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Effective mean flow

The flow rate of water through the porous medium per unit total (bulk) area perpendicular to the direction of flow, the so-called specific discharge q, is related to the effective mean flow velocity in the pores along the x-axis, u, by... [Pg.1152]

Specific Discharge q, Effective Mean Flow Velocity u, and Travel Time fw for Different Flow Regimes in Groundwater System S... [Pg.1159]

Its maximum moves along x at the effective mean flow velocity, u (Eq. 24-49) ... [Pg.1162]

Explain the difference between specific discharge and effective mean flow velocity. What is effective porosity ... [Pg.1179]

You are responsible for the safe operation of a drinking-water supply system that gets its raw water from a well located close to a river. From tracer experiments you know that the effective mean flow velocity is u =3 m d l and that the distance along the streamline from the point of infiltration to the well is x = 18 m. The dispersivity of the aquifer for this distance of flow is aL = 5 m. In order to be prepared for a possible pollution event in the river you are interested in the following questions ... [Pg.1180]

Appraisal activity, if performed, is the step in the field life cycle between the discovery of a hydrocarbon accumulation and its development. The role of appraisal is to provide cost-effective information with which the subsequent decision can be made. Cost effective means that the value of the decision with the appraisal information is greater than the value of the decision without the information. If the appraisal activity does not add more value than its cost, then it is not worth doing. This can be represented by a simple flow diagram, in which the cost of appraisal is A, the profit (net present value) of the development with the appraisal information is (D2-A), and the profit of the development without the appraisal information is D1. [Pg.173]

The balanced equation for turbulent kinetic energy in a reacting turbulent flow contains the terms that represent production as a result of mean flow shear, which can be influenced by combustion, and the terms that represent mean flow dilations, which can remove turbulent energy as a result of combustion. Some of the discrepancies between turbulent flame propagation speeds might be explained in terms of the balance between these competing effects. [Pg.518]

Particle trajectories can be calculated by utilizing the modern CFD (computational fluid dynamics) methods. In these calculations, the flow field is determined with numerical means, and particle motion is modeled by combining a deterministic component with a stochastic component caused by the air turbulence. This technique is probably an effective means for solving particle collection in complicated cleaning systems. Computers and computational techniques are being developed at a fast pace, and one can expect that practical computer programs for solving particle collection in electrostatic precipitators will become available in the future. [Pg.1228]

In shear layers, large-scale eddies extract mechanical energy from the mean flow. This energy is continuously transferred to smaller and smaller eddies. Such energy transfer continues until energy is dissipated into heat by viscous effects in the smallest eddies of the spectrum. [Pg.48]

A further advantage of the plate heat exchanger is that the effective mean temperature difference is usually higher than with the tubular unit. Since the tubular is always a mixture of cross and contra-flow in multi-pass arrangements, substantial correction factors have to be applied to the log mean temperature difference (LMTD). In the plate... [Pg.397]

Miyauchi and Vermeulen (M7, M8) have presented a mathematical analysis of the effect upon equipment performance of axial mixing in two-phase continuous flow operations, such as absorption and extraction. Their solutions are based, in one case, upon a simplified diffusion model that assumes a mean axial dispersion coefficient and a mean flow velocity for... [Pg.86]

In summary, we have commented briefly on the microscopic applications of NMR velocity imaging in complex polymer flows in complex geometries, where these applications have been termed Rheo-NMR [23]. As some of these complex geometries can be easily established in small scales, NMR velocimetry and visc-ometry at microscopic resolution can provide an effective means to image the entire Eulerian velocity field experimentally and to measure extensional properties in elastic liquids non-invasively. [Pg.415]

Figure 7.8 The effect of flow of scC02 on the recovery of Irganox 1010 from PP by means of SFE (temperature 120 °C modifier, 2% MeOH). After Thil6n and Shishoo [12]. Reprinted from M. Thil6n and R. Shishoo, Journal of Applied Polymer Science, 76, 938-946, Copyright (2000, John Wiley Sons, Inc.). This material is used by permission of John Wiley Sons, Inc. Figure 7.8 The effect of flow of scC02 on the recovery of Irganox 1010 from PP by means of SFE (temperature 120 °C modifier, 2% MeOH). After Thil6n and Shishoo [12]. Reprinted from M. Thil6n and R. Shishoo, Journal of Applied Polymer Science, 76, 938-946, Copyright (2000, John Wiley Sons, Inc.). This material is used by permission of John Wiley Sons, Inc.
Even higher shear rates in the extruder cannot prevent laminar flow in the screw flights and therefore resultant unmixed particles being carried over the shearing sections. Lengthening of the residence time in the barrel also has to be restricted to limit unacceptable temperature build-up, which would result in scorched compound. It is thus necessary to have an effective means of... [Pg.184]

The focus of RANS simulations is on the time-averaged flow behavior of turbulent flows. Yet, all turbulent eddies do contribute to redistributing momentum within the flow domain and by doing so make up the inherently transient character of a turbulent-flow field. In RANS, these effects of the full range of eddies are made visible via the so-called Reynolds decomposition of the NS equations (see, e.g., Tennekes and Lumley, 1972, or Rodi, 1984) of the flow variables into mean and fluctuating components. To this end, a clear distinction is required between the temporal and spatial scales of the mean flow on the one hand and those associated with the turbulent fluctuations on the other hand. [Pg.163]

Recently, the size and shape of a liquid droplet at the molten tip of an arc electrode have been studied,12151 and an iterative method for the shape of static drops has been proposed. 216 Shapes, stabilities and oscillations of pendant droplets in an electric field have also been addressed in some investigations. 217 218 The pendant drop process has found applications in determining surface tensions of molten substances. 152 However, the liquid dripping process is not an effective means for those practical applications that necessitate high liquid flow rates and fine droplets (typically 1-300 pm). For such fine droplets, gravitational forces become negligible in the droplet formation mechanism. [Pg.126]


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