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Temperature regimes

Rockwell hardness testing has been extended to both low and high temperature regimes usually by enclosing the sample and part of the machine in an environmental chamber and using extensions for the anvil and indenter. [Pg.465]

Reversibility of Equation 2. Notwithstanding the problems and conflicts, there is widespread agreement that the NTC phenomenon may well be related to the reversibiUty of equation 2 (13,60,63—67) R- + O2 ROO-. In the low temperature regime, the equiUbrium Hes to the right and alkylperoxy radicals are the dominant radical species. They form hydroperoxides, the chain-branching agent, by reaction 3. [Pg.338]

Boltzmann s constant, and T is tempeiatuie in kelvin. In general, the creep resistance of metal is improved by the incorporation of ceramic reinforcements. The steady-state creep rate as a function of appHed stress for silver matrix and tungsten fiber—silver matrix composites at 600°C is an example (Fig. 18) (52). The modeling of creep behavior of MMCs is compHcated because in the temperature regime where the metal matrix may be creeping, the ceramic reinforcement is likely to be deforming elastically. [Pg.204]

Additions of selected alloying elements raise the recrystaUization temperature, extending to higher temperature regimes the tensile properties of the cold-worked molybdenum metal. The simultaneous additions of 0.5% titanium and 0.1% zirconium produce the TZM aUoy, which has a corresponding... [Pg.466]

Measurement of the hotness or coldness of a body or fluid is commonplace in the process industries. Temperature-measuring devices utilize systems with properties that vaiy with temperature in a simple, reproducible manner and thus can be cahbrated against known references (sometimes called secondaiy thermometers). The three dominant measurement devices used in automatic control are thermocouples, resistance thermometers, and pyrometers and are applicable over different temperature regimes. [Pg.759]

A disadvantage of the two-state methods is that modelling of a real potential energy surface (PES) by a TLS cannot always been done. Moreover, this truncated treatment does not cover the high-temperature regime since the truncation scheme does not hold at T> coq. With the assumption that transition is incoherent, similar approximations can be worked out immediately from the nonlocal effective action, as shown in Sethna [1981] and Chakraborty et al. [1988] for T = 0, and in Gillan [1987] for the classical heat bath. [Pg.89]

The formation of a layer of metal oxide on the surface of this steel provides better corrosion resistance in oxidizing environments than under reducing conditions. Common steels 304, 304L, 347, 316 and 316L are used for equipment exposed to aqueous solutions of acids and other low-temperature corrosive conditions. For high-temperature regimes involving... [Pg.68]

Numerical solution of Eq. (51) was carried out for a nonlocal effective Hamiltonian as well as for the approximated local Hamiltonian obtained by applying a gradient expansion. It was demonstrated that the nonlocal effective Hamiltonian represents quite well the lateral variation of the film density distribution. The results obtained showed also that the film behavior on the inhomogeneous substrate depends crucially on the temperature regime. Note that the film exhibits different wetting temperatures on both parts of the surface. For chemical potential below the bulk coexistence value the film thickness on both parts of the surface tends to appropriate assymptotic values at x cx) and obeys the power law x. Such a behavior of the film thickness is a consequence of van der Waals tails. The above result is valid when both parts of the surface exhibit either continuous (critical) or first-order wetting. [Pg.282]

One of the most important problems in the sphere of industrial activity is that attending high ambient temperature. Therefore, the search is on for substances that can increase the resistance of organisms to dangerous overheating. Experiments on white rats show that substance 103, called azomopine, has a protecting effect in different temperature regimes. [Pg.82]

Depending on the dose and temperature regime, the screening effect azomopine is observed after intoxication by chlorophos. The survival of white rats injected with this preparation is 50% higher than that of control rats. When toxic doses of copper sulfate were injected for 7 days, 70 and 36% of the rats survived. After the simultaneous injection of azomopine, their survival increased to 100 and 70% (74MI1). [Pg.83]

The temperature regimes for the stability of intermediates is different for various transition metals. For example on Fe(lll) the adsorbed ethylene decomposes partially at 200 K, while the conversion to surface carbon is complete at 370 K. Similarly, on nickel faces molecular chemisorption of ethylene is restricted to temperatures below ambient. At temperatures between approximately 290 K and 450 K ethylene chemisorption on nickel... [Pg.53]

CVI is a special CVD process in which the gaseous reactants penetrate (or infiltrate) a porous structure which acts as a substrate and which can be an inorganic open foam or a fibrous mat or weave. The deposition occurs on the fiber (or the foam) and the structure isgradually densified to form a composite.The chemistry and thermodynamics of CVT are essentially the same as CVD but the kinetics is different, since the reactants have to diffuse inward through the porous structure and the by-products have to diffuse out.f l Thus, maximum penetration and degree of densification are attained in the kinetically limited low-temperature regime. [Pg.129]

Ozin, Hanlan, and Power, using optical spectroscopy (49,121). In view of the marked temperature-effect observed for the cobalt system, we shall focus on this cluster system here. Evidence for cobalt-atom aggregation at the few-atom extreme first came from a comparison of the optical data for Co Ar — 1 10 mixtures recorded at 4.2 and 12 K (see Fig. 4). A differential of roughly 8 K in this cryogenic-temperature regime was sufficient to cause the dramatic appearance of an entirely new set of optical absorptions in the regions 320-340 and 270-280 nm (see Fig. 4). Matrix variation, from Ar, to Kr, to Xe, helped clarify atom-cluster, band-overlap problems (see Fig. 5). [Pg.87]

The temperature dependence of the reaction is remarkable. For a 5-h reaction, a temperature change of 18° results in a change in the yield of CFjSnBrs from 0 at 112° to 55% at 130°. Alternatively, for a 35-h reaction, the yield of (CF3) SnBr2 is very low at both 112 and 130° in the former, because the (CF3)2SnBr2 has yet to be formed, whereas, in the latter, most of the (CF3)2SnBr2 has decomposed. These results provide one explanation of the cause of the failure of the earlier study (8) to be productive the temperature regime is critical. [Pg.195]

Fig. 8-5 Soil and soil forming processes - a global view. The moisture and temperature regimes are generalized and intended only to show major pedoclimatic environments. Spodosols, for example, can also occur in a cryic regime and even in equatorial regions. Other orders could also occur in more than one moisture and temperature environment. (overleaf)... Fig. 8-5 Soil and soil forming processes - a global view. The moisture and temperature regimes are generalized and intended only to show major pedoclimatic environments. Spodosols, for example, can also occur in a cryic regime and even in equatorial regions. Other orders could also occur in more than one moisture and temperature environment. (overleaf)...
Laminar flame speed is one of the fundamental properties characterizing the global combustion rate of a fuel/ oxidizer mixture. Therefore, it frequently serves as the reference quantity in the study of the phenomena involving premixed flames, such as flammability limits, flame stabilization, blowoff, blowout, extinction, and turbulent combustion. Furthermore, it contains the information on the reaction mechanism in the high-temperature regime, in the presence of diffusive transport. Hence, at the global level, laminar flame-speed data have been widely used to validate a proposed chemical reaction mechanism. [Pg.44]

In the second step, these MoOj NWs were converted to M0S2 by exposure to H2S within either of two temperature regimes (500-700 °C or 800-1,000 °C) according to the reaction (for x = 2)... [Pg.196]

H2 TDS was used as the highest H2 desorption temperature (370 K) occurs below the temperature regime of encapsulation. For the reduced sample there was a 70% decrease In H2 chemisorption and a 33 K shift to lower temperatures when the unannealed sample (first H2 TDS) was compared to the sample annealed at 370 K (second H2 TDS). No change In the AES was observed after either the first or second TDS, showing that the Pt overlayer does not Island or encapsulate. We take these low Pt coverage experiments to Indicate an electronic Interaction (preferably bond formation, which does not require significant charge transfer) between Pt and reduced Tl species that Is activated at about 370 K. [Pg.84]

Fig. 3 A shows the effluent NH3 concentration observed for Ru/MgO as a function of reaction temperature for three different Pn, / Phj / Paf ratios at 20 bar total pressure. It is obvious that the reaction orders for N2 and H2 have opposite signs. Fig. 3B illustrates that the reaction orders for N2 and H2 partly compensate each other in the kineticaliy controlled temperature regime. Hence an increase in total pressure with a constant Pnj / Phj 1/3 ratio does not lead to a significant increase in conversion at lower temperatures. For the plication of alkali-promoted Ru catalysts under industrial synthesis conditions, it is necessary to find a compromise between kinetics and thermodynamics by increasing the Pn, / Phj ratio. The optimum observed for Cs-Ru/MgO prepared from CS2CO3 at 50 bar is at about Pnj / Phj 40 / 60 [15]. The high NH3 concentration of about 8 % obtained with 0.138 g catalyst using a total flow of 100 Nml/min clearly shows that Ru catalysts have indeed the potential to replace Fe-based catalysts in industrial synthesis [15]. Fig. 3 A shows the effluent NH3 concentration observed for Ru/MgO as a function of reaction temperature for three different Pn, / Phj / Paf ratios at 20 bar total pressure. It is obvious that the reaction orders for N2 and H2 have opposite signs. Fig. 3B illustrates that the reaction orders for N2 and H2 partly compensate each other in the kineticaliy controlled temperature regime. Hence an increase in total pressure with a constant Pnj / Phj 1/3 ratio does not lead to a significant increase in conversion at lower temperatures. For the plication of alkali-promoted Ru catalysts under industrial synthesis conditions, it is necessary to find a compromise between kinetics and thermodynamics by increasing the Pn, / Phj ratio. The optimum observed for Cs-Ru/MgO prepared from CS2CO3 at 50 bar is at about Pnj / Phj 40 / 60 [15]. The high NH3 concentration of about 8 % obtained with 0.138 g catalyst using a total flow of 100 Nml/min clearly shows that Ru catalysts have indeed the potential to replace Fe-based catalysts in industrial synthesis [15].
Investigations with the modular multi-channel [28,98] and silicon chip [19, 56-62] micro reactors demonstrate that by exact temperature control the oxidation of ammonia can be run with increased and deliberately steered selectivity. A major application is provided by carrying out former high-temperature reactions in the low-temperature regime. In the case of ammonia oxidation in the chip micro reactor, the yield of the value product NO was actually lower in that regime. In the case of the multi-plate-stack micro reactor, higher yields of the value product NO2 were achieved. [Pg.298]


See other pages where Temperature regimes is mentioned: [Pg.2411]    [Pg.187]    [Pg.126]    [Pg.369]    [Pg.414]    [Pg.260]    [Pg.2026]    [Pg.3]    [Pg.269]    [Pg.323]    [Pg.410]    [Pg.423]    [Pg.281]    [Pg.98]    [Pg.122]    [Pg.522]    [Pg.287]    [Pg.361]    [Pg.520]    [Pg.36]    [Pg.250]    [Pg.270]    [Pg.182]    [Pg.35]    [Pg.196]    [Pg.312]    [Pg.596]    [Pg.116]    [Pg.123]    [Pg.275]   
See also in sourсe #XX -- [ Pg.51 ]




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Cure temperatures, regimes

Furnaces temperature control regimes

Glass-transition temperature liquid regimes

High-temperature regime, supercooled liquids

Low-temperature regime

Low-temperature regime, supercooled liquids point

Other Temperature Regimes

Temperature dependence supercooled regime

Temperature-time-regimes

Temperature/thermal regime

Temperatures furnace temperature control regimes

Transient regimes temperature variation

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