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Determination suspended solids

Total Solids None Total Solids is the sum of dissolved and suspended solids, determined gravimetrically See Dissolved Solids and Suspended Solids ... [Pg.147]

For a 50,000 GPD filtration operation with an average loading 50 mg/L TSS (Total Suspended Solids) determine the optimum flocculant to use in order to achieve at least an 85 % reduction in solids. Assume that a rotary drum filter unit is used. [Pg.122]

In situ turbidity determinations using a Secchi disk are related to, but do not strictly correspond to suspended solids determinations [15]. The disk is a circular plate of about 20 cm in diameter made of sheet steel or other metal, and is painted with alternating black and white quadrants on its upper face. A rope or chain calibrated in meters is attached to the disk via an eyebolt at the center of the disk, so that the disk hangs horizontally. For a reading, the disk is lowered into the water until the black and white painted quadrants appear to be uniformly gray due to the turbidity of the water, and the depth at which this occurs is recorded. It is then lowered a few meters more and then... [Pg.110]

Suspended solids—determine the silt density index (SDI). [Pg.716]

There is a common requirement in water analysis to separate the dissolved or suspended component in the sample before analysis. This is usually achieved by a physical separation step. Filtration is the most commonly used sample pretreatment method. Membrane and glass fiber filters are available in a variety of pore sizes and membranes are available in different materials. Water analysts normally use GF/C glass fiber filters for suspended solids determinations and 0.45 pm cellulose-based filters to define the soluble/ insoluble fraction in samples. However, all filters and filtration apparatus must be checked to confirm... [Pg.5011]

The measurement of suspended solids may be undertaken by filter analysis, turbidity meter, or other instruments measuring size and density of particles. Membrane filters are the most suitable for carrying out suspended solids determinations on water that is allowed to flow directly from the process stream. [Pg.267]

In the removal of suspended solids from domestic and industrial wastes of frequently changing composition, turbidity measurement, being much quicker than suspended solids determination, is especially useful to adjust the optimum dosages of chemicals required. [Pg.71]

Finally, in particulate gravimetry the analyte is determined following its removal from the sample matrix by filtration or extraction. The determination of suspended solids is one example of particulate gravimetry. [Pg.234]

Removing the analyte from its matrix by filtration or extraction must be complete. When true, the analyte s mass can always be found from the analytical signal thus, for the determination of suspended solids we know that... [Pg.234]

A 200.0-mL sample of water was filtered through a preweighed glass fiber filter. After drying to constant weight at 105 °C, the filter was found to have increased in mass by 48.2 mg. Determine the total suspended solids for the sample in parts per million. [Pg.265]

Suspended Solids. Suspended soflds are determined by filtering a known volume of water through a glass-fiber filter and weighing the filter before and after filtration. The filter is dried at 105—110°C, and the weight difference is equal to the suspended soflds. [Pg.230]

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]

Depth tends to be determined from the retention time and the surface overflow rate. As surface overflow rates were reduced, the depth of sedimentation tanks was reduced to keep retention time from being excessive. It was recognized that depth was a valid design parameter and was more critical in some systems than retention time. As mixed-liquor suspended-solids (MESS) concentrations increase, the depth should also be increased. Minimum sedimentation-tank depths for variable operations should be 3.0 m (10 ft) with depths to 4.5 m (15 ft) if 3000 mg/L MESS concentrations are to be maintained under variable hydraulic conditions. With MESS concentrations above 4000 mg/L, the depth of the sedimentation tank should be increased to 6.0 m (20 ft). The key is to keep a definite freeboard over the settled-sludge blanket so that variable hydraulic flows do not lift the solids over the effluent weir. [Pg.2221]

Suspended Solids None Suspended Solids is the measure of undissolved matter, determined gravimetrically suspended solids plug lines, cause deposits in heat exchange equipment, boilers, etc. Subsidence, filtration, usually preceded by coagulation and settling... [Pg.147]

Starting point for evaluating the settling characteristics of suspended solids for dilute systems. Note that from the definition of the Reynolds number, we can readily determine the settling velocity of the particles from the application of the above expressions (u, = /xRe/dpp). The following is an interpolation formula that can be applied over all three settling regimes ... [Pg.275]

Step 5. After having found the adjusted mud weight, proceed horizontally from that point to the right to determine the volume percent of solids occupied by the basic emulsifier package. The volume percent of suspended solids is 100% less the sum of the volume-percent oil, the true volume-percent brine (Step 2), and the volume-percent emulsifier solids. [Pg.661]

The initial processing steps are determined to a large extent by the location of the product species, and they generally consist of cell/broth separation and/or cell debris removal. For products retained within the biomass during production, it is first necessary to concentrate the cell suspension before homogenization or chemical treatment to release the product. Clarification to remove the suspended solids is the process goal at this stage. [Pg.73]

The size of most biological reactors is determined by pollution load, for example, kg BOD (biochemical oxygen demand) or COD (chemical oxygen demand) per kg MLVSS (mixed liquor volatile suspended solids) per day in the case of suspended growth type systems, and kg BOD or COD per m3 of media or reactor volume in the case of fixed-film type systems. [Pg.2]

For fine suspended solids with particles that are too small to be separated from the liquid by gravitational or centrifugal methods, a barrier method such as a filter may be used. The liquid is passed through a filter medium (usually a cloth or screen) that provides a support for the solid particles removed from the slurry. In actuality, the pores in the filter medium are frequently larger than the particles, which penetrate some distance into the medium before being trapped. The layer of solids that builds up on the surface of the medium is called the cake, and it is the cake that provides the actual filtration. The pressure-flow characteristics of the porous cake primarily determine the performance of the filter. [Pg.401]

For wastewater samples, a number of additional solid determinations are typically performed, including total dissolved solids, volatile solids, and settleable solids. Total dissolved solids are the total solids minus the suspended solids and are determined in a manner similar to total solids, but after filtering out the suspended solids. Thus, a volume of the filtrate is measured into the evaporating dish and the water evaporated in a drying oven. [Pg.45]

For settleable solids, a sample of the wastewater is taken after the suspended solids are allowed to settle for a specified time. The solids in this sample are then measured in a manner similar to that for total solids. These are the nonsettleable solids. The settleable solids are then determined by subtracting from the total solids determined previously. See Workplace Scene 3.2. [Pg.45]

Cory Neth, an analyst for the City of Lincoln, Nebraska, Wastewater Treatment Plant Laboratory, removes a tray of crucibles from a muffle furnace. The crucibles are filtering crucibles used in the determination of suspended solids. The muffle furnace is used in the total suspended volatile solid test. [Pg.46]


See other pages where Determination suspended solids is mentioned: [Pg.110]    [Pg.110]    [Pg.110]    [Pg.110]    [Pg.233]    [Pg.1678]    [Pg.1678]    [Pg.1679]    [Pg.2057]    [Pg.2223]    [Pg.406]    [Pg.406]    [Pg.407]    [Pg.409]    [Pg.410]    [Pg.431]    [Pg.301]    [Pg.120]    [Pg.256]    [Pg.397]    [Pg.232]    [Pg.92]    [Pg.133]    [Pg.370]    [Pg.45]    [Pg.45]   
See also in sourсe #XX -- [ Pg.90 , Pg.91 ]




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Suspended solids

Suspending

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