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Dispersion lateral

In the present work, the transient and steady-state characteristics of a fluidized bed combustor are studied by solving numerically a dynamic model in which lateral solids and gas dispersion, lateral temperature distribution and wide size distribution of coal feed are taken into account. The influences of bubble size, excess air rate, specific area of heat exchangers and coal feed rate on the performance of the fluidized combustor are examined by means of simulation with the model. [Pg.96]

Disperse laterally and in-depth to increase lines-of-sight. [Pg.4]

Hydrothermal plumes are the water column manifestation of mid-ocean ridge hydrothermal activity (e.g. Baker etal., 1995). They form above areas of venting as a result of the buoyancy of the heated fluids as the fluids rise, they entrain ambient seawater, thus continuously increasing the plume volume until neutral buoyancy is achieved and the plume disperses laterally (Baker etal., 1995). These warm, buoyant plumes rise up to several hundred metres above the seafloor and extend for several kilometres away from vents [e.g. see reviews by Baker... [Pg.261]

Many modified designs have been proposed usually they are based on some hydrodynamic principle. Figure 2.20 shows a cap that includes an insert to give streamline vapor flow. Another experimental type, shown in Fig. 2.21, is provided with fins for better vapor dispersal. Lateral screened skirt caps have also been proposed, the most recent entry being the VST cap developed by the... [Pg.48]

In these expressions, molecular diffusion has been neglected relative to turbulent diffusion. When the reactor is sufficiently long, (Dr L ), the distance after which the spot has dispersed laterally and the flow has become uniform over the available flow section is small compared to the length of the reactor, and the main process observed inside the reactor is the transport of the spot inside the reactor and its gradual expansion along the axial direction. It is this phenomenon that we model by employing the concept of turbulent dispersion introduced in Chapter 8. For this reactor, the mean residence time is related simply to velocity U of the mean flow ... [Pg.175]

The Debye model is more appropriate for the acoustic branches of tire elastic modes of a hanuonic solid. For molecular solids one has in addition optical branches in the elastic wave dispersion, and the Einstein model is more appropriate to describe the contribution to U and Cj from the optical branch. The above discussion for phonons is suitable for non-metallic solids. In metals, one has, in addition, the contribution from the electronic motion to Uand Cy. This is discussed later, in section (A2.2.5.6T... [Pg.414]

Figure B3.3.12. Sulphur atoms in liquid iron at the Earth s core conditions, simnlated by first-principle Car-Parrinello molecular dynamics, (a) Initial conditions, showing a mannally-prepared initial cluster of snlphur atoms, (b) A short tune later, indicating spontaneous dispersal of the snlphur atoms, which mingle with the surroundmg iron atoms. Thanks are dne to D Alfe and M J Gillan for this figure. For fiirtlier details see [210. 211]. Figure B3.3.12. Sulphur atoms in liquid iron at the Earth s core conditions, simnlated by first-principle Car-Parrinello molecular dynamics, (a) Initial conditions, showing a mannally-prepared initial cluster of snlphur atoms, (b) A short tune later, indicating spontaneous dispersal of the snlphur atoms, which mingle with the surroundmg iron atoms. Thanks are dne to D Alfe and M J Gillan for this figure. For fiirtlier details see [210. 211].
The in situ process is simpler because it requires less material handling (35) however, this process has been used only for resole resins. When phenol is used, the reaction system is initially one-phase alkylated phenols and bisphenol A present special problems. As the reaction with formaldehyde progresses at 80—100°C, the resin becomes water-insoluble and phase separation takes place. Catalysts such as hexa produce an early phase separation, whereas NaOH-based resins retain water solubiUty to a higher molecular weight. If the reaction medium contains a protective coUoid at phase separation, a resin-in-water dispersion forms. Alternatively, the protective coUoid can be added later in the reaction sequence, in which case the reaction mass may temporarily be a water-in-resin dispersion. The protective coUoid serves to assist particle formation and stabUizes the final particles against coalescence. Some examples of protective coUoids are poly(vinyl alcohol), gum arabic, and hydroxyethjlceUulose. [Pg.298]

A wide variety of particle size measurement methods have evolved to meet the almost endless variabiUty of iadustrial needs. For iastance, distinct technologies are requited if in situ analysis is requited, as opposed to sampling and performing the measurement at a later time and/or in a different location. In certain cases, it is necessary to perform the measurement in real time, such as in an on-line appHcation when size information is used for process control (qv), and in other cases, analysis following the completion of the finished product is satisfactory. Some methods rapidly count and measure particles individually other methods measure numerous particles simultaneously. Some methods have been developed or adapted to measure the size distribution of dry or airborne particles, or particles dispersed inhquids. [Pg.130]

Later it was found growing in South America where the Indians used the red dye from the seeds as a body paint. An extract of the seeds appears on the market as annatto. This extract is used in coloring butter, margarine, and cheese such as Leicester cheese. In Mexican and South American cuisine, it finds special use as a flavor and coloring matter. The seeds are sold under the name achiote in many Latin grocery stores and markets. Ann at o is available as an aqueous solution, as an oleaginous dispersion, and a spray-dried powder. [Pg.405]

A flow reac tor with some deviation from plug flow, a quasi-PFR, may be modeled as a CSTR battery with a characteristic number n of stages, or as a dispersion model with a characteristic value of the dispersion coefficient or Peclet number. These models are described later. [Pg.2075]

Removal of deposits and corrosion products from internal surfaces revealed irregular metal loss. Additionally, surfaces in wasted areas showed patches of elemental copper (later confirmed by energy-dispersive spectroscopy) (Fig. 13.12). These denickelified areas were confined to regions showing metal loss. Microscopic analysis confirmed that dealloying, not just redeposition of copper onto the cupronickel from the acid bath used during deposit removal, had occurred. [Pg.307]


See other pages where Dispersion lateral is mentioned: [Pg.158]    [Pg.3057]    [Pg.214]    [Pg.491]    [Pg.386]    [Pg.139]    [Pg.355]    [Pg.168]    [Pg.216]    [Pg.114]    [Pg.24]    [Pg.289]    [Pg.158]    [Pg.3057]    [Pg.214]    [Pg.491]    [Pg.386]    [Pg.139]    [Pg.355]    [Pg.168]    [Pg.216]    [Pg.114]    [Pg.24]    [Pg.289]    [Pg.131]    [Pg.79]    [Pg.285]    [Pg.373]    [Pg.76]    [Pg.120]    [Pg.278]    [Pg.279]    [Pg.122]    [Pg.334]    [Pg.544]    [Pg.293]    [Pg.307]    [Pg.102]    [Pg.285]    [Pg.345]    [Pg.351]    [Pg.20]    [Pg.1229]    [Pg.1352]    [Pg.1396]    [Pg.1588]    [Pg.2319]   
See also in sourсe #XX -- [ Pg.221 ]

See also in sourсe #XX -- [ Pg.221 ]

See also in sourсe #XX -- [ Pg.221 ]




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Dispersion lateral, coefficient

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