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Suspending solids concentration

These data may be evaluated by selecting different nominal overflow rates (equivalent to settling rates) for each of the detention-time values, and then plotting the suspended-solids concentrations for each nominal overflow rate (as a parameter) against the detention time. For a specified suspended-sohds concentration in the effluent, a cui ve of overflow rate versus detention time can be prepared from this plot and used for optimizing the design of the equipment. [Pg.1679]

The suspended-solids concentration can be plotted on log-log paper as a function of the sampling (detention) time. A straight line usually wih resiilt, and the required static detention time t to achieve a certain suspended-sohds concentration C in the overflow of an ideal basin can be taken directly from the graph. If the plot is a straight hne, the data are described by the equation... [Pg.1679]

Continuous clarifiers generally are employed with dilute suspensions, principally industrial process streams and domestic municipal wastes, and their primary purpose is to produce a relatively clear overflow. They are basically identical to thickeners in design and layout except that they employ a mechanism of hghter construction and a drive head with a lower torque capability. These differences are permitted in clarification applications because the thickened pulp produced is smaller in volume and appreciably lower in suspended solids concentration, owing in part to the large percentage of relatively fine (smaller than 10 Im) solids. The installed cost of a clarifier, therefore, is approximately 5 to 10 percent less than that of a thickener of equal tank size, as given in Fig. 18-94. [Pg.1683]

The shiny should always be defined as completely as possible by noting suspended solids concentration, particle size distribution, viscosity, density of solids and liquid, temperature, chemical composition, and so on. [Pg.1694]

Pretreatment Chemicals Even though the suspended solids concentration of the slurry to be tested may be correct, it is frequently necessary to modify the sluriy in order to provide an acceptable filtration rate, washing rate, or final cake moisture content. The most common treatment, and one which may provide improvement in all three of these categories, is the addition of flocculating agents, either inorganic chemicals or natural or synthetic polymers. The main task at this point is to determine which is the most effective chemical and the quantity of chemical which should be used. [Pg.1694]

The filter application is typically applied to handling streams containing less than 100 to 200 mg/Liter suspended solids, depending on the required effluent level. Increased-suspended solids loading reduces the need for frequent backwashing. The suspended solids concentration of the filtered liquid depends on the particle size distribution, but typically, granular media filters are capable of producing a... [Pg.243]

Coil coating on galvanized steel generally produces significant suspended solids concentrations in wastewater. Another pollutant problem is the high concentration of dissolved zinc and iron in the... [Pg.267]

The introduction of enamel into the wastestream results in an increase in the concentration of metals, but these metals (antimony, titanium, zirconium, tin, cobalt, and manganese) are in solid form whereas the metals generated by surface preparation are normally in dissolved form. These solid metals increase the suspended solids concentration of the stream. Other metals that may be found in the enamel preparation and application wastestream in significant amounts include aluminum, copper, iron, lead, nickel, and zinc. Table 8.2 presents pollutant sampling data for the processes used in the porcelain enameling on steel industry. [Pg.312]

For a dust ignition to occur, the suspended solids concentration must lie between lower and upper limits which vary from material to material and are influenced by subtle factors such as particle shape and size distribution. From the standpoint of assessing safety hazards in commercial and industrial operations, the lower explosive limit is the more important one. The rationale of this statement is that, if the possibility of exceeding the lower limit in a powder-handling operation can not be completely ruled out, then a hazard must be recognized and appropriate measures taken. Over the... [Pg.838]

Apart from the structural properties of the molecule, surfactant sorption is affected by physico-chemical parameters, such as temperature, pH, organic carbon content of sediment, suspended solids concentration, ionic strength, etc. The most relevant of these are discussed next. [Pg.647]

Measurements of dissolved sorbing phase (e.g., weight of dissolved solids, turbidity, and DOC) demonstrate the increased loading of nonsettling microparticles or macromolecules in the supernatants of batch equilibrium experiments as the solids-to-water ratio increases. It is clear that nonsettling microparticles or macromolecules vary regularly with suspended solid concentration. [Pg.127]

Upflow expanded bed carbon columns are a third contacting process. The liquid waste enters the bottom of the carbon column and expands the carbon bed. Higher suspended solids concentrations can be handled in this system because of the greater distance between particles in an expanded bed. [Pg.126]

Wastewater streams from the utility functions include boiler and cooling tower blowdowns and waste brine and sludge produced by demineralizing and other water treatment systems. The quantity and quality of the wastewater streams depend on the design of the systems and the water source. These streams usually contain high dissolved and suspended solids concentrations and treatment chemicals from the boiler and cooling tower. The blowdown streams also have elevated temperatures. [Pg.254]

The application of such solution- versus solid-associated speciation information may be illustrated by considering an organic chemical, say 1,4-dimethylbenzene (DMB), in a lake and in flowing groundwater. In lakes, the solid-water ratio is given by the suspended solids concentration (since Vw Ftot), which is typically near lO-6 kg-L-1. From experience we may know that the Kid value for DMB in this case happens to be 1 L kg-1 therefore we can see that virtually all of this compound is in the dissolved form in the lake ... [Pg.287]

From Eisenreich et al. (1989).b For surface waters, rsw is approximately equal to the suspended solid concentration. [Pg.1065]

One oil company utilizes mixed media in a series of vertical pressure filters to provide high-quality water for a secondary recovery project. A blend of fresh and produced water b used as the source. Typical influent quality is IS to 30 ppm suspended solids and 4 to 5 ppm of free oil. Upsets that increase the oil and suspended solids concentration to more than 100 ppm... [Pg.235]

Suspended Material. The material retained by the 0.45-pm membrane filters during filtration of the water samples collected from Ralston Creek and Reservoir was classified as suspended solids concentrations are shown in figure 4. The 226r3 content of suspended sediment in the mine effluent was 1,300 pCi/g U content of suspended sediment was 2,400 pg/g. Suspended-material load for this sample was 6 mg/L during the sample collection. Total release of both radionuclides (dissolved and suspended) was then calculated to be 8.4 pCi/L for 226r3 and 1,710 pg/L for U. Assuming an average daily... [Pg.268]

In Table 16.2 some of the typical characteristics of the various types of membranes and configurations are given. In MBR systems SW membrane modules are not used as the channels within the spiral are prone to clogging when the feed water has high suspended-solids concentrations. Tubular membrane systems are not common either as they tend to become very expensive due to the low area to volume ratio. Commercial MBR systems today are normally based on immersed FS configurations or H F/CT configurations. [Pg.370]

The membrane flux, J, is in general a logarithmic function of the suspended solids concentration in the slurry (Michaels, 1968)... [Pg.451]

Total suspended solids concentration in filtrate = 900 mg/L = 0.09 percent. [Pg.566]


See other pages where Suspending solids concentration is mentioned: [Pg.1678]    [Pg.1678]    [Pg.1679]    [Pg.244]    [Pg.118]    [Pg.905]    [Pg.1165]    [Pg.101]    [Pg.467]    [Pg.627]    [Pg.633]    [Pg.181]    [Pg.255]    [Pg.354]    [Pg.438]    [Pg.239]    [Pg.578]    [Pg.579]    [Pg.51]    [Pg.102]    [Pg.31]    [Pg.375]    [Pg.458]    [Pg.458]    [Pg.1499]    [Pg.1499]    [Pg.1500]    [Pg.1500]    [Pg.457]   
See also in sourсe #XX -- [ Pg.265 ]




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