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Conpar method

When the sample has been processed, the result exists as a patch (or stain) on a 5 pm (usually ungridded) membrane, and this is then matched to a manbrane filter colour rating scale, based on quantitative and/or gravimetric levels of contamination. Accuracy levels by this method are lower than those obtained in methods such as the one previously described. The reason for the higher accuracy of the Conpar method is almost certainly the closer control of the membrane (0.8 pm) coupled with a viewing system that is, at its lowest point, 50-100 times better than the naked eye. [Pg.344]

Methods which enploy liquid phase treating liquors (spray, transfer rolls and belts, etc.) share a cannon difficulty stemming from the lew volume of liquor in relation to the large surface area of the fibers conprising the substrate to be treated. This difficulty is acerbated when aqueous liquors are to be applied to hydrophilic fibers. Foam coating methods enploy stable foams which allow the thickness of the liquid-air mixture to be controlled by a doctor blade or roll. Conparatively low add-ons can be achieved by virtue of the low density of the foam layer, but the stable nature of such foam, and its immobile liquid phase, inhibit rapid, uniform distribution through the substrate. [Pg.145]

The design of new methods to prepare peptide analogues, i.e. peptidomimetics, is an area of growing importance in pharmaceutical design (1-2). The incorporation of peptidomimetics into peptides can lead to a number of beneficial features, including increased proteolytic stability, improved bioavailability, decreased side-effects and higher selectivity and potency conpared to the parent peptide sequence... [Pg.502]

Now, cancel screens until you get back to the flowsheet (simulators run faster if there are not a large number of open screens). Go to Data in the menu and click on properties. In the Global screen, change the base method for VLE to NRTL-2. Click on Next. Continue clicking OK and redo the run. Check the results. Write these results down or print the plots. Compare the vapor and liquid products with this equilibrium data to the previous run. Go to Analysis and look at the T-x-y and the x-y plots. Conpare to the VLE data in the textbook (the most accurate comparison is with Table 2-lL... [Pg.116]

B. Explore. Except for some slight changes in the feed tenperature and column pressure, this problem is very similar to Example. VI. The solution for B and D obtained in that exanple is still correct. B = 6667 k h, D = 3333 kg/h. Equilibrium data are available in weight fractions in Figure 2-4 and in mole fraction units in Figure 2-2 and Table 2-1. To use the Lewis method we must have CMO. We can check this by conparing the latent heat per mole of pure ethanol and pure water. (This checks the third and most inportant criterion for CMO. Since the column is well insulated, the first criterion, adiabatic, will be satisfied.) The latent heats are (Himmelblau. 1974) ... [Pg.150]

Xq average conpare the three methods. Equilibrium data are in Table 2-7. Logically, parts b and c should give the same result. If they don t, there is probably a numerical error from the use of Sinpson s rule. Try dividing an area into two parts for more accuracy. [Pg.378]

D19. Repeat Problems 10.D9 and 10.D13 using the two-enthalpy feed method in which a portion of the feed is condensed to a saturated liquid and the remainder is still a saturated vapor. Select the amount of feed to condense so that the column has pinch points at minimum reflux at both the liquid and the vapor feed simultaneously. Use the same multiplier M as in Problem 10.D13. Conpare the diameter of this column to the diameter of 10.27 feet calculated for Problem 10.D9 and to the diameter calculated for Problem 10.D13. Calculate the ratio QR,2-entha]py feed ... [Pg.430]

Meyers extension and Chan s modification represent one-pot conversions of sulfones into alkenes. These are almost invariably used in modern synthetic applications due to the in )roved convenience and synthetic efficiency conpared to the classic (two-step) RBR. The Chan method is recommended as the first choice when contemplating the use of the RBR in synthesis. This is due to the highly dispersed nature of the solid-supported base, which provides more reliable reactivity. [Pg.291]

DFT approaches conpared to HF, even higher quality results might be expected with the use of methods such as B3LYP hence, DFT is often now the method of choice for calculations on medium to large organic molecules. [Pg.382]

Conpared to the knowledgebase on the practical use of Pechini method for synthesis of different oxide materials, relatively little is known about chemistry of this technique. Most of the fundamental studies on citric acid and its metal conplexes were carried out in 60 and 70 s—either before Pechini publication or right after it when polymerizable complex method has not deserved much attention yet. Therefore most of the results are not directly related to polymerizable complex method. More recent studies on the chemistry ofPechini method often were carried out by material scientists with necessary chemistry background and focused on very specific questions or narrow set ofparticular problems. We will attempt... [Pg.79]

For larger retrofit projects, discounted profitability criteria should be used. The algorithm to conpare alternatives using discounted cash flows follows the same four-step method outlined in Section 10.3. For small retrofit projects, nondiscounted criteria may often be sufficiently accurate for conparing alternatives. Both types of criteria are discussed in the next sections. [Pg.316]

The concept of incremental economic analysis was introduced and applied to an exanple involving large capital budgets and also to a retrofit project. It was shown that both the net present value (JVPV) and equivalent annual operating cost (EAOC) methods were particularly useful when conparing alternatives using discounted cash flows. [Pg.339]

Using the results from Problem 1 above and Tables 1.5 and LI, conpare the results for the simulation of the benzene recovery column, T-101, using a shortcut method and a rigorous method. One way to do this comparison is to use the number of theoretical plates from the shortcut method as an input to the rigorous method. The rigorous method is used to simulate the same separation as the shortcut method, that is, same overhead purity and recovery. The difference in the methods is then reflected by the difference between the reflux required for both methods. Comment on the difference for this nearly ideal system Remember that there is no need to simulate the whole flowsheet for this problem just use the input to the column from Table 1.5. [Pg.437]

Having built the models, we must now examine methods to conpare them with the experiment and deduce the values of the characteristic properties. [Pg.443]

The vortex development of a low-density polyethylene in different flat dies under various proeessing conditions has been analyzed by the Finite Element Method enploying the modified White-Metzner model as constitutive equation. The theoretical results are conpared with the velocity distributions measured by Laser-Doppler Velocimetry (LDV). [Pg.1068]


See other pages where Conpar method is mentioned: [Pg.304]    [Pg.47]    [Pg.425]    [Pg.31]    [Pg.137]    [Pg.101]    [Pg.22]    [Pg.119]    [Pg.154]    [Pg.349]    [Pg.417]    [Pg.918]    [Pg.81]    [Pg.365]    [Pg.467]    [Pg.41]    [Pg.139]    [Pg.539]    [Pg.63]    [Pg.285]    [Pg.314]    [Pg.409]    [Pg.430]    [Pg.417]    [Pg.841]    [Pg.2347]   
See also in sourсe #XX -- [ Pg.344 ]




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