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Temperature dependence, deposition rate

Support for this step was obtained by us in experiments where M was shown to add directly to bis(arene)metal complexes to give M2L2 (45, 46). Maximum nuclearity and stability of these species depends on the element, atom deposition rate, temperature and the type of arene. Mono-alkyl and -silyl substituted arenes give compounds that are unstable above 0 C. On the other hand, single crystals of a related triple-decker sandwich of mesitylene and chromium have been obtained (47),... [Pg.250]

In this section we will discuss the process in terms of reaction kinetics, film composition and film properties. Important to note is that the degree of utilization of WF6 under typical deposition conditions (ie. 50 nm/min and 2 seem WF6 per 6" wafer) is at least 50%. Thus the reactor is very likely to run in a depletion or feed controlled mode. As a result we expect the deposition rate to depend strongly on the WF6 total flow and be relatively insensitive to temperature variation. [Pg.182]

Plasma-enhanced (PE) CVD deposition of silicon nitride is typically performed at temperatures between 250 °C and 400 °C from silane (SiH4) and ammonia (NH3) gases. The plasma enhances the deposition rates. The deposition rate strongly depends on the deposition temperature and RF power, typical rates being around 400 nmmin4 [17]. Because of the low deposition temperature,... [Pg.148]

Even when considered by itself, a coating process can be very complicated. The film thickness is typically critical to the performance of the device to be manufactured. However, the conductivity of the film also depends on the concentration and structure (e.g., crystallinity) of the polymer in the film, which can also depend on the deposition rate, temperature, solvent removal rate, and a host of other parameters. [Pg.1224]

There are not many experiments at open cells with small T variations which are directed to determination of fundamental kinetic quantities like transfer coefficients of homogeneous redox couples [67], heterogeneous rate constant of the charge transfer [68], or nucleation at solid electrodes [21] system described in [21, 69], deposition of lead at the boron-doped diammid electrode, is a good example for a possible new role of thermoelectrochemistry which could provide important information about the nucleation process at non-metaUic electrodes without underpotential deposition. The temperature dependence of this t)q)e of nucleation has been studied, yet only scarcely. [Pg.26]

Figure 2.3. Catalysis (0), classical promotion ( ), electrochemical promotion ( , ) and electrochemical promotion of a classically promoted (sodium doped) ( , ) Rh catalyst deposited on YSZ during NO reduction by CO in presence of gaseous 02.14 The Figure shows the temperature dependence of the catalytic rates and turnover frequencies of C02 (a) and N2 (b) formation under open-circuit (o.c.) conditions and upon application (via a potentiostat) of catalyst potential values, UWr, of+1 and -IV. Reprinted with permission from Elsevier Science. Figure 2.3. Catalysis (0), classical promotion ( ), electrochemical promotion ( , ) and electrochemical promotion of a classically promoted (sodium doped) ( , ) Rh catalyst deposited on YSZ during NO reduction by CO in presence of gaseous 02.14 The Figure shows the temperature dependence of the catalytic rates and turnover frequencies of C02 (a) and N2 (b) formation under open-circuit (o.c.) conditions and upon application (via a potentiostat) of catalyst potential values, UWr, of+1 and -IV. Reprinted with permission from Elsevier Science.
In the case of control by surface reaction kinetics, the rate is dependent on the amount of reactant gases available. As an example, one can visualize a CVD system where the temperature and the pressure are low. This means that the reaction occurs slowly because of the low temperature and there is a surplus of reactants at the surface since, because of the low pressure, the boundary layer is thin, the diffusion coefficients are large, and the reactants reach the deposition surface with ease as shown in Fig. 2.8a. [Pg.51]

The deposition rate increases upon increasing the pressure. This is explained by noting that the impingement rate per unit area, r,, of molecules on the filament is linearly dependent on the pressure as r, = pj 2nksT, with the gas temperature. However, as the pressure becomes higher, the collisional mean free path of the silane becomes smaller, and the silane supply to the filaments becomes restricted. Moreover, the transport of deposition precursors to the substrate is restricted as well. The mean free path of silane was estimated to be 2.5 cm at a pressure of 0.02 mbar [531]. i.e.. the mean free path about equals the distance between filament and substrate. Indeed, a maximum in deposition rate is observed at this pressure. This corresponds to a value of pdk of 0.06 (cf. [530]). The microstructure parameter plotted as a function of pd has a minimum around Ms = 0.06 0.02 [530]. [Pg.160]

Supported model catalysts are frequently prepared by thermally evaporating metal atoms onto a planar oxide surface in UHV. The morphology and growth of supported metal clusters depend on a number of factors such as substrate morphology, the deposition rate, and the surface temperature. For a controlled synthesis of supported model catalysts, it is necessary to monitor the growth kinetics of supported metal... [Pg.85]

Temperature plays an important role in determining the amount and type of the carbon deposit. Generally during FTS at higher temperatures the amount of carbon deposited will tend to increase,30-31 but the case is often not so straightforward. An example of temperature dependence on the rate of carbon deposition and deactivation is the case of nickel CO hydrogenation catalysts, as studied by Bartholomew.56 At temperatures below 325°C the rate of surface carbidic carbon removal by hydrogenation exceeds that of its formation, so no carbon is deposited. However, above 325°C, surface carbidic carbon accumulates on the surface... [Pg.56]

Because the rate of growth depends, in a complex way, on temperature, supersaturation, size, habit, system turbulence and so on, there is no simple was of expressing the rate of crystal growth, although, under carefully defined conditions, growth may be expressed as an overall mass deposition rate, RG (kg/m2 s), an overall linear growth rate, Gd(= Ad./At) (m/s) or as a mean linear velocity, // (= Ar/At) (m/s). Here d is some characteristic size of the crystal such as the equivalent aperture size, and r is the radius corresponding to the... [Pg.847]

Adachi and Mizushima [30] studied the deposition system DMTC + O2 + H2O in the 400-500 °C temperature range, hi the presence of water vapor, the deposition rate dependence on DMTC concentration increased from [DMTC] to [DMTC]° . They suggested that in the reaction of DMTC + O2, the rate-determining step is the oxidation of Sn-Cl bonds, while in the reaction of DMTC + O2 + H2O, the oxidation of Sn - CH3 bonds is rate determining. As will be seen below, this description of the chemistry is almost certainly incorrect (Sect. 5.2). They also reported an activation energy of 38 kcalmoC for the hydrolysis of DMTC (Fig. 7) and asserted that the hydrolytic decomposition of Sn - Cl bonds is much faster at these temperatures. [Pg.13]


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See also in sourсe #XX -- [ Pg.71 , Pg.72 , Pg.73 , Pg.74 ]




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