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The best free PDF editor for editing PDFs . Merge, compress, create, add text , review and edit PDF files. Convert Word to PDF and image formats PNG, JPEG, ... Figure 6-28 shows changes in these parameters as the vessel volume is increased for several processes. The exponents x and y in Figure 6-28 should be determined experimentally or veri ed even for the processes listed in these plots. Some mixing equipment vendors prefer to use the TQ /V criterion because it has a direct impact on the overall size and cost of the mixer, including the gearbox. When choosing a scale-up method, one must consider changes in other ow and power parameters and their impact on the process result. Table 6-8 shows how these important parameters change on scale-up to 10 times the diameter and 1000 times the volume of laboratory mixing tank. Scale-up methods based on constant blend time require the mixer speed in the commercial vessel to be the same as in the laboratory vessel. This, however, results in a very large increase in the motor power. Such a demanding criterion is necessary for very fast to instantaneous reactions where the reaction lifetime may be a few seconds. Commercial reactors for such systems are, therefore, relatively small in size. Using constant P/V, the mixer speed decreases by 78%, but the blend time increases by a factor of 4.6. If constant P/V is used in scaling up a reacting system, the reactors may need to be sized for longer residence time than the laboratory reactor because of the increase in blend time. It should be noted that the Reynolds number increases by a factor of 21.5, and therefore, pdf editor software online free: Edit PDF - Free PDF Editor Working Directly in your Browser mac pdf editor online PDFzorro | edit pdf-files online
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