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Columns estimating

Prepare a mechanical design of the chlorobenzene column, estimating the shell thickness, the positions and sizes of all nozzles, and the method of support for the plates and the column shell. Make a dimensioned sketch suitable for submission to a drawing office. [Pg.969]

Figure 25-24 Time (/m) for mobile phase fo traverse a 4.6-mm-diameter HPLC column, estimated with the equation fm Ldl/(2F), where L is the length of the column (cm), dc is the column diameter (cm), and F is the flow rate (mL/min). [Pg.576]

ID The following substances were separated on a gel filtration column. Estimate the molecular mass of the unknown. [Pg.625]

For tropospheric ozone, the residual technique was pioneered by Fishman et al. (1990), who used total O3 column, estimated from TOMS, combined with the co-located stratospheric ozone profiles from SAGE or SBUV in a series of studies to demonstrate the presence of elevated tropospheric ozone for large-scale pollution events (Fishman et al., 1991 1992 1996). [Pg.314]

The process for making cyclohexane by saturation of benzene consists of a feed-effluent heat exchanger, a saturation reactor, and a product stabilizer column. Estimate the cost of a plant that produces 200,000 metric tons per year (200 kMTA) of cyclohexane using the correlation in Table 6.2 and Bridgewater s method. [Pg.312]

Figure 3 Dowex AB 1-X8 borate resin micro-column estimation of tritiated water released from 1 mM... Figure 3 Dowex AB 1-X8 borate resin micro-column estimation of tritiated water released from 1 mM...
With resolution IV designs, we can completely separate all the main effects from the two-factor interactions, as shown in Table 4.16. The contrasts corresponding to the actual columns of the design estimate the main effects of the eight variables, while the contrasts defined by products of two columns estimate combinations of two-factor interactions. ... [Pg.173]

Loadabillty of columns estimated as described by Karch [11], was found to be comparable for both branched and unbranched packings. Values between 5.10 -A and 1.10 -5 g per gram of packing were found, depending on carbon content of the packing and solute used for this estimation. [Pg.60]

D4. We wish to repeat the distillation in Examples 10-2 and 10-3 except that valve trays will be used. The valves have a 2-inch diameter head. For the top of the column, estimate the pressure drop vs. hole velocity curve. Assume that and values are the same as in Figure 10-21. Each valve weighs approximately 0.08 pound. [Pg.428]

The batch distillation column in Problem 9.D23 is a 6-inch diameter packed column that is packed with 5/8-inch metal Pall rings. Operate at a vapor flux that is 70% of flooding. Design for conditions at the end of the batch calculated at the bottom of the column. Estimate the viscosity as that of pure water at 100°C (0.26 cP). Find the operating time for the batch distillation with the packed column. [Pg.431]

You have 0.50 g of a mixture that you wish to purify by column chromatography. How much adsorbent should you use to pack the column Estimate the appropriate column diameter and height. [Pg.809]


See other pages where Columns estimating is mentioned: [Pg.1250]    [Pg.138]    [Pg.1250]    [Pg.524]    [Pg.30]    [Pg.298]    [Pg.274]    [Pg.37]    [Pg.892]    [Pg.552]    [Pg.371]    [Pg.361]    [Pg.618]    [Pg.65]    [Pg.724]    [Pg.431]    [Pg.274]    [Pg.47]    [Pg.274]    [Pg.84]   


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