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Periodic effluent concentrations

Figure 8. Periodic effluent concentrations for three different switching fractions as measured continuously using the ir analyzer Ct = 180 s. Catalyst 11)... Figure 8. Periodic effluent concentrations for three different switching fractions as measured continuously using the ir analyzer Ct = 180 s. Catalyst 11)...
Aquatic toxicity is becoming (ca 1997) a permit requirement on all discharges. Aquatic toxicity is generally reported as an LC q (the percentage of wastewater which causes the death of 50% of the test organisms in a specified period ie, 48 or 96 h, or as a no observed effect level (NOEL), in which the NOEL is the highest effluent concentration at which no unacceptable effect will occur, even at continuous exposure. [Pg.178]

Fig. 5.2.2. Continuous stirred tank reactors experiment (different test periods A and B). Reactor fed with sludge spiked with C12-LAS, the concentration of which in the influent (filled symbols) was increased approximately from 100 to 268mgLT1 the effluent concentration (empty diamonds). (Figure taken from Ref. [47].)... Fig. 5.2.2. Continuous stirred tank reactors experiment (different test periods A and B). Reactor fed with sludge spiked with C12-LAS, the concentration of which in the influent (filled symbols) was increased approximately from 100 to 268mgLT1 the effluent concentration (empty diamonds). (Figure taken from Ref. [47].)...
Fig. 4 Variation in hospital effluent concentrations of two common pharmaceutical compounds over a 24-h period... Fig. 4 Variation in hospital effluent concentrations of two common pharmaceutical compounds over a 24-h period...
Sublethal testing of the Kimberly-Clark final mill effluent indicated inhibition of growth in fathead minnow and Selenastrum capricornutum and inhibition of reproduction of Ceriodaphnia dubia during the period from 1994 to 2000. Zones of potential effects were estimated (Tab. 6) and plotted (Fig. 1) to illustrate the location of effluent concentrations > the lowest IC25 (%v/v) for each test. [Pg.152]

Fig. 2. Bifurcation diagrams describing the behavior of the CO/O2 system as CO pressure is varied, (a) CO2 effluent concentration (which is proportional to the reaction rate) as a function of CO inlet concentration at four different temperatures in an atmospheric reactor over a pulverized Pt/silica/alumina catalyst. Oscillation existence regions are indicated by vertical hatching (from Ref. 98). (b) Work function maxima and minima plotted as a function of CO pressure at 540 K on Pt(l 10). The periodicity of the oscillations (as indicated above the curve) is seen to increase as CO pressure is decreased. (From Ref. 231.)... Fig. 2. Bifurcation diagrams describing the behavior of the CO/O2 system as CO pressure is varied, (a) CO2 effluent concentration (which is proportional to the reaction rate) as a function of CO inlet concentration at four different temperatures in an atmospheric reactor over a pulverized Pt/silica/alumina catalyst. Oscillation existence regions are indicated by vertical hatching (from Ref. 98). (b) Work function maxima and minima plotted as a function of CO pressure at 540 K on Pt(l 10). The periodicity of the oscillations (as indicated above the curve) is seen to increase as CO pressure is decreased. (From Ref. 231.)...
The following 5-day biochemical oxygen demand (BOD5) and total suspended solids (TSS) data were collected from a clarifier at a local municipal wastewater treatment plant over a 7-day period. The National Pollutant Discharge Elimination System (NPDES) permit limitations for BOD5 and TSS effluent concentrations from this wastewater treatment plant are 45mg/L on a 7-day average. Based on this information, is the treatment plant within its NPDES permit limits ... [Pg.590]

Daily BOD5 and TSS Effluent Concentration Data Collected Over a 7-Day Period at a Municipal Wastewater Treatment Plant... [Pg.590]

Toxic units are a measure of toxicity in a sample as determined by the acute toxic units (TUa) or chronic toxicity units (TUC) measured. An acute toxic unit is the reciprocal of the effluent concentration that causes 50% of the organisms to die by the end of the acute exposure period (USEPA, 1991c). It is calculated by expressing the real or true concentration of the effluent as the numerator (which for an effluent will be 100%) and the lethality end-point as the denominator, as follows ... [Pg.104]

Chronic toxic units (TUC) can be calculated in the same way as with acute exposure (USEPA, 1991c). The TUC is the reciprocal of the effluent concentration that causes no observable effect on the test organisms by the end of the chronic exposure period (i.e. 100/NOEC). It needs to be remembered, however, that TUa and TUC values are different and cannot be mixed in the calculations. Toxic units are dimensionless, so values obtained with other samples and compounds can be compared. Because these values depend on the organism and the end-point used, these data should always be reported (Scroggins, 1999). [Pg.104]

Belter and co-workers developed a periodic countercurrent process for treating a fermentation broth to recover novobiocin. They found that they were able to scaleup the laboratory results to production operations if the two systems have similar mixing patterns and the same distribution of residence times in the respective columns. The mixing patterns are the same when the space velocity (F/%) and the volume ration (f /c) are the same. This is shown in Fig. 22 for the effluent concentration of novobiocin from laboratory and production columns. [Pg.431]

The experimental columns, both in vitro and in vivo, cleared 90-95% of the bilirubin in the blood. Cbntrol columns had no effect on serum bilirubin concentrations. Serum bilirubin concentrations in the treated rats and reservoirs fell less rapidly than effluent concentrations, presumably because of mixing with untreated blood. In a series of six experiments in vitro, serum bilirubin concentration in the blood reservoir decreased on the average by 61% within 30 min. In a series of six experiments in vivo, serum bilirubin concentration in the rats decreased by 50% within 30 min and remained low even after the enzyme treatment, indicating that a short period of exposure rapidly lowers the bilirubin level in rats (Fig. 14) (55). [Pg.37]

Using this information, determine the reactor effluent concentration and reactor volume necessary to fulfill payback periods of 2,5, and 10 years. Recall from Section 5.5.5.1 that the volumetric flow rate of the feed to the reactor network is Q = 1.2 L/s. [Pg.138]

Several studies have been conducted to measure methyl parathion in streams, rivers, and lakes. A U.S. Geological Survey (USGS) of western streams detected methyl parathion in five river samples taken from four states during a 14-month period in 1970 and 1971. The amount of methyl parathion detected ranged from 0.04 to 0.23 pg/L (Schultz et al. 1973). A later and more extensive USGS study analyzed water samples from major rivers of the United States four times yearly in the period of 1975-1985. Of the 2,861 water samples, 0.1% had detectable levels of methyl parathion (Gilliom et al. 1985). In a study of Arkansas surface waters, samples of lake and river/stream water were collected and analyzed over a three-year period (Senseman et al. 1997). Of the 485 samples collected, methyl parathion was found in one river/stream sample at a maximum concentration of 3.5 pg/L. Results from an EPA study in California detected methyl parathion in 3 of 18 surface drain effluent samples at concentrations of 10-190 ng/kg. Subsurface drain effluent water had concentrations of 10-170 ng/kg in 8 of 60 samples (lARC 1983). [Pg.158]

The reactivities of spray-dried sorbents were examined in a fast fluidized bed. The reactor was operated at a carbonation temperature of 50 °C, and a gas velocity of 2 m/s with an initial sorbent inventory of 7 kg to compare CO2 concentration profiles in effluent gas for spray-dried Sorb NH series and NX30 sorbent. Figure 5 shows the comparison of CO2 concentration profiles in effluent gas of Sorb NHR, NHR5, and NX30 in a fast fluidized-bed reactor. The CO2 removals of Sorb NHR and NHR5 were initially maintained at a level of 100 % for a short period of time and quickly dropped to a 10 to 20 % removal level. [Pg.503]


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