Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Flow Relationships

These relationships are concerned with the flow between two or more units/ items. For example, the flow between two units/items may involve steam, water, electrical energy, fuel, air, or lubricating oil. Furfhermore, the flow could also be unconfined, such as heaf radiation from one body/unit/item to another. The problems experienced with many products quite often include the proper flow of fluids and energy from one ifem/unif to another item/ unit through confined passages, consequenfly leading to safety-related problems. [Pg.64]

The causes of flow-related problems include complete or partial interconnection failure and faulfy cormections between units/items. In regard to fluids, the factors that must be considered with care from fhe safefy aspect include loss of pressure, confaminafion, flammabilify, lubridfy, odor, and toxicity. [Pg.64]


The power-steam flow relationship in Figure 23.10b can be represented over a reasonable range by a linear relationship, as shown in Figure 23.10c7-9. The straight-line relationship is given by7-9 ... [Pg.473]

For greater concentrations of fine particles the suspension is more likely to be non-Newtonian, in which case the viscous properties can probably be adequately described by the power law or Bingham plastic models. The pressure drop-flow relationship for pipe flow under these conditions can be determined by the methods presented in Chapters 6 and 7. [Pg.449]

Dillard RL, Eastman H, Fordtran JS. Volume-flow relationship during the transport of fluid through the human small intestine. Gastroenterology 1965 49(1) 58—66. [Pg.188]

Studies by Sedlak (j6) have shown a similar response-flow relationship for liquid electrolyte cells which utilize a teflon-bonded diffusion electrode. The empirical equations and relationships derived generally apply to the SPE sensor cells. [Pg.564]

Grigull (G8), 1942 Treatment of heat transfer in condensate film on vertical surface, assuming applicability of Prandtl pipe-flow relationships. Comparison with experimental data,... [Pg.213]

But any theory based entirely on surface decompn is,however, incomplete because it fails to consider the overall surface structure with the accompanying heat flow relationships... [Pg.214]

Liquid flow relationships Mass balances around the 1th tray (where 1 = 2,..., N - 1, i f) N... [Pg.574]

Anderson, H.A., Hepburn, A., Miller, J.D., Stewart, M., Ferrier, R.C. and Walker, TA.B. (1990) Humic substances of surface waters. Litter and soil through flow relationships in two forested ecosystems. Anal. Chim. Acta, 232, 3-10. [Pg.128]

The Eulerian continuum approach, based on a continuum assumption of phases, provides a field description of the dynamics of each phase. The Lagrangian trajectory approach, from the study of motions of individual particles, is able to yield historical trajectories of the particles. The kinetic theory modeling for interparticle collisions, extended from the kinetic theory of gases, can be applied to dense suspension systems where the transport in the particle phase is dominated by interparticle collisions. The Ergun equation provides important flow relationships, which are useful not only for packed bed systems, but also for some situations in fluidized bed systems. [Pg.164]

Before closing this chapter, we feel that it is useful to list in tabular form some isothermal pressure-flow relationships commonly used in die flow simulations. Tables 12.1 and 12.2 deal with flow relationships for the parallel-plate and circular tube channels using Newtonian (N), Power Law (P), and Ellis (E) model fluids. Table 12.3 covers concentric annular channels using Newtonian and Power Law model fluids. Table 12.4 contains volumetric flow rate-pressure drop (die characteristic) relationships only, which are arrived at by numerical solutions, for Newtonian fluid flow in eccentric annular, elliptical, equilateral, isosceles triangular, semicircular, and circular sector and conical channels. In addition, Q versus AP relationships for rectangular and square channels for Newtonian model fluids are given. Finally, Fig. 12.51 presents shape factors for Newtonian fluids flowing in various common shape channels. The shape factor Mq is based on parallel-plate pressure flow, namely,... [Pg.735]

Characteristic Curves. The pressure head versus flow relationship for a centrifugal pump, called the characteristic curve, and illustrated in Figure 13, depends very much upon the design of the impeller, its vanes and the volute casing. [Pg.78]

Branston NM, Strong AJ, Symon L (1977) Extracellular potassium activity, evoked potential and tissue blood flow. Relationships during progressive ischaemia of baboon cerebral cortex. J Neurol Sci 32 305-321... [Pg.68]

The forces can be controlled in various ways to find a proper pathway leading to quasi-linear force-flow relationships so that the theory of linear nonequilibrium thermodynamics can be applied. For a first-order reaction S -> P, doubling the concentrations of S and P will double the reaction rate for an ideal system, although the affinity remains the same, and a distinction must be made between thermodynamic and kinetic linearity. Proper pathways are associated with thermodynamic linearity. The rate of a process depends not only on the force but also on the reference state the flow of a solute across a membrane depends on its chemical potential and on its thermodynamic state on both sides of the membrane. [Pg.557]

Both axial and centrifugal compressors are subject to an unstable region of low flow operation called surge. This region is defined by the pressure-flow relationship which has a peak determined by the operating speed. For various compressor speeds, these peaks may be connected to determine a surge line, which defines a region of unstable operation at lower flows. [Pg.56]

When air is absent in the pores and the pore diameter is substantially greater than the mean free path, X, of the diffusing water molecules (distance traveled between collisions with other molecules), water molecules collide more frequently with each other than with the pore walls and the Poiseuille flow relationship applies. The mean free path can be calculated using Eq. (7), where kb is the Boltzmann constant and a is the collision diameter of the water molecule. However, for pore diameters in the range of membranes that are suitable for OD applications and for a gas-phase pressure attributable to water vapor alone at ambient temperature (approximately 20 mm Hg, 2.7 kPa), the mean free path is significantly greater than the pore diameter. This results in more frequent collisions of the water molecules with the pore walls than with each other, and Knudsen diffusion predominates. [Pg.1987]

Fig. 7 Materials flow relationship. (A) Relationship of component section-process-structure-product-performance. (B) schematic of a flat laminate sheet production process. (From Ref. °l)... Fig. 7 Materials flow relationship. (A) Relationship of component section-process-structure-product-performance. (B) schematic of a flat laminate sheet production process. (From Ref. °l)...
Generally, the permeability Bq rn ) has to be determined experimentally. However, for simple structures the permeability coefficient Bq can be determined analytically. Considering a cylindrical pore, for example, the permeability can be calculated from the Poiseuille flow relationship Bo = dg/32 [49]. [Pg.308]

A subgraph of a dynamic task net (partial abstraction) This subgraph represents a fragment of a dynamic task net which is structurally and behaviorally consistent with respect to the process meta-model of DYNAMITE [243]. Zero or more tasks can be part of the process view and not all of a task s parameters need to be in the process view. Only a subset of the existing flow relationships between tasks needs to be represented in the process view. [Pg.339]

View definition rules A set of rules defines which elements of the underlying private process are also part of the process view. For instance, some specific model elements (i.e. tasks, products, resources, or flow relationships) can be assigned to the view, or all model elements of a specific type can be chosen instead. [Pg.339]

Relationships defined in CLiP models can be reflected in class diagrams by introducing new associations between classes. Currently, this is not possible in our approach, as only a limited set of default associations has been implemented to connect classes, like associations denoting control flow relationships or data flow relationships. We use UML stereotypes to define the type of an association link between two classes. Up to now, other relationships, e.g., those with a more semantical character, are neglected, although their integration is easily possible by simply using additional UML stereotypes as annotations for associations. [Pg.625]


See other pages where Flow Relationships is mentioned: [Pg.2265]    [Pg.2347]    [Pg.226]    [Pg.480]    [Pg.480]    [Pg.235]    [Pg.120]    [Pg.120]    [Pg.255]    [Pg.543]    [Pg.607]    [Pg.311]    [Pg.170]    [Pg.73]    [Pg.480]    [Pg.480]    [Pg.489]    [Pg.98]    [Pg.2102]    [Pg.235]    [Pg.252]    [Pg.334]    [Pg.1626]    [Pg.397]    [Pg.308]    [Pg.336]    [Pg.357]   


SEARCH



Calculation of flow rate-pressure drop relationship for

Flow of fluids — energy and momentum relationships

Flow rate-pressure drop relationship

Flow-force relationships

Melt Flow load relationship

Melt Flow temperature relationship

Melt Flow viscosity relationship

Overall relationship between mass flow and pressure difference

Pressure Drop-Flow Relationship

Pressure flow relationship

Relationship between relaxation time and flow diagram non-exponential decay (slowing down)

Relationship of water diffusion to osmotic flow

Rough pipe turbulent flow, relationship

Stationary-state relationship and flow diagram

Stress-strain relationship simple shear flow

© 2024 chempedia.info