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Pressure minimization

We have seen that equilibrium in an isolated system (dt/= 0, dF= 0) requires that the entropy Sbe a maximum, i.e. tliat dS di )jjy = 0. Examination of the first equation above shows that this can only be true if. p. vanishes. Exactly the same conclusion applies for equilibrium under the other constraints. Thus, for constant teinperamre and pressure, minimization of the Gibbs free energy requires that dGId Qj, =. p. =... [Pg.362]

I, ow gas velocity and pressure minimizes the tendene y towtirds current cho]iping,... [Pg.643]

Finally, the use of the constant pressure minimization algorithm allows searching for phenomena that can be considered as precursors of pressure-induced transitions. For example, the predicted behaviour of the anatase cell constants as a function of pressure shows that the a(P) and c(P) plots are only linear for P<4 GPa, the value that is close to both the theoretical and experimental transition pressures. At higher pressures the a constant starts to grow under compression, indicating inherent structural instability. In the case of ratile there is a different precursor effect, nami y at 11 GPa the distances between the titanium atom and the two different oxygens, axial and equatorial, become equal. Once again, the pressure corresponds closely to the phase transition point. [Pg.22]

Operating the column at the minimum pressure minimizes the energy cost of separation. Towering this pressure increases the relative volatility of distillation components and thereby increases the capacity of the reboiler by reducing operating temperature, which also results in reduced fouling. Reducing pressure also affects other parameters, such as tray efficiencies and latent heats of vaporization. [Pg.244]

These two main fields of application for chromatography result of course in a dissimilar approach to selecting the chromatographic system. If time pressure minimizes the possible number of experiments the use of generic gradient systems (Section 4.3.1.3) is recommended. In such cases solubility problems are also important,... [Pg.124]

The first stage of any lattice simulation is to equilibrate the structure, i.e. bring it to a state of mechanical equilibrum. The simplest procedure is to equilibrate under conditions of constant volume, i.e. with invariant cell dimensions. Extensions to the procedure were introduced by Parker (1982, 1983) who introduced the use of constant pressure minimization in the computer code METAPOCS, in which lattice energy minimization was performed with respect... [Pg.59]

The basis of constant pressure minimization is that both lattice vectors and coordinates are adjusted to remove forces on both the atoms and the unit cell as a whole. This is commonly performed simultaneously, using the same approach for the lattice vectors as was used in constant volume minimization for the coordinates (i.e. treating the lattice vectors as additional variables). [Pg.60]

Betai receptor-preferring adrenergic agonist. At moderate dose, increases contractility without increasing heart rate or blood pressure. Minimal effect on blood vessels. [Pg.62]

It is not always possible to elevate the liquid level fed to the extrusion head mandrel and escape high hydrostatic pressure (see Fig. 2.5e) lest the hose should rupture. To avoid this, the Cl is applied on the hose wall during rotation [98]. The liquid vortex formed this way promotes the required level of the liquid on the mandrel near the hose surface, making use of a minimum amount of Cl and changing the rotation velocity of the hose. The dynamic interaction of the hose and the Cl intensifies its diffusion into the polymer material, breaks the vapor jacket at the inhibitor-hose interface and facilitates the uniform distribution of Cl pressure, minimizing the probability of hose rupture. [Pg.119]

Not all ceramic compounds are put through single-screw and twin-screw extruders. If the idea is to achieve very high extrusion pressures, minimal contamination, short series, etc., an intermittent piston extruder can be the machine of choice. [Pg.8]

Gas-liquid plus catalytic solid Use when (i) the reaction occurs in the liquid phase (in the presence or not of homogeneous catalyst) or at the catalyst interface (ii) temperatures and pressures for reaction are consistent with distillation conditions (iii) reactions are reversible equilibrium not irreversible (iv) not for supercritical, gas phase reactions, or solid reactants or products, high temperatures or pressures. Minimizes catalyst poisoning, lower pressure than fixed bed. Used for hydrogenation reactions and MTBE and acrylamide production. For example, 90% conversion via reactive distillation contrasted with 70% conversion in fixed bed option. [Pg.277]

Distillation column controls combined with pressure minimization and flash zone temperature control to maintain yields of the most valuable products while minimizing energy use in reboiling or feed heater... [Pg.56]

Integrated arrangement, self-pressurization, minimization of in-vessel penetrations and their location at the upper part of the RPV. [Pg.260]

Ceramic RA. The dust is collected by high-velocity impingement in a fluid which wets clay particles well and has a low vapour pressure minimizing evaporation over the sampling period of a week. Annals Occup. Hyg. 9 (1) 29 1966). [Pg.145]

There are many types of combustion chamber designs which manufacturers use to mix fuel and air. There are claimed advantages for each type. These may be fuel economy, ability to make use of simpler fuel systems, wide speed-range coverage, or firing pressure minimization. These systems generally fan into an open-chamber (Fig. 6.90) or divided-chamber (Fig. 6.91) category. [Pg.995]

In analytical systems for instance, the objective is to identify components present in a small sample volume consequently these systems must be able to accommodate highly efficient columns containing very small particle diameter packings producing high column back pressures. Minimal volume in pipework, valves, and detector flow cells are required and a large emphasis is placed on data handling with automatic calculation of peak areas for concentration determination. There is no requirement for a fraction collector. [Pg.1]

Minimize cooling time Minimize maximum injection pressure Minimize volumetrical shrinkage... [Pg.1896]


See other pages where Pressure minimization is mentioned: [Pg.123]    [Pg.229]    [Pg.204]    [Pg.204]    [Pg.202]    [Pg.60]    [Pg.226]    [Pg.56]    [Pg.68]    [Pg.196]    [Pg.12]    [Pg.261]    [Pg.320]    [Pg.660]    [Pg.677]    [Pg.311]    [Pg.75]    [Pg.736]    [Pg.141]    [Pg.112]    [Pg.161]    [Pg.595]    [Pg.81]   


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