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Figure 9-21 shows the nished org chart.
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64. Hussain, A. S. (2006), Quality by design and bioequivalence/bioavailability assessment, paper presented at the The Heidelberg PAT Conference 2006, Heidelberg, Germany. 65. Lyon, R. C., and Hammond, S. (2006), Process monitoring of pilot-scale pharmaceutical blends by near-infrared chemical imaging and spectroscopy, paper presented at the Eastern Analytical Symposium, Somerset, NJ. 66. D Sa, A. (2005), Process analytical technology (PAT): regulatory process, review and inspection, paper presented at the 19th International Forum on Process Analytical Technology IFPAC 2005, Arlington, VA. 67. Views on prescription drugs and the pharmaceutical industry, The Kaiser Family Foundation, 2005. 68. Arlington, S., Barnett, S., Hughes, S., Palo, J., and Shu, E. (2002), Pharma 2010: The threshold of innovation, IBM Business Consulting Services, Somers, NY. 69. Arlington, S., et al., (2005), The metamorphosis of manufacturing, IBM Business Consulting Services, Somers, NY.
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Fig. 5.6 PR18 stage The pbCFD default grid size of 21x71x21 (total of 31 311 nodes) was used for this study. All CFD control parameters were set to default values, including the use of the energy diffusion terms. The PR18 compressor was composed of 16 main blades. The inlet extension duct is bent 180 degrees prior to the impeller leading edge, and the downstream element stretches to a location more than a full length of the impeller. The downstream radial extension region was cut short by using a CFD replacement segment to force more grid points in the impeller section to provide better predictions. It took 20 CPU minutes on a Pentium 400 MHz processor for the mass flow solver to converge the solution to within 1 per cent of the design flow, 15 CPU min. to within 2 per cent of the design flow. The final mass flow at the end of the computation was recorded at 0.1503 kg/s, almost exactly to the design flow of 0.15 kg/s. The predicted rotor efficiency was 0.933, about two points lower than the measured data. Front cavity leakage is not included. In the computed results, the flow was well-guided through the blade passages, with no separation region observed in the flow field. The computational results with or without the energy diffusion terms only showed two tenths of a point difference in predicted rotor efficiency, possibly due to the two-dimensionality of the rotor blade and the low pressure ratio. Table 5.6 summarized the mass-averaged pbCFD results. An additional observation can be made from Table 5.6. Results are entered using only part of the inlet duct (90 degree inlet) and the full inlet duct which covers 180 degrees of turning. Once again, it is observed that modelling the full inlet is important. With only half of the inlet duct, the stage efficiency is computed at one point higher efficiency than with the full inlet duct.
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