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43 ILab: An Advanced User Interface Approach for Complex Parameter Study Process Speci cation on the Information Power Grid, Yarrow, M, McCann, K M, Biswas, R and Wijngaart, R F V D (2000) Grid 2000: First IEEE/ACM International Workshop, Bangalore, India, 2000, http://wwwipgnasagov/research/papers/nas-00-009pdf The creation of parameter study suites has recently become a more challenging problem as the parameter studies have become multitiered and the computational environment has become a supercomputer Grid The parameter spaces are vast, the individual problem sizes are getting larger, and researchers are seeking to combine several successive stages of parameterization and computation Simultaneously, Grid-based computing offers immense resource opportunities but at the expense of great dif culty of use We present ILab, an advanced graphical user interface approach to this problem.

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Our novel strategy stresses intuitive visual design tools for parameter study creation and complex process speci cation and also offers programming-free access to Grid-based supercomputer resources and process automation 44 US-CMS Testbed Production Joint News Update with GriPhyN/iVDGL, Particle Physics Data Grid, 2002, http://wwwppdgnet/ppdg newshtm Members of the CMS experiment working in concert with PPDG, iVDGL, and GriPhyN have carried out the rst production-quality simulated data generation on a data Grid comprising sites at Caltech, Fermilab, the University of California-San Diego, the University of Florida, and the University of Wisconsin-Madison This is a combination of efforts supported by DOE SciDAC, HENP, MICS, and the NSF as well as the EU funded EU DataGrid project.

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identical relationship is valid with boiling solutions in which the elevation of boiling point would have the same effect as that of signi cant increases in impeller submergence. It is also unlikely that liquid viscosity will have a signi cant in uence as long as the Reynolds number is high. These two facts encourage the conclusion that the results will be valid for all low viscosity liquids. The locus of the limiting power appropriate to ooding an 0.18 m diameter Rushton impeller at a submergence of 0.3 m is also shown in Figure 11-15. The much higher relative power demand of an impeller in rapidly boiling liquid compared with that in the near- ooded, cold-sparged condition at the same shaft speed (i.e., of Fr or Sm) is evident. These boiling cavitation and (cold) gas ooding lines represent limits between which a sparged boiling reactor might be expected to operate. Example 11-3: Impeller Power in a Boiling Crystallizer. An upward-pumping pitched blade impeller of 0.6 m in diameter is to be speci ed for a boiling crystallizer in which it is submerged by 0.7 m. If the critical Smith number for this impeller is 1.3 with RPD obeying a Sm0.4 law, and the RPD is not to be lower than 60% of the ungassed value, what is the maximum speed at which the impeller should be driven See Table 11-8 for the calculations. The relevant equations, which are solved using TK Solver or a similar program, are FlG = QG ND3 Fr = N2 D g PU = Po N3 D5 L 2gS 2 = 2 2 vt S D 1 Fr vt = ND

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