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Form compressible fluid

Process engineering and design using Visual Basic [Pg.182]

T hetmal coraJuclivity of Hiid MaesOoM Premie T effpeieture [Pg.182]

Pipe material iheirnai cenductiviy Insulabon material jSeled [Pg.182]

A few points must be noted to fully xmderstand the heat gain/loss calculation. These are explained as follows  [Pg.182]

Design a gas lift line for the following parameters. The fluid is a high-pressure sales gas without any free water or formation liquid. [Pg.183]


Discharge Coefficients and Gas Discharge A compressible fluid, upon discharge from an orifice, accelerates from the puncture point and the cross-sec tional area contracts until it forms a minimum at the vena contracta, If flow is choked, the mass flux G, can be found at the vena contrac ta, since it is a maximum at that point, The mass flux at the orifice is related to the mass flux at the vena contracta by the discharge coefficient, which is the area contraction ratio (A at the vena contracta to Ay at the orifice) ... [Pg.2353]

These asymptotic forms may be useful for conceptual studies, but the real design calculations must be based on the full Ergun equation. Turning to the case of compressible fluids, scaleup using geometric similarity with Sr = Sl = S is generally infeasible. Simply stated, the reactors are just too long and have too much inventory. [Pg.108]

Dixon, D. J., Johnston, K. P. and Bodmeier, R. A. AIChE Jl. 39 (1993) 127. Polymeric materials formed by precipitation with a compressed fluid antisolvent. [Pg.769]

Atomizers Atomization is the process of breaking up a continuous liquid phase into discrete droplets. Figure 24-22 shows the idealized process by which the surface area of a liquid sheet is increased until it forms droplets. Atomizers may be classified into two broad groups (see Fig. 24-23), pressure atomizers, in which fuel oil is injected at high pressure, and twin-fluid atomizers, in which fuel oil is injected at moderate pressure and a compressible fluid... [Pg.31]

Equation (7.27) will hold for incompressible fluids and for compressible fluids with small values of AP. If the pressure gradient across the bed is large and the fluid is compressible, equation (7.27) takes the form... [Pg.52]

The Navier-Stokes equations have been derived and written in a form that exposes V-V explicitly. In large measure this is done in anticipation of the simplifications that accrue for incompressible flow where V-V = 0. It is also important to recognize situations in which compressible fluids (i.e., gases) behave as though they were incompressible, thus permitting the incompressible-flow simplifications. [Pg.83]

In Ihe case of a liquid, this equation can be considerably simplified—in fact, it becomes Bernoulli s well-known equation—but in Ihe case of compressible fluids, which may also undergo some change of form, such as condensation or compression, the longer equation applies. Most practical problems in fluid friction arise in connection with the flow of fluid through pipes. [Pg.657]


See other pages where Form compressible fluid is mentioned: [Pg.181]    [Pg.181]    [Pg.230]    [Pg.145]    [Pg.228]    [Pg.649]    [Pg.788]    [Pg.433]    [Pg.365]    [Pg.188]    [Pg.248]    [Pg.423]    [Pg.131]    [Pg.24]    [Pg.327]    [Pg.133]    [Pg.228]    [Pg.364]    [Pg.327]    [Pg.406]    [Pg.545]    [Pg.135]    [Pg.209]    [Pg.24]    [Pg.350]    [Pg.247]    [Pg.483]    [Pg.31]    [Pg.474]    [Pg.612]    [Pg.145]    [Pg.797]    [Pg.92]    [Pg.424]   
See also in sourсe #XX -- [ Pg.181 , Pg.182 , Pg.183 ]




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Compressed fluid

Pressure drop form compressible fluid

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