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Operating cases

With the above as an introduction, we now consider the important operational case of filtration performed under constant pressure. In practice, all the parameters defined above are nearly constant under steady state conditions except V and r, which are varied by the operator. We may therefore integrate the working expression for filtration over the limits of volume from 0 to V, and for residence time over the limits of 0 to x ... [Pg.379]

It is an anionic detergent which softens the stool by water accumulation in intestinal lumen and emulsifies the colon contents. It is indicated in obstetric, habitual, geriatric, paediatric constipation or when straining is to be avoided (recent myocardial infarction, severe hypertension, post-operative cases, abdominal hernia), fissures, haemorrhoids and bed ridden patients. Dose 100-200 mg/day. [Pg.254]

The operators === (case equality) and == (case inequality) are not supported for synthesis. [Pg.27]

Figures.10 Numerical algorithm forthe monodimensional model of the membrane filtration unit. Plant operating case Constant filtrate flow rate Cp = Cp jppp. Figures.10 Numerical algorithm forthe monodimensional model of the membrane filtration unit. Plant operating case Constant filtrate flow rate Cp = Cp jppp.
From Fig. 3.15 we can note that, by analogy to the 2 bar constant pressure case, example FIS shows a new special case where we have positive and small negative values in the concentrated suspension flow rate at the plant exit. This result can be explained by the background noise in the measurement of the flow of suspension. Nevertheless, the mean value of the flow rate is small but positive. If the efficiency of the filtration at constant pressure is given by the solid concentration ratio between the exit and fresh suspensions, then, as shown in Fig. 3.13, the ratio is always lower than 2 for operation case F2/1.6. For cases FI and FIS, this ratio increases permanently, non-uniformly and attains values over 12 g/1 in the proximity of the complete clogging state. [Pg.63]

Contractions between the creation operators or the annihilation operators vanish identically because of the Fermi-Dirac statistics obeyed by electrons [cf. Eq. (43)] and as in the single-excitation operator case, contractions between creation and annihilation operators are zero, because the indices belong to disjoint sets [cf. Eq. (44)]. Hence, Eq. (62) becomes... [Pg.219]

Fielding Jr., R.C., Gibbons, D.H., Legrand, F.R, 1994. In-depth drive fluid diversion using an evolution of colloidal dispersion gels and new bulk gels An operational case history of North Rainbow Ranch Unit. Paper SPE 27773 presented at the SPE/DOE Improved Oil Recovery Symposium, Tulsa, 17-20 April. [Pg.576]

Here again, the dead volume takes up space that is not accessible. As a result, the tracer will exit early because the system volume, through which it must pass is smaller than the perfect operation case. [Pg.897]

The question may be formulated as whether it is possible to find out a coherent computational way to obtain a statistically meaningful expression for expectation values in any observable operator case. Irrespeetive of the system s observables being made either of momentum or position flmctions. Moreover, if it is possible to find out such a general way, in the expectation value general expression, the DF must be explicitly present and featuring the customary role of probability distributions as in theoretical statistics. [Pg.12]

To better appreciate the meaning of Eq. (6.22), we write in detail some elements of the overlap" matrix (7V r/) for the one-electron addition operator case (recall the definition of the occupied" and unoccupied" orbitals, 0,... [Pg.127]

Palma L, Di Lorenzo N, Guidetti B. Lymphocytic infiltrates in primary glioblastomas and recidivous gliomas. Incidence, fate, and relevance to prognosis in 228 operated cases. J Neurosurg 1978 49 854-861. [Pg.514]

Increasing the thickness of both the rhenium liner and the uranium nitride pin were required in the reactor design to meet the safety conditions. During normal operations the rhenium had a negative effect on the k-effective but was countered by the extra fuel in the core. In two of the three accident scenarios, the neutron spectrum is more thermal than during normal operation due to the addition of water to the core. For the dry sand accident case, the spectrum is faster than the normal operation case. For the accident scenarios, the extra thermal absorption of neutrons from the additional rhenium dominated the effects from the additional fissionable fuel. [Pg.46]

RUSSIA ANALYSIS OF ANOMALIES AND ABNORMAL OPERATION CASES... [Pg.117]

Numerous interlocked assemblies were designed in connection with attempts to gain control of rotational and translational motions at the molecular level, a stepping stone toward possible outstanding development. [ -As-re ards light-operated cases, a representative shuttling scheme for a rotaxane-based molecular abacus is depicted in Fig. As active components. [Pg.1438]

For cocurrent operation (case 3a in Figure 3.1) both the case design and simulation are simple. The four balance equations (3.18 through 3.21) supplemented by a suitable drying rate and heat flux equations are solved starting at inlet end of the dryer, where all boundary conditions (i.e., all parameters of incoming streams) are defined. This situation is shown in Figure 3.4. [Pg.60]

Case Study 1 is on retfofitting the vacuum system of a crude distillation column in a typical petroleum refinery. Design details for the present operation (Case 1 A) are shown in Figure 11.5. Pressure at the top of the distillation colunm is 48 torr, vacuum system suction flow rate is 8500 kg/h and discharge pressure is 865 torr. The suction stream contains 8000 kg/h of water vapour and 500 kg/h of non-condensable gases (molecular... [Pg.332]

Fig. 4.18 Plot of leaction temperatures over the instant of cooling failure without and with stop of NaOH feed for the complete feeding within 1 h (case 1 cooling failure immediately after start of operation case 2 cooling failure immediately after start of operation with stop of NaOH feed case 3 cooling failure 2,000 s after start of operation case 4 cooling failure 2,000 s after start of operation with stop of NaOH feed)... Fig. 4.18 Plot of leaction temperatures over the instant of cooling failure without and with stop of NaOH feed for the complete feeding within 1 h (case 1 cooling failure immediately after start of operation case 2 cooling failure immediately after start of operation with stop of NaOH feed case 3 cooling failure 2,000 s after start of operation case 4 cooling failure 2,000 s after start of operation with stop of NaOH feed)...

See other pages where Operating cases is mentioned: [Pg.1967]    [Pg.238]    [Pg.13]    [Pg.492]    [Pg.492]    [Pg.502]    [Pg.502]    [Pg.511]    [Pg.340]    [Pg.13]    [Pg.347]    [Pg.284]    [Pg.110]    [Pg.79]    [Pg.1725]    [Pg.61]    [Pg.65]    [Pg.67]    [Pg.315]    [Pg.131]    [Pg.20]    [Pg.79]    [Pg.180]    [Pg.1971]    [Pg.311]    [Pg.130]   
See also in sourсe #XX -- [ Pg.13 , Pg.492 , Pg.502 ]




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Worst case operating conditions

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