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Viscosity wastewater

In spite of the potential problems of swelling and breakage, LEMs have been tested on the pilot plant scale with good results (2,9,11, 12), and will soon be used for the commercial separation of zinc from Viscose wastewater from rayon and cellophane processing (13). [Pg.70]

If a waste is a mixture of water and organic liquid, you must report it as wastewater unless the organic content exceeds 50 percent. Slurries and sludges containing water must be reported as solid waste if they contain appreciable amounts of dissolved solids, or solids that may settle, such that the viscosity or density of the waste is considerably different from that of process wastewater. [Pg.47]

Mannich polymers Cationic, solution polymer flocculants with MW of 5 to 8 M. Very high viscosity and only 4 to 8% active strength solution liquid. A hydrolyzed polyacrylamide, it is very useful for general municipal wastewater treatment. Dose rate normally 200 to 300 ppm or more. [Pg.48]

Several million of tons of oils from refineries, oil transportation, cutting machines, mills, off-shore platforms, etc., are spilled every year in water reservoirs and the sea. About half of this amount contaminates fresh water and an estimate suggests that humans use almost 4 L of hydrocarbons per person each day in the world [176], Oils can be present in wastewaters as a supernatant layer, adsorbed on suspended particles, forming emulsions, or even dissolved. Oils produce many changes in water properties their viscosity and conductivity are altered, and they acquire color and opacity. In addition to a negative esthetic impact and a bad taste, the light necessary for photo-biological processes is absorbed. [Pg.296]

Temperature Most industrial wastes tend to be on the warm side. For the most part, temperature is not a critical issue below 37°C if wastewaters are to receive biological treatment. It is possible to operate thermophilic biological wastewater-treatment systems up to 65°C with acclimated microbes. Low-temperature operations in northern climates can result in very low winter temperatures and slow reaction rates for both biological treatment systems and chemical treatment systems. Increased viscosity of wastewaters at low temperatures makes solid separation more difficult. Efforts are generally made to keep operating temperatures between 10 and 30°C if possible. [Pg.62]

CPI separator is used to remove oils and greases from industrial wastewater. The influent concentration of oil is 50 mg/L. The diameter of oil droplet to be removed is 90 pm. Density of water at 10°C is 0.999 g/cm and density of oil is 0.898 g/cm. The absolute viscosity of the water is 0.013077 poises. The standard size of plate is 3 x 5 m with spacing 2 cm. Calculate the following items ... [Pg.543]

The bitumen layer from the two separation processes is a similar density to water and also quite viscous. It contains some occluded water plus a small amount of mineral fines. By diluting this fraction with naphtha, in which the bitumen is soluble, the viscosity is decreased sufficiently to allow cleaner phase separation to take place. Phase separation, accelerated by centrifuging, produces separate streams of the wastewater (plus some mineral fines) and the naphtha solution of bitumen. Flash distillation of the naphtha solution then yields the crude bitumen product and recovers the naphtha for recycle. [Pg.573]

Suspension—polymerization of monomers dispersed in an inert phase with monomer-soluble initiator Low dispersion viscosity compared to bulk good heat transfer high polymerization rate and high molecular weight direct application of the latex Smaller reactor capacity than bulk reactor wall fouling wastewater problems Polystyrene, PVC, polypropylene... [Pg.1067]

Other criteria Criteria 3-6 for the selection of the diluent solvent are discussed in this section. Third criterion is the favorable mass-transfer characteristics of the diffusion of the pollutant in question through the LM. The diluent properties that are important in this context include diluent viscosity, diffusion coefficient of the pollutant in the diluent phase, and the value ofToiiuent/feed phase [1] The viscosity of the LM has a strong influence on the diffusion coefficient of the pollutant in the diluent phase, thus the application of a highly viscous diluent can lead to a substantial decrease in the mass-transfer rates of the biodegraded pollutant [2]. This prolongs wastewater treatment. [Pg.362]

Figure 3 shows the settling velocity as a function of particle density and diameter for a typical seawater density and viscosity value that may be encountered near a wastewater discharge site. Nonlinearity of the settling velocity contours on the semilogarithmic plot results as the... [Pg.290]

Considerable quantities of sodium sulfate and zinc sulfate are also formed f ri sg regeneration of cellulose fibers. Part of the sodium and zinc sulfates is discharged from the spinning bath together with the viscose fibers and enters the wastewater through the aftertreatment of the fibers. [Pg.36]


See other pages where Viscosity wastewater is mentioned: [Pg.204]    [Pg.332]    [Pg.2212]    [Pg.124]    [Pg.431]    [Pg.65]    [Pg.299]    [Pg.531]    [Pg.902]    [Pg.396]    [Pg.127]    [Pg.380]    [Pg.444]    [Pg.204]    [Pg.332]    [Pg.1968]    [Pg.164]    [Pg.172]    [Pg.247]    [Pg.544]    [Pg.429]    [Pg.327]    [Pg.203]    [Pg.223]    [Pg.363]    [Pg.204]    [Pg.332]    [Pg.846]    [Pg.546]    [Pg.2216]    [Pg.147]    [Pg.306]    [Pg.40]    [Pg.150]    [Pg.707]   


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