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Concentration-lime data

CDP7-P An understanding of bacteria transport is vital to the efficient operation of water flooding of petroleum reservoirs. [R. Lappan and H. S. Fogler. SPE Production Eng., 7(2), 167 (1992)]. Analyze the cell concentration lime data. [3rd Ed. P7-28aI... [Pg.469]

Evaluating the specific reaction rate from batch reaciar concentration-lime data... [Pg.151]

There are various major fields of application for chemical sensors environmental studies, quality control of chemically produced compounds and processed food and biomedical analysis, especially for medical diagnostics. In the field of environmental analysis there is a great demand for the type of continuous monitoring that only a sensor can provide, since the relevant parameter for toxicological risk assessment is always the dose (i.e., a concentration multiplied by an exposure lime). The study of environmental chemistry also depends upon a continuous data output that provides not only baseline levels but also a reliable record of concentration outbursts. Data networks can be used to accumulate multiple determinations of a particular analyte regardless of whether these are acquired simultaneously or at different times within a three-dimensional sampling space (which may have dimensions on the order of miles). [Pg.952]

Granular bed filters are used in ten coil coating plants to remove residual solids from the clarifier effluent, and are considered to be tertiary or advanced wastewater treatment. Chemicals may be added upstream to enhance the solids removal. Pressure filtration is also used in this industry to reduce the solids concentration in clarifier effluent and to remove excess water from the clarifier sludge. Figure 7.4 shows a granular bed filter and Table 7.13 presents the heavy metal removal data of a lime clarification and filtration system. [Pg.282]

Half-Life. Once these activation parameters have been determined lor a initiator, half-life times tit a given temperature, i.e.. the lime required for 50 decomposition at a selected temperature, and half-life temperatures for a given period, i.e.. the temperature required for 509f decomposition of an initiator over a given time, can be calculated. Half life data arc useful for comparing the activity or one initiator with another when the half-life data arc determined in the same solvent and at the same concentration and. preferably, when the initiators are of the same class. [Pg.840]

Part of this data in Table II is a series of British maceral concentrates. The Woolley Wheatly Lime sample is 93% fusinite while the Teversal Dunsil concentrate is 80% semifusinite with 13% fusinite. The Aldwarke Silkstone sample contains 43% semifu-sinite and 43% fusinite. The petrographic analysis of PSOC-2 reveals nearly equivalent amounts of fusinite, semifusinite, micrinite, and macrinite (6.8, 8.1, 7.5 and 8.5% respectively in the whole coal) while PSOC-858 contains primarily semifusinite as the inertinite. The differences in faH values for these iner-tinite samples are greater than the experimental error and these differences suggest that NMR techniques may be useful in characterizing the chemical structural differences between inertinite macerals. [Pg.94]

C/Co, in terms of a lime parameter r, at a number of values of a parameter Z, which involves the bed length Z. In Example 15.2, this diart is used to find the concentration profile of the effluent, the break and exhaustion times, and the % utilization of the adsorbent bed. In this case, the model affords a fair comparison with experimental data. [Pg.501]

Fig. 6-8. Experimental results of Cu in soil solution for McLaren soil vs. lime during adsorption and desorption for initial concentration C = 50 and 100 mg I, The solid and dashed curves are predictions based on parameters from adsorption data using the imilliiouclion and second-order models given in Tables 6-4 and 6-5, respectively. The irreversible mechanism was accounted for based on concurrent reactions. Fig. 6-8. Experimental results of Cu in soil solution for McLaren soil vs. lime during adsorption and desorption for initial concentration C = 50 and 100 mg I, The solid and dashed curves are predictions based on parameters from adsorption data using the imilliiouclion and second-order models given in Tables 6-4 and 6-5, respectively. The irreversible mechanism was accounted for based on concurrent reactions.
In most time-lag experiments, the initial downstream penetrant concentration. C,. is zero tied the upstream concentration Cj is assumed to he established instantaneously at its equilibrium value. Although 6 is an additional parameter not requited to evaluate permeability and solubility data, it is wise, when possible, to verify that the lime lags obeerved experimentally are consistent with the ptedlclious of Fick s Law. To perfonn this lest, oue needs only to fit an empirical eqnelion to the D(C) versus C data shown in Fig- 20.3-6 and to perform the integration indicated. 17... [Pg.1109]

Antiphotooxidative effect of carotenoids on the induction lime of soybean oil as measured by the Rancimat method. The effect of 100 ppm or 200 ppm capsanthin, P-carotene, or lutein on the photooxidative stability of soybean oil containing 200 ppm chlorophyll was measured by the Rancimat method after 4 hours light exposure at 2S°C. Preliminary studies showed that the induction lime of purified soybean oil containing 100 or 200 ppm carotenoids without chlorophyll was slightly lower than that of the blank sample which contained no carotenoids (data not shown. Therefore, there is no anti-autoxidative effect of carotenoids on the soybean oil- Table I shows that as the concentration of the carotenoids increased from 100 to 200 ppm, the induction time as well as the anti-photooxidation index (API) increased. The induction time of soybean oil containing the carotenoids was longer than that of (he control sample which contained no carotenoid however, it was still shorter than that of the blank sample which contained no carotenoid and no chlorophyll. [Pg.102]

Thus the three-quarters life (or any given fractional life) is also independent of concentration for a first-order reaction. Examination of the data shows that the first three-quarters life (time to [A] = 0.237 mol dm -) is about 80 min and by inteipolation the second (lime to [A] = 0.178 mol dm - ) is also about 80 min. Therefore the reaction is first-order and the rate constant is approximately... [Pg.452]

Initial laboratory tests aimed at stabilizing the arsenic at pH 5 and 8 showed a lead solubility of 30 an 32 ppm. These tests were carried out without excess lime addition. During the TCLP test, acetic acid is added so that the pH of the leach solution is not controlled at any particular value. This explains the relatively high Pb solubility. Phosphate was then added during the arsenic precipitation stage, again without excess alkaline material. The results of the TCLP tests with phosphate additions showed a Pb leachate concentration of 40 to 60 mg/1. These data indicate that phosphate alone is not able to control the leaching of the lead. [Pg.942]


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Concentration data

Liming

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