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Flow limitation

The compressors operating range is between two major regions as seen in Fig. 10-74, which is a performance map of a centrifugal compressor. These two regions are. surge, which is the lower flow limit of... [Pg.925]

Eveiy effort should be made to eliminate direct (Bourdon-type) pressure gauges. Diaphragm pressure gauges constructed of appropriate corrosion-resistant materials are preferred. Flow limiters should be used to limit flow in case of loss of integrity... [Pg.2309]

Downcomers sized too small for actual flow. Limited capacity. Design error. [Pg.300]

The charging current is therefore roughly proportional to the square of (ucO, the velocity-diameter product. An important outcome is that the velocity-diameter product can be used to characterize charging current in pipe flow and as a basis for setting flow limits when filling tanks (5-4). [Pg.108]

This is a low value, therefore, the possibility exists of an up-rate relative to any nozzle flow limits. At this point, a comment or two is in order. There is a rule of thumb that sets inlet nozzle velocity limit at approximately 100 fps. But because the gases used in the examples have relatively high acoustic velocities, they will help illustrate how this limit may be extended. Regardless of the method being used to extend the velocity, a value of 150 fps should be considered maximum. When the sonic velocity of a gas is relatively low, the method used in this example may dictate a velocity for the inlet nozzle of less than 100 fps. The pressure drop due to velocity head loss of the original design is calculated as follows ... [Pg.39]

Define flow limits and degree of aquifer confinement... [Pg.120]

The liquid bulk flow limits the upward flow of small particles from the internal side and has a significant influence on the separating effect. Hydroclones are applied successfully for classification, clarification and thickening of suspensions containing particles from 5 to 150 tm in size. [Pg.539]

Hsieh and McNulty [210] developed a new correlation for weeping of sieve and valve trays based on experimental research and published data. For sieve trays the estimation of the weeping rate and weep point is recommended using a two-phase countercurrent flow limitation model, CCFL. [Pg.184]

The studies of Diehl and Koppany further examined vertical up-flow limitations. [Pg.133]

Airway wall fibrosis, thickening + Flow limitation... [Pg.363]

Flow limitations restrict application of the DFI interface for pSFC-MS coupling. pSFC-DFI-MS with electron-capture negative ionisation (ECNI) has been reported [421], The flow-rate of eluent associated with pSFC (either analytical scale - 4.6 mm i.d. - or microbore scale 1-2 mm, i.d.) renders this technique more compatible with other LC-MS interfaces, notably TSP and PB. There are few reports on workable pSFC-TSP-MS couplings that have solved real analytical problems. Two interfaces have been used for pSFC-EI-MS the moving-belt (MB) [422] and particle-beam (PB) interfaces [408]. pSFC-MB-MS suffers from mechanical complexity of the interface decomposition of thermally labile analytes problems with quantitative transfer of nonvolatile analytes and poor sensitivity (low ng range). The PB interface is mechanically simpler but requires complex optimisation and poor mass transfer to the ion source results in a limited sensitivity. Table 7.39 lists the main characteristics of pSFC-PB-MS. Jedrzejewski... [Pg.482]

Figure 2 Individual organ representations for a three-subcompartment (A), two-subcompartment (B), or typical membrane-linked and blood flow-limited (C) physiologically based pharmacokinetic model. See text for definition of symbols. Figure 2 Individual organ representations for a three-subcompartment (A), two-subcompartment (B), or typical membrane-linked and blood flow-limited (C) physiologically based pharmacokinetic model. See text for definition of symbols.
The three-compartment tissue model is ordinarily simplified by lumping all three subcompartments, lumping subcompartments 1 and 2, or lumping subcompartments 2 and 3. These simplifications result in the blood flow-limited (i.e., lumping all three subcompartments) and the membrane-limited (i.e., lumping any two subcompartments) tissue models. Differential mass balance equations for a noneliminating membrane-limited compartment are... [Pg.81]

Lumping compartments 1, 2, and 3 into a single homogeneous tissue compartment implies the blood flow-limited model. The tissue mass balance equation for a noneliminating organ is... [Pg.82]

A complete or global tissue distribution model consists of individual tissue compartments connected by the blood circulation. In any global model, individual tissues may be blood flow-limited, membrane-limited, or more complicated structures. The venous and arterial blood circulations can be connected in a number of ways depending on whether separate venous and arterial blood compartments are used or whether right and left heart compartments are separated. The two most common methods are illustrated in Figure 3 for blood flow-limited tissue compartments. The associated mass balance equations for Figure 3A are... [Pg.83]

Tissue volumes may be expressed in mass or volume units. When volume units are used, a tissue density of 1 is normally assumed. Predicted concentrations from a blood flow-limited compartment may be compared directly to observed values. [Pg.88]

Chen and Gross [48] derived equations to calculate partition coefficients for blood flow-limited compartments from either constant rate infusion (i.e., steady-state conditions) or intravenous bolus regimens. For a noneliminating organ under steady-state conditions,... [Pg.93]

Gallo et al. [49] developed the area method for calculation of partition coefficients for both blood flow-limited and membrane-limited compartments. [Pg.93]

Following intravenous bolus administration, the partition coefficients for a noneliminating blood flow-limited compartment is... [Pg.94]

Distinguishing Between Blood Flow-Limited and Membrane-Limited Organ Models... [Pg.97]

With these observations in mind, the simplest practical measure to reduce electrostatic discharge risks associated with vessel loading is to reduce the rate at which the dry solids are added to the vessel. This approach works because the slower rate of flow provides an opportunity for accumulating charge to relax away by various mechanisms before hazardous conditions become established. Often, the same type of flow limitation is effective in reducing the likelihood of ESD during vessel unloading. In many cases, the maximum safe rate of inflow (or outflow) has to be determined by empirical means. [Pg.856]

Process simulators contain the model of the process and thus contain the bulk of the constraints in an optimization problem. The equality constraints ( hard constraints ) include all the mathematical relations that constitute the material and energy balances, the rate equations, the phase relations, the controls, connecting variables, and methods of computing the physical properties used in any of the relations in the model. The inequality constraints ( soft constraints ) include material flow limits maximum heat exchanger areas pressure, temperature, and concentration upper and lower bounds environmental stipulations vessel hold-ups safety constraints and so on. A module is a model of an individual element in a flowsheet (e.g., a reactor) that can be coded, analyzed, debugged, and interpreted by itself. Examine Figure 15.3a and b. [Pg.518]

Ingram, R.H., Wellman, J.J., McFadden, E.R., Jr. and Mead, J. (1977). Relative contributions of large and small airways to flow limitation in normal subjects before and after atropine and isoproterenol. J. Clin. Invest. 59 696-703. [Pg.361]


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See also in sourсe #XX -- [ Pg.4 , Pg.9 ]




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