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Darcy flux

In this equation r) is the volume of water per unit volume of solid, t is time, F is the Darcy flux of water relative to the solid, and m is a space like coordinate defined in terms of the distribution of the solid phase. Substitution of Darcy s law in this equation results in equations similar to the Richards equation and, at least in 1-dimension, these can be solved like their non-swelling analogues. This equation implicitly deals with volume change that might accompany change in water content. [Pg.202]

Fanning friction factor Darcy friction factor mass flux... [Pg.500]

The clean water flux across a membrane without any material being deposited follows Darcy s Law ... [Pg.355]

Fanning (Darcy) friction factor f(f or fD) e, D 2 V2L fo = 4f TW yv2 e, = friction loss (energy/mass) rw = wall stress (Energy dissipated)/ (KE of flow x 4L/D) or (Wall stress)/ (momentum flux) Flow in pipes, channels, fittings, etc. [Pg.36]

Although pV2/2 represents kinetic energy per unit volume, pV2 is also the flux of momentum carried by the fluid along the conduit. The latter interpretation is more logical in Eq. (5-50), because rw is also a flux of momentum from the fluid to the tube wall. However, the conventional definition includes the (arbitrary) factor i. Other definitions of the pipe friction factor are in use that are some multiple of the Fanning friction factor. For example, the Darcy friction factor, which is equal to 4/, is used frequently by mechanical and civil engineers. Thus, it is important to know which definition is implied when data for friction factors are used. [Pg.123]

The two flux equations of importance to subsurface transport are Darcy s law for the advective flow of water and other liquids and Fick s law for the diffusive flow of molecules and gases. These laws are independently discussed below. [Pg.54]

It is often easy to measure the flux density, e.g., using a flowmeter, and then determine the hydraulic conductivity or diffusion coefficient by dividing the flux by the driving force. One of the most difficult problems is determining how to represent the driving force. The symbol V is called an operator, which signifies that some mathematical operation is to be performed upon whatever function follows. V means to take the gradient with respect to distance. For Darcy s law under saturated... [Pg.54]

In eq 51, the first term represents a convection term, and the second comes from a mass flux of water that can be broken down as flow due to capillary phenomena and flow due to interfacial drag between the phases. The velocity of the mixture is basically determined from Darcy s law using the properties of the mixture. The appearance of the mixture velocity is a big difference between this approach and the others, and it could be a reason the permeability is higher for simulations based on the multiphase mixture model. [Pg.461]

The traditional, continuum-based approach uses Darcy s law, modified for partially saturated porous media, to quantify the flux of water ... [Pg.214]

In this equation ut should be interpreted as the volumetric flux density (directional flow rate per unit total area). The indexes range from 1 to 3, and repetition of an index indicates summation over that index according to the conventional summation convention for Cartesian tensors. The term superficial velocity is often used, but it is in our opinion that it is misleading because n, is neither equal to the average velocity of the flow front nor to the local velocity in the pores. The permeability Kg is a positive definite tensor quantity and it can be determined both from unidirectional and radial flow experiments [20], Darcy s law has to be supplemented by a continuity equation to form a complete set of equations. In terms of the flux density this becomes ... [Pg.368]

Generally, the pure-water flux through a membrane layer, uw is directly proportional to the applied hydrostatic pressure difference (transmembrane pressure, AP) according to Darcy s law as follows ... [Pg.321]

The flux solvent evolution of pure water with the transmembrane pressure across NF/LPRO membranes are reported in Fig. 6. The linear dependence of fluxes with the transmembrane pressure shows that Darcy s law is verified. As expected, the hydraulic permeabilities determined from the slopes (Table 3) show higher values for NF than LPRO membranes, due to their larger pore size. The NF90 membrane shows the higher hydraulic permeability with Z p = 14.8 Lh 1 m 2bar 1. [Pg.67]

The relationship between flow and pressure drop is expressed by Darcy s law [7,8], an empirical equation applied (starting in the last century) to numerous forms of porous media. This law may be thought of as the Ohm s law of fluid flow, another linear law of transport expressing, in this case, the flux density q of fluid (analogous to current density) in the form... [Pg.63]

This brief discussion of the flow regime of an unconfined system emphasizes its three-dimensional nature and the large variety of water fluxes, velocities, and ages that prevail in each case study. The unconfined groundwater regime differs fundamentally from the one-dimensional tube of Darcy s experiment, with its particular properties (section 14.6). [Pg.30]

Both MTPM and DGM share the Darcy s constitutive equation governing the permeation molar flux intensity of the z th component Nf,... [Pg.159]


See other pages where Darcy flux is mentioned: [Pg.82]    [Pg.1458]    [Pg.1461]    [Pg.1462]    [Pg.205]    [Pg.989]    [Pg.990]    [Pg.295]    [Pg.600]    [Pg.664]    [Pg.664]    [Pg.466]    [Pg.40]    [Pg.227]    [Pg.82]    [Pg.1458]    [Pg.1461]    [Pg.1462]    [Pg.205]    [Pg.989]    [Pg.990]    [Pg.295]    [Pg.600]    [Pg.664]    [Pg.664]    [Pg.466]    [Pg.40]    [Pg.227]    [Pg.2039]    [Pg.20]    [Pg.42]    [Pg.53]    [Pg.74]    [Pg.363]    [Pg.20]    [Pg.459]    [Pg.495]    [Pg.221]    [Pg.66]    [Pg.371]    [Pg.385]    [Pg.391]    [Pg.76]    [Pg.65]   
See also in sourсe #XX -- [ Pg.205 ]

See also in sourсe #XX -- [ Pg.227 ]




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