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Fluid-splitting

Middleman suggests the simplest model for the separation region based on the assumption that the fluid splits at a point where ux = 0 and p = 0. The above equation can be solved numerically to give... [Pg.293]

TEMA G shell-and-tube exchanger, tube fluid split into two streams individually mixed, shell fluid mixed stream symmetric... [Pg.1272]

Continuum theory has also been applied to analyse tire dynamics of flow of nematics [77, 80, 81 and 82]. The equations provide tire time-dependent velocity, director and pressure fields. These can be detennined from equations for tire fluid acceleration (in tenns of tire total stress tensor split into reversible and viscous parts), tire rate of change of director in tenns of tire velocity gradients and tire molecular field and tire incompressibility condition [20]. [Pg.2558]

Verlet, L. Computer Experiments" on Classical Fluids. I. Thermodynamical Properties of Lennard-Jones Molecules. Physical Review 159 (1967) 98-103 Janezic, D., Merzel, F. Split Integration Symplectic Method for Molecular Dynamics Integration. J. Chem. Inf. Comput. Sci. 37 (1997) 1048-1054 McLachlan, R. I. On the Numerical Integration of Ordinary Differential Equations by Symplectic Composition Methods. SIAM J. Sci. Comput. 16 (1995) 151-168... [Pg.347]

Twin-fluid atomizer Twisted pair cable Twitchell splitting Twitchell s reagents Two-film theory... [Pg.1032]

Figure 4.20 Sulfide deposits (dark patches) on longitudinally split brass heat exchanger tube. Note the perforation where wastsige penetrated the tube wall. Sulfide was spalled after perforation by escaping fluids. Figure 4.20 Sulfide deposits (dark patches) on longitudinally split brass heat exchanger tube. Note the perforation where wastsige penetrated the tube wall. Sulfide was spalled after perforation by escaping fluids.
Howe er, most conventional pump impellers receive the fluid into the impeller eye, at the center or inside diameter of the impeller. There are single suction impellers, and dual or double suction impellers with two eyes, one on each side. Dual suction impellers are mostly specified for low NPSH applications because the eye area is doubled (it ean reeeive twice as much fluid at a lower velocity head). Dual suction impellers arc mostly found on split case pumps where the shaft passes completely through the impeller. But they can afso be found mounted onto the end of the shaft in some special pump designs. [Pg.66]

G is a split flow. The fluid comes in and goes both way.s around the longitudinal baffle and then exits. H is very rare a double split flow. J is a divided flow. K is a kettle type reboiler, which is a special type and is best explained by looking at the example AKT in Figure 3-9. Kettle types are common where there is a boiling liquid or where gas is liberated from shell fluid as it is heated. The weir controls the liquid, making sure the tubes are always immersed in liquid. Gas that flashes from the liquid can exit the top nozzle. [Pg.56]

Tube Rupture. It is common for a heat exhanger to have a high-pressure fluid in the tubes and a lower-pressure rated shell. If there is a break in one of the tubes, the higher pressure fluid will leak to the shell, resulting in overpressure. It is conservative to assume a tube is completely split with choked flow from both sides of the break. [Pg.357]

According to Allen and Tildesley, the standard recipe to evaluate Af/ in step one of the algorithm described in Sec. IIIB involves computing the energy of atom i with all the other atoms before and after the move (see p. 159 of Ref. 25, italics by the present author) as far as simple fluids are concerned. The evaluation of Af/ can be made more efficient in this case by realizing that for short-range interactions U can be split into three contributions... [Pg.26]

Aeeording to Wertheim [8-11], the fluid density at a point 1 of the bulk assoeiating fluid is split into two terms, namely the density of unbonded speeies, po(l)> and the density of (singly) bonded speeies, Pi(l), sueh that the total density is p(l) = po(l) + Pi(l)- We set the matrix of densities for a dimerizing fluid... [Pg.195]

In addition, solute foeusing is possible by maintaining a low initial temperature (e.g. 40 °C) for a long period of time (8-12 min ) to allow the mixture of deeom-pressed earbon dioxide, helium gas and the solutes to foeus on the GC eolumn. The optimization of the GC inlet temperature ean also lead to inereased solute foeusing. After supereritieal fluid analysis, the SF fluid effluent is deeompressed through a heated eapillary restrietor from a paeked eolumn (4.6 mm i.d.) direetly into a hot GC split vaporization injeetor. [Pg.326]

Figure 12.22 SFC-GC analysis of aromatic fraction of a gasoline fuel, (a) SFC trace (b) GC ttace of the aromatic cut. SFC conditions four columns (4.6 mm i.d.) in series (silica, silver-loaded silica, cation-exchange silica, amino-silica) 50 °C 2850 psi CO2 mobile phase at 2.5 niL/min FID detection. GC conditions methyl silicone column (50 m X 0.2 mm i.d.) injector split ratio, 80 1 injector temperature, 250 °C earner gas helium temperature programmed, — 50 °C (8 min) to 320 °C at a rate of 5 °C/min FID detection. Reprinted from Journal of Liquid Chromatography, 5, P. A. Peaden and M. L. Lee, Supercritical fluid chromatography methods and principles , pp. 179-221, 1987, by courtesy of Marcel Dekker Inc. Figure 12.22 SFC-GC analysis of aromatic fraction of a gasoline fuel, (a) SFC trace (b) GC ttace of the aromatic cut. SFC conditions four columns (4.6 mm i.d.) in series (silica, silver-loaded silica, cation-exchange silica, amino-silica) 50 °C 2850 psi CO2 mobile phase at 2.5 niL/min FID detection. GC conditions methyl silicone column (50 m X 0.2 mm i.d.) injector split ratio, 80 1 injector temperature, 250 °C earner gas helium temperature programmed, — 50 °C (8 min) to 320 °C at a rate of 5 °C/min FID detection. Reprinted from Journal of Liquid Chromatography, 5, P. A. Peaden and M. L. Lee, Supercritical fluid chromatography methods and principles , pp. 179-221, 1987, by courtesy of Marcel Dekker Inc.
Equipment Failure pumps, tubes in heat exchangers and furnaces, turbine drivers and governor, compressor cylinder valves are examples of equipment which might fail and cause overpressure in the process. If an exchanger tube splits or develops a leak, high pressure fluid will enter the low side, overpressuring either the shell or the channels and associated system as the case may be. [Pg.427]

Rubber Sleeve Core Barrels. Rubber sleeve core barrels are special application tools designed to recover undisturbed core in soft, unconsolidated formations. As the core is cut, it is encased in the rubber sleeve that contains and supports it. Using face discharge ports in the bit, the contamination of the core by circulating fluid is reduced. The rubber sleeve core barrel has proven to be a very effective tool, in spite of the fact that the rubber sleeve becomes weak with a tendency to split as the temperature increases about 175°F. [Pg.794]

The conditions which lead a homogeneous fluid mixture to split into two separate fluid phases can be described by classical thermodynamic stability analysis as discussed in numerous textbooks.9 Such analysis has often been... [Pg.190]

The use of a fused silica capillary column for the GC analysis of the neutral oil extract has provided the means for improving the resolution of components in a more inert system. The sultones are determined by temperature-programmed GC over CP-Sil-5 CB (methyl silicone fluid) in a 25 m x 0.2 mm fused silica capillary column using nonadecane as internal standard. A sample split ratio of 1 100 is recommended for a 3-pl injection. [Pg.448]

When a bluff body is interspersed in a fluid stream, the flow is split into two parts. The boundary layer (see Chapter 11) which forms over the surface of the obstruction develops instabilities and vortices are formed and then shed successively from alternate sides of the body, giving rise to what is known as a von Karman vortex street. This process sets up regular pressure variations downstream from the obstruction whose frequency is proportional to the fluid velocity, as shown by Strouai. 9. Vortex flowmeters are very versatile and can be used with almost any fluid — gases, liquids and multi-phase fluids. The operation of the vortex meter, illustrated in Figure 6.27, is described in more detail in Volume 3, by Gjnesi(8) and in a publication by a commercial manufacturer, Endress and Hauser.10 ... [Pg.266]

We first explain the setting of reactors for all CFD simulations. We used Fluent 6.2 as a CFD code. Each reactant fluid is split into laminated fluid segments at the reactor inlet. The flow in reactors was assumed to be laminar flow. Thus, the reactants mix only by molecular diffusion, and reactions take place fi om the interface between each reactant fluid. The reaction formulas and the rate equations of multiple reactions proceeding in reactors were as follows A + B R, ri = A iCaCb B + R S, t2 = CbCr, where R was the desired product and S was the by-product. The other assumptions were as follows the diffusion coefficient of every component was 10" m /s the reactants reacted isothermally, that is, k was fixed at... [Pg.641]


See other pages where Fluid-splitting is mentioned: [Pg.7]    [Pg.165]    [Pg.439]    [Pg.1272]    [Pg.153]    [Pg.110]    [Pg.409]    [Pg.7]    [Pg.165]    [Pg.439]    [Pg.1272]    [Pg.153]    [Pg.110]    [Pg.409]    [Pg.225]    [Pg.609]    [Pg.513]    [Pg.514]    [Pg.358]    [Pg.653]    [Pg.2532]    [Pg.359]    [Pg.115]    [Pg.1109]    [Pg.15]    [Pg.597]    [Pg.719]    [Pg.352]    [Pg.334]    [Pg.334]    [Pg.334]    [Pg.334]    [Pg.271]    [Pg.506]    [Pg.212]    [Pg.200]    [Pg.641]    [Pg.642]   
See also in sourсe #XX -- [ Pg.8 ]




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