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Fluid distribution

This section will look at formation and fluid data gathering before significant amounts of fluid have been produced hence describing how the static reservoir is sampled. Data gathered prior to production provides vital information, used to predict reservoir behaviour under dynamic conditions. Without this baseline data no meaningful reservoir simulation can be carried out. The other major benefit of data gathered at initial reservoir conditions is that pressure and fluid distribution are in equilibrium this is usuaily not the case once production commences. Data gathered at initial conditions is therefore not complicated... [Pg.125]

At the development planning stage, a reservoir mode/will have been constructed and used to determine the optimum method of recovering the hydrocarbons from the reservoir. The criteria for the optimum solution will most likely have been based on profitability and safety. The model Is Initially based upon a limited data set (perhaps a seismic survey, and say five exploration and appraisal wells) and will therefore be an approximation of the true description of the field. As development drilling and production commence, further data is collected and used to update both the geological model (the description of the structure, environment of deposition, diagenesis and fluid distribution) and the reservoir model (the description of the reservoir under dynamic conditions). [Pg.332]

Fluid distribution is good beeause of the single flow passage. [Pg.40]

We also have studied fluid distribution in the pore H = 6 (Fig. 12(b)) at Ppq = 4.8147 and at two values of Pp, namely at 3.1136 (p cr = 0.4) and at 7.0026 (pqOq = 0.7 Fig. 12(b)). In this pore, we observe layering of the adsorbed fluid at high values of the chemical potential Pp. The maxima of the density profile pi(z) occur at distances that correspond to the diameter of fluid particles. With an increase of the fluid chemical potential, pore filhng takes place primarily at pore walls, but second-order maxima on the density profile pi (z) are also observed. The theory reproduces the computer simulation results quite well. [Pg.336]

More disagreement exists with respect to axial dispersion—for example, regarding the applicability of the diffusion model, and regarding the influence of gas and liquid flow rates. More work on these aspects and on the influence of fluid distribution and method of packing is required. Some of the available results are compared in Fig. 3. [Pg.102]

As the physical scale of a reactor increases by numbering up more channels, the micromanifold challenge increases. Fluid distribution occurs in multiple dimensions within a layer [15, 16], from one layer to another [17], and from one reactor to another [18]. An external manifold, also known as the macromanifold or tube connection, as shown in Figure 11.2a, brings the fluids from inlet pipes to the many parallel layers in medium- to large-capacity reactors. [Pg.242]

What are the basic laws for fluid distribution How critical is even distribution in a reactor module Discuss. [Pg.425]

M. E. Brewster, W. Anderson, N. Bodor, Brain, Blood and Cerebrospinal Fluid Distribution of a Zidovudine Chemical Delivery System in Rabbits , J. Pharm. Sci. 1991, 80, 843-846. [Pg.546]

Similar metal sheets have also been used as DLs in the cathode of PEMFCs. Wilkinson et al. [37,38] presented the idea of using fluid distribution layers made out of metal meshes with electrically conductive fillers inside the holes of the meshes. A very similar idea was also presented by Fiamada and Nakato [39]. Eosfeld and Eleven [40] presented another example of fuel cells that use metal meshes as diffusion layers along with metal FF plates. [Pg.211]

D. P. Wilkinson, J. Stumper, S. A. Campbell, M. T. David, and G. J. Lament. Electrochemical cell with fluid distribution layer having integral sealing capability. US Patent 5976726 (1999). [Pg.290]

S. D. Knights, D. P. Wilkinson, and P. Beattie. Electrochemical fuel cell with fluid distribution layer having nonuniform perforations. US Patent 2003039876 (2003). [Pg.290]

Broughton, D. (1965) Fluid distributing means for packed chambers. US Patent 3,214,247. [Pg.246]

Avoid foods that may generate dryness Patients who suffer from the syndrome of dryness should avoid spicy food and food that induces heat, such as hot pepper, onion, cinnamon and deep-fried food. Very sour food, such as citrus fruits and vinegar, should not be consumed in excess as they may make the fluid distribution slow or even stop. [Pg.350]

Thus, the sorption of chemicals on the surface of the solid matrix may become important even for substances with medium or even small solid-fluid equilibrium distribution coefficients. For the case of strongly sorbing chemicals only a tiny fraction of the chemical actually remains in the fluid. As diffusion on solids is so small that it usually can be neglected, only the chemical in the fluid phase is available for diffusive transport. Thus, the diffusivity of the total (fluid and sorbed) chemical, the effective diffusivity DieS, may be several orders of magnitude smaller than diffusivity of a nonsorbing chemical. We expect that the fraction which is not directly available for diffusion increases with the chemical s affinity to the sorbed phase. Therefore, the effective diffusivity must be inversely related to the solid-fluid distribution coefficient of the chemical and to the concentration of surface sites per fluid volume. [Pg.819]


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See also in sourсe #XX -- [ Pg.21 , Pg.22 , Pg.54 , Pg.58 ]

See also in sourсe #XX -- [ Pg.19 ]




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