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Time to volume

The commercial production of cellulosic ethanol is moving closer with advances in technology along with federal and private funding for new plants and research centers. These are accelerating the time to volume production which could push the cost of ethanol from cellulosic feedstocks to well under 1.00 a gallon below the cost of corn ethanol. [Pg.99]

The variance in volume units of the output function of the chromatographic system can be simply obtained by combining eqns. fl,9 and 11, and converting time to volume units by multiplying by the flow rate, which results in ... [Pg.7]

Figure 3.9 Ratio of filtration time to volume as a fimction of total volume of filtered water, showing the three dominant filtration mechanisms of A blocking filtering B cake filtration C cake blocking/ compaction. The MFl is represented as the slope of the linear curve during cake filtration. Figure 3.9 Ratio of filtration time to volume as a fimction of total volume of filtered water, showing the three dominant filtration mechanisms of A blocking filtering B cake filtration C cake blocking/ compaction. The MFl is represented as the slope of the linear curve during cake filtration.
Time to market and time to volume are powerful metrics employed by companies such as Sony and Canon where short iife cycles dictate a focus on rapid response to fast-changing technoiogies and voiatiie customer demand. [Pg.116]

The time span within which a new product is ramped up after the end of product development to stable volume production is called the ramp-up phase (Fig. 9.1). In accordance to Terwiesch et al., time-to-volume attracted reasonable more attention than time-to-market already at the beginning of the century (Terwiesch et al. 2001, p. 435). The fundamental difference between time-to-market and time-to-volume is... [Pg.221]

Because the characteristic of tubular reactors approximates plug-flow, they are used if careful control of residence time is important, as in the case where there are multiple reactions in series. High surface area to volume ratios are possible, which is an advantage if high rates of heat transfer are required. It is sometimes possible to approach isothermal conditions or a predetermined temperature profile by careful design of the heat transfer arrangements. [Pg.54]

Place 84 g. of iron filings and 340 ml. of water in a 1 - 5 or 2-litre bolt-head flask equipped with a mechanical stirrer. Heat the mixture to boiling, stir mechanically, and add the sodium m-nitrobenzenesulphonate in small portions during 1 hour. After each addition the mixture foams extensively a wet cloth should be applied to the neck of the flask if the mixture tends to froth over the sides. Replace from time to time the water which has evaporated so that the volume is approximately constant. When all the sodium salt has been introduced, boU the mixture for 20 minutes. Place a small drop of the suspension upon filter paper and observe the colour of the spot it should be a pale brown but not deep brown or deep yellow. If it is not appreciably coloured, add anhydrous sodium carbonate cautiously, stirring the mixture, until red litmus paper is turned blue and a test drop upon filter paper is not blackened by sodium sulphide solution. Filter at the pump and wash well with hot water. Concentrate the filtrate to about 200 ml., acidify with concentrated hydrochloric acid to Congo red, and allow to cool. Filter off the metanilic acid and dry upon filter paper. A further small quantity may be obtained by concentrating the mother liquid. The yield is 55 g. [Pg.589]

Dissolve 20 g, (19 -6 ml.) of anihne in a mixture of 55 ml. of concentrated hydrochloric acid (1) and 55 ml. of water contained in a 350 ml, conical flask. Place a thermometer in the solution and immerse the flask in a bath of crushed ice (2) cool until the temperature of the stirred solution falls below 5°, Dissolve 16 g. of sodium nitrite in 75 ml. of water and chUl the solution by immersion in the ice bath add the sodium nitrite solution (3) in small volumes (2-3 ml. at a time) to the cold anihne hydrochloride solution, and keep the latter weh stirred with the thermometer. Heat is evolved by the reaction. The temperature should not be allowed to rise above 10° (add a few grams of ice to the reaction mixture if necessary) otherwise appreciable decomposition of the diazonium compound and of nitrous acid wih occur. Add the last 5 per cent, of the sodium nitrite solution more slowly (say, about 1 ml. at a time) and, after stirring for 3-4 minutes, test a drop of the solution diluted with 3-4 drops of water with potassium iodide - starch paper (4) if no immediate blue colour... [Pg.598]

The sodium sulphite solution may also be prepared by dissolving 100 g. of pure (or a corresponding quantity of commercial) sodium hydroxide in about 125 ml. of water, and then diluting to 750 ml. The flask is cooled in running water, a few drops of phenolphthalein indicator are added, and sulphur dioxide passed in until the pink colour just disappears (it is advisable to add a further 1-2 drops of the indicator at this point) and then for 2-3 minutes longer. It is best to remove a sample for test from time to time, dilute with 3-4 volumes of water, and test with I drop of phenolphthalein. [Pg.637]

Phenolsulphonephthalein (phenol red). Mix 10 g. of o-sulpho-benzoic anhydride (Section VIII,9), 14 g. of pure phenol and 10 g. of freshly fused zinc chloride in a small conical flask. Place a glass rod in the flask and heat gently over a flame to melt the phenol. Then heat the flask containing the well-stirred mixture in an oil bath at 135-140° for 4 hours. Stir from time to time, but more frequently during the first hour if the mixture froths unduly, remove the flask from the bath, cool and then resume the heating. When the reaction is complete, add 50 ml. of water, allow the water to boil and stir to disintegrate the product. Filter the crude dye with suction and wash it well with hot water. Dissolve the residue in the minimum volume of warm (60°) 20 per cent, sodium hydroxide solution, filter, and just acidify the filtrate with warm dilute hydrochloric acid (1 1). Filter the warm solution, wash with water, and dry upon filter paper. The yield of phenol red (a brilliant red powder) is 11 g. [Pg.990]

Besides the solute peak, Figure 12.7 also shows a small peak eluted soon after the sample is injected into the mobile phase. This peak results from solutes that move through the column at the same rate as the mobile phase. Since these solutes do not interact with the stationary phase, they are considered nonretained. The time or volume of mobile phase required to elute nonretained components is called the column s void time, or void volume. [Pg.549]

It is convenient to begin by backtracking to a discussion of AS for an athermal mixture. We shall consider a dilute solution containing N2 solute molecules, each of which has an excluded volume u. The excluded volume of a particle is that volume for which the center of mass of a second particle is excluded from entering. Although we assume no specific geometry for the molecules at this time, Fig. 8.10 shows how the excluded volume is defined for two spheres of radius a. The two spheres are in surface contact when their centers are separated by a distance 2a. The excluded volume for the pair has the volume (4/3)7r(2a), or eight times the volume of one sphere. This volume is indicated by the broken line in Fig. 8.10. Since this volume is associated with the interaction of two spheres, the excluded volume per sphere is... [Pg.554]

Port-type ted dessert wines require skin contact time to extract the anthocyanins, but the fermentation must be short to retain the sugar level neat the 6—10% level desired. The winemaker cannot always achieve desired composition in individual lots. In order to teach the desired standard, it is necessary to make new lots to enable blending to that standard. The right volume of a tedder, less sweet wine will need to be made to bring to standard a lot with low color and mote sugar, for example, while keeping the alcohol also within the desired limits. [Pg.374]

Fig. 11. Changes ia mixing parameters on scale-up to 125 times the volume of the pilot plant. Fig. 11. Changes ia mixing parameters on scale-up to 125 times the volume of the pilot plant.
Starches are quite hydrophilic and the granules swell in water to several times their volume. In the preparation of starches for coating, the granules are heated at 93°C to ensure complete breakdown. The starch is then mixed with the pigment while it is fluid. Normal practice is to coat the paper at an elevated temperature to help control viscosity. [Pg.10]


See other pages where Time to volume is mentioned: [Pg.2098]    [Pg.45]    [Pg.105]    [Pg.25]    [Pg.166]    [Pg.2098]    [Pg.45]    [Pg.105]    [Pg.25]    [Pg.166]    [Pg.40]    [Pg.230]    [Pg.455]    [Pg.103]    [Pg.236]    [Pg.297]    [Pg.473]    [Pg.610]    [Pg.631]    [Pg.716]    [Pg.765]    [Pg.916]    [Pg.998]    [Pg.236]    [Pg.210]    [Pg.213]    [Pg.421]    [Pg.548]    [Pg.770]    [Pg.251]    [Pg.411]    [Pg.178]    [Pg.581]    [Pg.191]    [Pg.384]    [Pg.384]    [Pg.233]    [Pg.197]    [Pg.376]   
See also in sourсe #XX -- [ Pg.116 ]




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