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Submerged solid

Terms used, methods of sampling, and sample handling will be different for water and submerged solid and semisolid samples. The methods described earlier (i.e., transect and grid sampling) are also applicable to these situations. However, semisolid samples, such as those obtained from lake bottoms, require a special sampler. [Pg.165]

Figure 3. Possible conditions of the momentum boundary layer around a submerged solid sphere with increasing relative velocity. Key a, envelope of pseudo-stagnant fluid b, streamline flow c, flow separation and vortex formation d, vortex shedding e, localized turbulent eddy formation. Reproduced, with permission, from Ref. 38. Copyright 1981, Springer-Verlag. Figure 3. Possible conditions of the momentum boundary layer around a submerged solid sphere with increasing relative velocity. Key a, envelope of pseudo-stagnant fluid b, streamline flow c, flow separation and vortex formation d, vortex shedding e, localized turbulent eddy formation. Reproduced, with permission, from Ref. 38. Copyright 1981, Springer-Verlag.
An extensive literature exists regarding the interface between water and solids, and only the main concepts are dealt with here. Two situations may be distinguished regarding the surface between water and a solid in one case a gaseous phase (vapor and/or air) is also present, as when a drop of water is located on a solid support, and the other case is at a submerged solid in the water (or an aqueous solution), e.g., at an electrode. [Pg.151]

Rotating microscreen batch, fluid loading 3 to 6 L/s m of submerged area usually 66% area submerged solids loading 0.05 to 0.1 g/s m headless 7 to 14 cm to max. of 45 cm. Clean by backwash at 2 to 5 % volumetric throughput capacity. Screen pack downstream of extruders screen pack area directly proportional to rate of extrusion. Cycle time for the screen to blind > time between shutdowns. For example, screen pack area 0.17 m s/kg and screen pack diameter 20 cm s/kg but must be custom selected for the polymer. [Pg.159]

Lcs Weight of container with liquid and submerged solid (M)... [Pg.452]

Of importance in the case of mineral fibers is the adsorption of substances from a solution in which they are submerged. Willard Gibbs published an isotherm for the adsorption of dissolved substances onto a solid substrate. It was shown that a substance which lowered the surface tension of a liquid at the solid-liquid interface would usually be more concentrated on the surface of a submerged solid than in the body of the solution. These are usually referred to as surface-active agents. On the other hand, substances that raise the surface tension of a liquid in which they are dissolved will be negatively adsorbed at a surface. The concentration of these salts will be greater in the body of the solution than at an interface. In company reports, I have called these salts body active salts. Many electrolytes will raise the surface tension of water. [Pg.108]

Theoiy permits the approximation of the maximum size of a bubble that can adhere to a submerged horizontal surface if the contact angle between bubble and sohd (angle formed by solid-hquid and liquid-gas interfaces) is known [Wark, ]. Phys. Chem.,. 37, 623 (1933) Jakob, Mech. Eng., 58, 643 (1936)]. Because the bubbles that actually rise from a surface are always considerably smaller than those so calculated and inasmuch as the contact angle is seldom known, the theoiy is not direc tly useful. [Pg.1416]

Pitched-blade turbines (Fig, 18-3) are used on top-entering agitator shafts instead of propellers when a high axial circulation rate is desired and the power consumption is more than 2,2 kW (3 hp), A pitched-blade turbine near the upper surface of liquid in a essel is effecth e for rapid submergence of floating particulate solids,... [Pg.1627]

For suspension of free-settling particles, circulation of pseudoplastic slurries, and heat transfer or mixing of miscible liqiiids to obtain uniformity, a speed of 3.50 or 420 r/min should be stipulated. For dispersion of dry particles in hquids or for rapid initial mixing of hquid reactants in a vessel, an 11.50- or 1750- r/min propeller should be used at a distance Df/4 above the vessel bottom. A second propeller can be added to the shaft at a depth below the hquid surface if the submergence of floating hquids or particiilate solids is other wise inadequate. Such propeller mixers are readily available up to 2.2 kW (3 hp) for off-center sloped-shaft mounting. [Pg.1631]

When abrasive solid particles must be suspended, maintenance costs for the submerged shaft seal of a side-entering propeller may become high enough to make this type of mixer an uneconomical choice. [Pg.1631]

Rotation speeds to 40 r/min are possible with cakes typically 3 to 6 mm (0.12 to 0.24 in) thick. Filter sizes range from 930 cm to 19 m (1 to 207 ft") with 93 percent of the area active. The slurry is fed into a conical feed tank designed to prevent solids from settling without the use of mechanical agitators. The proper hquid level is maintained by overflow, and submergence ranges from 5 to 70 percent of the drum circumference. [Pg.1716]

Sedimentation Tanks These tanks are an integral part of any activated-sludge system. It is essential to separate the suspended solids from the treated liquid if a high-quality effluent is to be produced. Circular sedimentation tanks with various types of hydraulic sludge collectors have become the standard secondary sedimentation system. Square tanks have been used with common-wall construc tion for compact design with multiple tanks. Most secondary sedimentation tanks use center-feed inlets and peripheral-weir outlets. Recently, efforts have been made to employ peripheral inlets with submerged-orifice flow controllers and either center-weir outlets or peripheral-weir outlets adjacent to the peripheral-inlet channel. [Pg.2221]

Because the radius of the solid discharge port is ususally less than the radius of the liquid overflow at the broader end of the bowl, part of the settled solids is submerged in the pond. [Pg.527]

Nevertheless, as response data have accumulated and the nature of the porous deformation problems has crystallized, it has become apparent that the study of such solids has forced overt attention to issues such as lack of thermodynamic equilibrium, heterogeneous deformation, anisotrophic deformation, and inhomogeneous composition—all processes that are present in micromechanical effects in solid density samples but are submerged due to continuum approaches to mechanical deformation models. [Pg.50]

Periphyton are microscopic and macroscopic algae that attach to and grow on solid surfaces, such as lake bottoms, rooted aquatic vegetation, and submerged woody debris. Periphyton form part of the base of littoral food webs in lakes. Periphyton communities are taxonomically diverse and the attached communities contain other organisms, such as bacteria and zooplankton, as well as detrital material. Periphyton vary seasonally and annually in both abundance and species composition. [Pg.99]

Controlled contact between two immiscible liquids has also been achieved by flowing one liquid along a solid support submerged in the second phase [28,29]. Several different arrangements have been used, although all are based on similar principles. For example, a wetted wall column which offered liquid-liquid contact times of 0.5-10 s was used to measure solute transfer rates [29]. [Pg.335]

Reposition the test-tube clamp so that the test tube containing the solid naphthalene is again partially submerged in the boiling water bath. Heat the test tube until the naphthalene is melted and you can remove the thermometer and stirrer as a unit. CAUTION The thermometer, stirring wire, and test tube may be hot. Do not discard the naphthalene. Remove all the naphthalene from the stopper, thermometer, and stirrer by washing them with acetone. [Pg.118]

Vacuum filter systems consist of a horizontal cylinder partially submerged in a tank of biosolids. A layer of porous filter media fabric or tightly wound coils covers the outer surface of the cylinder. As the cylinder surface passes through the tank, a layer of biosolids adheres to the cylinder and vacuum is applied.61 The dewatered biosolids cake is then scraped off the fabric at up to 30% solids. [Pg.895]

This also applies to a body submerged in a fluid that is subject to any acceleration. For example, a solid particle of volume Vs submerged in a fluid within a centrifuge at a point r where the angular velocity is on is subjected to a net radial force equal to Ap on2rVs. Thus, the effect of buoyancy is to effectively reduce the density of the body by an amount equal to the density of the surrounding fluid. [Pg.94]


See other pages where Submerged solid is mentioned: [Pg.156]    [Pg.1396]    [Pg.20]    [Pg.325]    [Pg.213]    [Pg.16]    [Pg.156]    [Pg.1396]    [Pg.20]    [Pg.325]    [Pg.213]    [Pg.16]    [Pg.32]    [Pg.323]    [Pg.1138]    [Pg.1717]    [Pg.335]    [Pg.352]    [Pg.432]    [Pg.155]    [Pg.204]    [Pg.212]    [Pg.330]    [Pg.432]    [Pg.459]    [Pg.350]    [Pg.898]    [Pg.415]    [Pg.51]    [Pg.42]    [Pg.236]    [Pg.326]    [Pg.263]    [Pg.103]    [Pg.412]   
See also in sourсe #XX -- [ Pg.148 ]




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Submergence

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