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Gas limitations

When the temperaPire is high and the density is low, one expects to recover the classical ideal gas limit. The number of particles is still given by N = Thus the average number of particles is given by equation... [Pg.426]

The part of the mainland within the area covered by the investigation is not rcsidcniial. hui primarily industrial. The two large oil refineries belonging to Shell UK Oil and Mobil Oil Coinpany Limited are located on the riverside. The liquefied petroleum gases cylinder (LPG) filling plant of C.ilor Gas Limited is north of the refineries. Fisons Limited s ammonium nitrate plant i in i c cstern part of the area. [Pg.429]

Calor Gas Limited, Coryton occupies a small site employing about 100 people to fill cylinders with LPG which is supplied by pipelines from both of the nearby refineries and stored in it.s seven tanks 350 tonnes total capacity. Large numbers of portable cylinders of all sizes, full and empty, are on the site totalling about 500 tonnes of LPG. These are transported by road gases are transported in tank trucks. [Pg.430]

In general, pneumatic systems are less expensive to manufacture and operate, but there are factors that prohibit their universal application. The compressibility of air, as any gas, limits the operation of pneumatic systems. For example, a pneumatic cylinder cannot maintain... [Pg.583]

One can define intrinsic binding constants in the same way as before, e.g., Eq. (2.2.25), but now these constants will depend on the ligand concentration C. The relation (D.4) gives an implicit dependence of the absolute activity A = exp(Pp) on the ligand concentration C. However, since the analytical dependence of G on C is not known, one cannot write the explicit function A = A(C). This may be done to first order in C. Note that when C — 0 the integral on the rhs of Eq. (D.4) is zero, and we have the ideal gas limit of the chemical potential. If we expand the integral to first order in C, we obtain the first-order deviation with respect to an ideal gas. [Pg.318]

Note that at C = 0, p = -. Here, we need only the limiting behavior when CG 1. This is the ideal gas limit... [Pg.318]

As mentioned previously, because of its unique chemistry, ZSM-5 produces less wet gas per octane gain than increasing riser top temperature (Figure 7). This happens because ZSM-5 does not increase Cg" yields. Thus, using ZSM-5 allows the refiner to reoptimize FCC conditions to again reach a wet gas limit. [Pg.79]

The fact that the species transferred across the sensor membrane (the analyte or reaction product) must be a gas limits application of this type of flowthrough sensor, which, however, is still more versatile than are the sensors based on integrated separation (gas diffusion) and detection [4] described in Section 4.2 in fact, while these latter can only exploit physico-chemical properties of the analytes transferred, sensors based on triple integration allow the implementation of a (bio)chemical reaction and formation of a reaction product, so they are applicable to a much wider variety of systems with adequate sensitivity and selectivity. [Pg.262]

Read SJ, Hirano T, Davis SM, Donnan GA. Limiting neurological damage after stroke. A review of pharmacological treatment options. Drugs Aging 1999 14 11-39. [Pg.706]

Failing to identify the limiting reactant can lead to failure in the scale-up of trickle-bed reactors (Dudukovic, 1999). Gas-limited reactions occur when the gaseous reactant is slightly soluble in the liquid and at moderate operating pressures. For liquid-limited reactions, concurrent upflow is preferred (packed bubble columns) as it provides for complete catalyst wetting and thus enhances the mass transfer from the liquid phase to the catalyst. On the other hand, for gas reactions, concurrent downflow operation (trickle-bed reactors), especially at partially wetted conditions, is preferred as it facilitates the mass transfer from the gas phase to the catalyst. The differences between upflow and downflow conditions disappear by the addition of fines (see Section 3.7.3, Wetting efficiency in trickle-bed reactors). [Pg.540]

In the broad vicinity of the low-pressure (or ideal gas) limit, induced spectra may also be represented in the form of of a virial expansion,... [Pg.5]

In fact, Joule s experiment is not sufficiently accurate to detect the actual (small) value of (dU/dV)T for real gases at near-ambient conditions. However, it will later be proven (Sidebar 5.6) that the vanishing of (dU/dV)T becomes exact in the ideal gas limit,... [Pg.92]

Claim The Kelvin scale TK as defined by (4.19) agrees with the ideal scale Tl based on the ideal gas limit. [Pg.131]

The first term on the right-hand side is the idea gas limit, and the remaining -logarithmic terms express the successive virial corrections for the real gas behavior. It is evidently most convenient for this problem to choose the standard state pressure as P° = 0, where all gases are ideal. With this choice, we can write the relationship between fugacity and pressure as... [Pg.183]

Table 11.2. For comparison, we also include values for the (physically unrealistic) monatomic ideal gas limit, as previously described in Sidebar 11.3. Table 11.2. For comparison, we also include values for the (physically unrealistic) monatomic ideal gas limit, as previously described in Sidebar 11.3.
Note that in the above, performance and properties all refer to the gas, which is appropriate when dealing with a gas-limited transfer process. [Pg.89]

Gas Limits in Air, by Volume Minimum of Diluent Required to Make Mixture Nonflammable in All Proportions ... [Pg.11]

Dynamic tracer tests can be used to determine dynamic holdup and catalyst contacting which in trickle-flow regime can be correlated with Reynolds and Gallileo number. A simple reactor model for gas limiting reactant when matched to experimental results for one solvent and one catalyst activity predicts reactor performance well for different catalyst activities and in other solvents over a wide range of liquid velocities. [Pg.435]

Film growth is under oxygen-rich conditions so the films are stoichiometric. The high partial pressure of the reactive gas limits the surface mobility, so film properties are not ideal. Furthermore, dopants are oxidized and thus, TCO films become non-conductive. [Pg.199]

Rather than think in terms of joining the two formulations in the dilute-gas limit, it is possible to reduce the general form to one that superficially looks like that limit. Recall that when retardation and magnetic susceptibilities are ignored the Lifshitz result (omitting magnetic terms) becomes... [Pg.212]


See other pages where Gas limitations is mentioned: [Pg.428]    [Pg.483]    [Pg.159]    [Pg.138]    [Pg.1402]    [Pg.2492]    [Pg.436]    [Pg.181]    [Pg.406]    [Pg.41]    [Pg.22]    [Pg.184]    [Pg.5]    [Pg.15]    [Pg.160]    [Pg.79]    [Pg.80]    [Pg.13]    [Pg.14]    [Pg.182]    [Pg.540]    [Pg.249]    [Pg.32]    [Pg.583]    [Pg.1233]    [Pg.67]    [Pg.91]    [Pg.461]    [Pg.292]    [Pg.107]   
See also in sourсe #XX -- [ Pg.217 ]




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