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Distributor quality

B = distributor quality factor C = vapor capacity factor... [Pg.264]

General Generally, from a macroscopic point of view, maldistribution can be divided into two different phenomena (Stanek, 1994). The first one is small-scale maldistibution, which is connected mainly to the so-called preferred paths. It is the case where the liquid follows specific paths through bed and travels with velocities considerably higher than the mean. The same phenomenon is characterized as chaneling. The second case is large-scale maldistribution, which is connected to the nonhomogeneous (nonunifonn) initial distribution of the liquid and is referred to as wall effects. The concepts of distributor quality and liquid maldistribution in fixed beds are frequently found in the related technical literature, and these concepts are connected to each other—the better die distributor quality, the better the liquid distribution and flow into bed (Klemas and Bonilla, 1995). [Pg.158]

The distributor quality DQ, is expressed as the portion (%) of the fixed-bed cross-sectional area (inlet surface), which is homogeneously wetted by the liquid. The initial maldistribution in the bed inlet (Mdo) is a statistical average of the mass flow rate standard deviation divided by the free surface in the bed inlet. These parameters are related as follows (Klemas and Bonilla, 1995) ... [Pg.158]

For example, for a distributor quality of 90-95%, the initial maldistribution is 23-33%. This means that the distributor should have excellent quality to lead to a good initial liquid... [Pg.158]

Liquid distribution in a packed bed is a function of the internal vapoi/liquid traffic, the type of packing employed, and the quality of the liquid distributors mounted above the packed bed. Vapor distribution is controlled by the internal vapor/liquid traffic, by the type of packing employed, and by the quality of the vapor distributors located below the packed beds. [Pg.145]

The use of V-notches in a trough wall for overflow is more sensitive to leveling problems than the other designs, and for the same %- to Me-in. level tolerance produces a more severe non-uniform flow distribution. The quality of distribution from a V-notch is poor compared to the other types of trough distributor, but does have advantages in slurry systems [131]. It should not be used for critical distillation applications, but is good for heat transfer and where solids are in the system. [Pg.265]

The quality grading system relates to uniformity of distribution across the tower cross-section, where 100% quality indicates ideal uniform distribution. Distributors are designed to suit the system, particularly the packing type and size. [Pg.268]

The type of distribution to select depends on the sensitivity of the tower performance to the liquid distribution as discussed earlier. Norton s [83] data indicate that the sensitivity of tower performance to liquid distribution quality depends only on the number of theoretical stages in each bed of packing achierable at its System Base HETP [83]. Tower beds of high efficiency packing are more sensitive to liquid distribution quality than shorter beds of medium efficiency packing [83]. It is important to extend the uniformity of the distributor all the way to within one packing particle diameter of the tower wall [85]. [Pg.268]

Figure 9-10. Effect of liquid maldistribution on efficiency FRI data for 25-mm Pall rings in cyciohexane/n-heptane distillation with two different quality distributors. Used by permission of the American Institute of Chemical Engineers, Chemical Engineering Progress, Perry, D. and Nutter, ., Jan. (1990) p. 30, and by special permission of Fractionation Research, Inc., all rights reserved. Figure 9-10. Effect of liquid maldistribution on efficiency FRI data for 25-mm Pall rings in cyciohexane/n-heptane distillation with two different quality distributors. Used by permission of the American Institute of Chemical Engineers, Chemical Engineering Progress, Perry, D. and Nutter, ., Jan. (1990) p. 30, and by special permission of Fractionation Research, Inc., all rights reserved.
PSD is an important indicator of the fluidization characteristics of the catalyst, cyclone performance, and the attrition resistance of the catalyst. A drop in fines content indicates the loss of cyclone efficiency. This can be confirmed by the particle size of fines collected downstream of the cyclones. An increase in fines content of the E-cat indicates increased catalyst attrition. This can be due to changes in fresh catalyst binder quality, steam leaks, and/or internal mechanical problems, such as those involving the air distributor or slide vah es. [Pg.107]

A fundamental problem that occurs even in fully industrialized countries and large international companies, is that whereas many smaller boiler plant managers purchase well-designed and efficient boilers, pumps, and auxiliaries from recognized quality manufacturers and distributors, the design and construction of FW tanks and even the overall boiler house system may be placed in the hands of persons with inadequate training and experience. [Pg.110]

Areas for the manufacture of sterile products are classified according to the required characteristics of the environment. Each manufacturing operation requires an appropriate level of microbial and particulate cleanliness four grades (Table 22.1) are specified in the Rules and Guidance for Pharmaceutical Manufacturers and Distributors (1997), defined by measures of airborne contamination (Table 22.2). Environmental quality is substantially influenced by the air supplied to the manufacturing environment. [Pg.432]

Rules and Guidance for Pharmaceutical Manufacturers and Distributors (1997) London HMSO. Spooner D.F. (1996) Hazards associated with the microbiological contamination of cosmetics, toiletries andnon-sterile pharmaceuticals. Iw.Microhial Quality Assurance in Cosmetics, Toiletries andNon-sterile Pharmaceuticals, 2nd edn (eds R.M. Baird S.F. Bloomfield), pp. 9-27. London Taylor Francis. [Pg.438]

Distributors and wholesalers may act as middlemen, moving raw products from the farmer to the processor or manufacturer, or moving processed food to retailers. They will have information on how much is needed by the manufacturer and what quality. Brokers may also do the marketing and check that stores properly present your product. [Pg.136]

Good distribution of gas over the whole cross-section of the bed may often be difficult to achieve, although this is enhanced by ensuring that the pressure drop across the distributor is large compared with that across the bed of particles. In general, the quality of gas distribution improves with increased flowrate because the pressure drop across the... [Pg.315]

Add multiple bed density taps to the regenerator to determine quality of fluidization and identify a damaged or partially plugged air distributor... [Pg.96]


See other pages where Distributor quality is mentioned: [Pg.264]    [Pg.265]    [Pg.265]    [Pg.158]    [Pg.64]    [Pg.264]    [Pg.265]    [Pg.265]    [Pg.158]    [Pg.64]    [Pg.261]    [Pg.34]    [Pg.34]    [Pg.557]    [Pg.364]    [Pg.40]    [Pg.42]    [Pg.44]    [Pg.9]    [Pg.31]    [Pg.16]    [Pg.139]    [Pg.293]    [Pg.320]    [Pg.216]    [Pg.9]    [Pg.130]    [Pg.225]    [Pg.67]    [Pg.84]    [Pg.295]    [Pg.186]    [Pg.187]    [Pg.81]    [Pg.87]   
See also in sourсe #XX -- [ Pg.158 ]

See also in sourсe #XX -- [ Pg.158 ]




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