catalytic test. On the other hand, in the case of the mechanical mixtures, where spillover hydrogen is continuously produced by the CoMo/Si02 phase and can migrate to the silica-alumina surface, the predicted protection effect is noticed. The relative losses of activity are much lower... [Pg.104]

Steady-state molecular beam studies of the reaction of methylacetylene on reduced Ti02 (001) surfaces were undertaken to determine whether this reaction could be performed catalytically under UHV conditions. A representative experiment is presented in Figure 1. Prior to each experiment, the surface was sputtered and annealed to a temperature between 400 K and 550 K surfaces prepared in this manner have the highest fraction of Ti(+2) sites (ca. 30% of all surface cations) of any surface we have been able to create by initial sputtering [3]. Thus these are the surfaces most active for cyclotrimerization in TPD experiments [1]. Steady-state production of trimethylbenzene (as indicated by the m/e 105 signal detected by the mass spectrometer) was characterized by behavior typical of more traditional catalysts a jump in activity upon initial exposure of the crystal to the molecular beam, followed by a decay to a lower, constant level of activity over a longer time scale. Experiments of up to 6 hours in duration showed... [Pg.299]

For a reliable calculation of coefficient a from the potential dependence of kinetic cnrrents, experimental data are needed in which the kinetic currents are varied by at least an order of magnitnde. It follows that in at least one point the ratio 4/4 shonld not be higher than 3. In the case considered in Section 6.4, where 4,red = 4,ox this corresponds to valnes of 4/4 or k°/Kj which are not higher than 0.15. The highest valne of typically fonnd in aqneons solntions is about 2 X 10 cm/s. It follows that steady-state methods can yield reliable kinetic parameters only for reactions in which < 3 X 10 cm/s. At a component concentration of this corresponds... [Pg.198]

As a noble gas, Rn in groundwater does not react with host aquifer surfaces and is present as uncharged single atoms. The radionuclide Rn typically has the highest activities in groundwater (Fig. 1). Krishnaswami et al. (1982) argued that Rn and all of the other isotopes produced by a decay are supplied at similar rates by recoil, so that the differences in concentrations are related to the more reactive nature of the other nuclides. Therefore, the concentration of Rn could be used to calculate the recoil rate for all U-series nuclides produced by a recoil. The only output of Rn is by decay, and with a 3.8 day half-life it is expected to readily reach steady state concentrations at each location. Each measured activity (i.e., the decay or removal rate) can therefore be equated with the input rate. In this case, the fraction released, or emanation efficiency, can be calculated from the bulk rock Ra activity per unit mass ... [Pg.331]

Fio. 29. Average steady-state size of the dispersed phase at different viscosity ratios. The solid and dashed lines represent simulations in which and /xc are held constant. Other process parameters are the same as used for Fig. 28 (except 0 = 0.05). It is clear that the magnitudes of both viscosities must be considered rather than just the viscosity ratio. The lowest viscosity in each case is 1 Pa - s and the highest 1000 Pa - s. The curves are equally spaced on a logarithmic scale for viscosity. [Pg.159]

Elimination from the vitreous occurs by one of two pathways. This can be visualized by injecting fluorescent compounds and examining the concentration distribution in frozen sections obtained after a steady state has been established [230]. If the major route of elimination is by means of the re-tina/choroid, at steady state the lowest concentration would be in the vicinity of the retina. The contours observed in frozen sections of the rabbit eye obtained after intravitreal injection of fluorescein exhibit this pattern, with the highest concentration immediately behind the lens (Fig. 16A). Compounds not chiefly eliminated through the retina exit the vitreous by passive diffusion and enter the posterior aqueous, where they are eliminated by the natural production and outflow of aqueous humor. In such a situation, the contours would be perpendicular to the retina, with the highest concentration towards the rear of the vitreous cavity. This appears to be the case for fluorescently labeled dextran polymer, whose contours decrease in concentration toward the hyaloid membrane (Fig. 16B). [Pg.447]

Fig. 18 Finite element modeling of steady-state concentration profiles in the human eye[241] from a hypothetical device that releases from one side only, (a) Device releases towards the front (b) device releases towards the back. Arbitrary concentration units (scale, inset a) highest concentration marked x. Contours are shown for x-z plane and for x-y plane through the center, x-z portion of finite element mesh displayed (inset b) device (opaque to diffusion) represented by voided region. (Adapted from Ref. 244.)... [Pg.451]


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