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, Unsteady-State Multicomponent Gaseous Diffusion, PhD Thesis in Chemical Engineering, Carnegie Institute of Technology, Pittsburgh, PA, 1965 Arnold, K R and Toor, H L, "Unsteady Diffusion in Ternary Gas Mixtures," AIChE J, 13, 909-914 (1967) Arwickar, K J, Mass Transfer in Packed Column Absorption and Multicomponent Distillation, PhD Thesis in Chemical Engineering, University of California, Santa Barbara, CA, 1981 Austin, D G and Jeffreys, G V, The Manufacture of Methyl Ethyl Ketone from 2-Butanol, The Institution of Chemical Engineers, Rugby, England, 1979 Bandrowski, J and Kubaczka, A, "On the Condensation of Multicomponent Vapors in the Presence of Inert Gases," Int J Heat Mass Transfer, 24, 147-153 (1981) Bandrowski, J and Kubaczka, A, "On the Prediction of Diffusivities in Multicomponent Liquid Systems," Chem Eng Sci, 37, 1309-1313 (1982) Bell, K J and Ghaly, M A.



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Since these key decision makers may not be easily available to you, you have to be ready to tell them your vision and how they can help in a condensed way, at a moment s notice. This is where you can use your change vision the 30-second rocket pitch or elevator speech that you can pull out in an instant if you happen to be on the elevator or walking down the corridor with one of the decision makers. At Montefiore Hospital some time ago, a number of executives sheepishly confessed that they had discovered that one of the few ways to get ideas to the world-famous and no-

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while [ $var1 -ge 0 ] do echo "Outer loop: $var1" for (( var2 = 1; $var2 3; var2++ )) do var3=$[ $var1 * $var2 ] echo " Inner loop: $var1 * $var2 = $var3" done var1=$[ $var1 - 1 ] done $ ./test15 Outer loop: 5 Inner loop: 5 * 1 = 5 Inner loop: 5 * 2 = 10 Outer loop: 4 Inner loop: 4 * 1 = 4 Inner loop: 4 * 2 = 8 Outer loop: 3 Inner loop: 3 * 1 = 3 Inner loop: 3 * 2 = 6 Outer loop: 2 Inner loop: 2 * 1 = 2 Inner loop: 2 * 2 = 4 Outer loop: 1 Inner loop: 1 * 1 = 1 Inner loop: 1 * 2 = 2 Outer loop: 0 Inner loop: 0 * 1 = 0 Inner loop: 0 * 2 = 0 $

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, "An Approximate Generalized Design Method for Multicomponent/Partial Condensers," AIChE Symp Ser, 69, 72-79 (1972) Bennett, D L, Agrawal, R, and Cook, P J, "New Pressure Drop Correlation for Sieve Tray Distillation Columns," AIChE J, 29, 434-442 (1983) Biddulph, M W, and Kalbassi, M A, "Distillation Efficiencies for Methanol/1-Propanol/Water," Ind Eng Chem Res, 27, 2127-2135 (1988) Biddulph, M W Kalbassi, M A, and Dribicka, M M, "Multicomponent Efficiencies in Two Types of Distillation Column," AIChE J, 34, 618-625 (1988) Billet, R, Distillation Engineering, Chemical Publishing Co, New York, 1979 Bird, R B, Stewart, W E, and Lightfoot, E N, Transport Phenomena, Wiley, New York, 1960 Blom, J, An Experimental Determination of the Turbulent Prandtl Number in a Developing Temperature Boundary Layer, PhD Thesis, Technical University of Eindhoven, The Netherlands, 1970 Bolles, W L.

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Photoshop has background and foreground colors on the toolbar. Illustrator has a fill color and a stroke color. Fill and stroke are both foreground colors. The background color in Illustrator is always transparent. If you double-click the Fill or Stroke on the toolbar, you open the Color Picker, shown in Figure 5.23. For icons, you should use the RGB settings or enter the RGB hex number directly. To the upper right of the Fill and Stroke icons is a double-headed arrow pointing at the Fill and Stroke. Clicking this icon swaps the Fill and Stroke colors of the currently selected shape. To the bottom right of the Fill and Stroke icons is the Default Fill and Stroke icon. It looks like a smaller version of the Fill and Stroke icon. The default colors are black and white. Figure 5.23 Color Picker

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