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Temperature Considerations

If the constant temperature algorithm is used in a trajectory analysis, then the initial conditions are constantly being modified according to the simulation of the constant temperature bath and the relaxation of the molecular system to that bath temperature. The effect of such a bath on a trajectory analysis is less studied than for the simulation of equilibrium behavior. [Pg.330]

Reforming reaction takes place at high temperatures. Typically, in vehicle systems utilizing methanol reformation, hydrogen is directly injected into the cell where methanol and water are vaporized to form H2, CO, and C02 [6], This reformation takes place at approximately 280°C [6], Materials that operate at these temperatures are quite costly. In addition, separate loop cooling systems (currently in the form of humidifiers) are required to keep the overall cell temperature down and the water management under control for a PEM fuel cell. An aqueous membrane is required to prevent boiling, temperatures below 100°C are necessary [6], [Pg.155]


The iaterpretation of the spectroscopy of SBSL is much less clear. At this writing, SBSL has been observed primarily ia aqueous fluids, and the spectra obtained are surprisiagly featureless. Some very interesting effects are observed when the gas contents of the bubble are changed (39,42). Furthermore, the spectra show practically no evidence of OH emissions, and when He and Ar bubbles are considered, continue to iacrease ia iatensity even iato the deep ultraviolet. These spectra are reminiscent of blackbody emission with temperatures considerably ia excess of 5000 K and lend some support to the concept of an imploding shock wave (41). Several other alternative explanations for SBSL have been presented, and there exists considerable theoretical activity ia this particular aspect of SBSL. [Pg.260]

The fuels Hsted in Table 2 are generally representative of fuels to be encountered over the range of industrial furnaces and, depending on the type (cooled or refractory wall), exhibit operating temperatures considerably different from adiabatic values. The choice of fuel is dependent upon a number of factors including cost, availabiUty, cleanliness, emissions, reflabiUty, and operations. Small furnaces tend to bum cleaner, easier to use fuels. Large furnaces can more effectively use coal. [Pg.142]

The temperature dependence of melt viscosity at temperatures considerably above T approximates an exponential function of the Arrhenius type. However, near the glass transition the viscosity temperature relationship for many polymers is in better agreement with the WLF treatment (24). [Pg.173]

In selecting the boiling temperature, consideration must be given to the effect of temperature on heat-transfer characteristics of the type of evaporator to be used. Some evaporators show a marked drop in coefficient at low temperature—more than enough to offset any gain in available temperature difference. The condenser cooling-water temperature and cost must also be considered. [Pg.1145]

The classical value is attained by most molecules at temperatures above 300 K for die translation and rotation components, but for some molecules, those which have high heats of formation from die constituent atoms such as H2, die classical value for die vibrational component is only reached above room temperature. Consideration of the vibrational partition function for a diatomic gas leads to the relation... [Pg.110]

PVC on its own is extremely heat- and shear-sensitive and cannot be processed into finished goods, as it starts degrading at temperatures considerably lower than those required to process it. The processing of PVC requires a number of additives. These include heat stabilizers, impact modifiers, processing aids, and lubricants. [Pg.318]

Now at temperatures considerably less than TK, a increases with T, hence at some intermediate temperature it must pass through a maximum. If there is also a point of inversion from — to -f- at lower temperatures (e.y., chloroform at 127°) there are therefore two points of inversion for cr" if there is no such point there is probably always the one at the critical temperature. [Pg.188]

The compound in Fig. 3b exhibits two smectic phases (Sm and Sm ) in addition to nematic, whereas the compound in Fig. 3a exhibits only a nematic phase. The substitution of an alkoxy for an alkyl tail is known to shift phase transition temperatures considerably. In the cyano-biphenyls (Fig. 4), substitution of an alkoxy tail raises the melting point from 24 to 48 °C and T from 35 to 68 °C [22]. [Pg.8]

Many contaminated sites are located in areas with temperatures considerably less than 15°C, and investigations into the role of temperature have therefore been carried out. Some of the cardinal results have been discussed in Chapter 4, and it may be concluded that although the rates at 4-5°C may be low, selection of organisms for adaptation to the ambient temperature will generally ensure that degradative activity is retained. There may, however, be selective degradation of specific groups of components in mixtures such as PCBs. [Pg.613]

The barriers to rotation are far too small to allow isolation of the different staggered conformations or conformers, even at temperatures considerably below rt. [Pg.147]

James Dewar observed in 1894 phosphorescence from frozen solutions utilizing liquid air [5], Jean Becquerel discovers in 1907 that samples frozen at liquid air temperatures considerably narrow the spectral shape and increased information is obtained from the luminescence spectra [26],... [Pg.9]

Heat-sensitive or water-immiscible compounds are purified by steam distillation at temperatures considerably lower than their usual boiling temperatures. [Pg.230]

The containers are held at the required test temperature by placing in a single cabinet oven. For tests at temperatures considerably below the boiling point of the liquid, the container is simply stoppered, but for temperatures near the boiling point the container can be fitted with a reflux condenser to minimise evaporation. The standard notes the need to stir the liquid and/or replace it at intervals depending on its stability. [Pg.66]


See other pages where Temperature Considerations is mentioned: [Pg.1913]    [Pg.330]    [Pg.838]    [Pg.330]    [Pg.85]    [Pg.186]    [Pg.16]    [Pg.67]    [Pg.308]    [Pg.233]    [Pg.109]    [Pg.2190]    [Pg.481]    [Pg.937]    [Pg.1032]    [Pg.431]    [Pg.362]    [Pg.838]    [Pg.381]    [Pg.429]    [Pg.17]    [Pg.317]    [Pg.241]    [Pg.214]    [Pg.37]    [Pg.193]    [Pg.115]    [Pg.137]    [Pg.433]    [Pg.391]    [Pg.85]    [Pg.70]    [Pg.395]    [Pg.206]    [Pg.50]   


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Material and Engineering Considerations at Application Temperatures

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Modulated temperature theoretical considerations

Oven temperature control considerations

Painting temperature considerations

Temperature and Energy Considerations in Tubular Reactors

Temperature profile selectivity considerations

Temperature profile thermodynamic considerations

Time-temperature considerations

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