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Why are there only a few hundred distinct values when there are thousands of products The probabilities are ratios between two numbers, the number of times that a product appears, and the number of orders. For all products, the number of orders is the same, so the number of different probabilities is the number of different frequencies of products. There is much overlap, especially because over one thousand products appear only once. With just a few hundred values, plotting them individually is possible as in Figure 9-7, which has both the histogram and the cumulative histogram. The histogram is on the left-hand axis. However, this histogram is visually misleading, because the points are not equally spaced.
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A Gradient fill is applied in a slightly different manner than a Solid or Pattern fill. To apply a Gradient fill, follow these steps: 1. Select your object. 2. Select the Gradient tool from the flyout menu under the Paint Bucket tool, or by pressing the keyboard shortcut, G, twice. 3. From the Fill category option list in the Fill section of the Property inspector, choose one of the gradient options. When the selected gradient is initially applied, the current Stroke and the Fill colors are used to create the blend. 4. Click on the Fill color well in the Property inspector and the Edit Gradient pop-up dialog box appears. You can use the preset gradient colors that Fireworks offers, shown in Figure 11-6, or you can simply use one as a base and modify any colors to suit your graphic needs.
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The final object in the Characters menu is used for inserting these or any other character entity. The Insert Other Character object displays a large table with symbols for 99 different characters, as shown in Figure 6-28. Simply select the desired symbol, and Dreamweaver inserts the appropriate HTML code at the current cursor position. By the way, the very first character which appears to be blank actually inserts the code for a nonbreaking space, also accessible via the keyboard shortcut Ctrl+Shift+spacebar (Command+Shift+spacebar). The nonbreaking space is also available in the Characters menu in the Text category of the Insert bar.
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Going with the ow
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Hoogendoorn, C. J., and A. P. den Hartog (1967). Model studies on mixers in the viscous ow region, Chem. Eng. Sci., 22, 1689 1699. Jaworski, Z., A. W. Pacek, and A. W Nienow (1994). On the ow close to cavern boundaries in yield stress uids, Chem. Eng. Sci., 49, 3321 3324. Johnson, R. T. (1967). Batch mixing of viscous liquids, IEC Proc. Des. Dev., 6, 340 345. Khang, S. J., and O. Levenspiel (1976). New scale-up and design method for stirrer agitated batch mixing vessels, Chem. Eng. Sci., 31, 569 577. Kramers, H., G. M. Baars, and W. H. Knoll (1953). A comparative study of the rate of mixing in stirred tanks, Chem. Eng. Sci., 2, 35 42. Langheinrich, C., T. Eddleston, N. C. Stevenson, A. N. Emery, T. M. Clayton, N. K. H. Slater, and A. W. Nienow (1998). Liquid homogenisation studies in animal cell bioreactors of up to 8 m3 in volume, Food Bioprod. Process. (Trans. Inst. Chem. Eng. C), 76, 107 116. Manikowski, M., S. Bodemeier, A. L bbert, W. Bujalski, and A. W. Nienow (1994). u Measurement of gas and liquid ows in stirred tank reactors with multiple agitators, Can. J. Chem. Eng., 72, 769 781. Metzner, A. B., and R. E. Otto (1957). Agitation of non-Newtonian uids, AIChE J., 3, 3 10. Nagata, S., M. Nishikawa, H. Tada, and S. Gotoh (1971). Power consumption of mixing impellers in pseudo-plastic liquids, J. Chem. Eng. Jpn., 4, 72 76. Nienow, A. W. (1997). On impeller circulation and mixing effectiveness in the turbulent ow regime, Chem. Eng. Sci., 52, 2557 2565. Nienow, A. W., and T. P. Elson (1988). Aspects of mixing rheologically complex uids, Chem. Eng. Res. Des., 66, 5 15. Norwood, K. W., and A. B. Metzner (1960). Flow patterns and mixing rates in agitated vessels, AIChE J., 6, 432 437. Okita, N., and Y. Oyama (1963). Mixing characteristics in jet mixing, Jpn. Chem. Eng., 1, 92 101. Otomo, N., W. Bujalski, and A. W. Nienow (1993). Mixing time measurements for an aerated, single- and double-impeller stirred vessel by using a conductivity technique, Proc. 1993 Institution of Chemical Engineers Research Event, Birmingham, Jan., pp. 669 671. Otomo, N., W. Bujalski, and A. W. Nienow (1995). An application of a compartment model to a vessel stirred with either dual radial or dual axial ow impellers, Proc. 1995 Institution of Chemical Engineers Research Event, Edinburgh, Jan. pp. 829 831. Perry, R. H., and D. Green (eds.) (1984). The Chemical Engineers Handbook, 6th ed., Mcgraw-Hill, New York, Sec. 6. Pollard, J., and T. A. Kantyka (1969). Heat transfer to agitated non-Newtonian uids, Trans. Inst. Chem. Eng., 47, T21 T27. Proch zka, J., and J. Landau (1961). Studies on mixing: XII. Homogenisation of liquids a in the turbulent regime, Coll. Czech. Chem. Commun., 26, 2961 2973. R` cz, I., and J. G. Wassink (1974). Str mungsverlauf und Mischzeiten in axialen a o Strahlmischern, Chem. Ing. Tech., 46, 261. Rajaratnam, N. (1986). In The Encyclopaedia of Fluid Mechanics, Vol. 2, N. Cheremisnoff, ed., Gulf Publishing, Houston, TX, Chap. 15.
1. While drawing a path, create a straight segment by clicking and releasing the mouse button, moving the Pen pointer, and then clicking and releasing the mouse button again. 2. Move the Pen pointer over the last anchor point you created in Step 1. The Convert Point icon appears. (It looks like the regular Pen icon except that a small triangle missing its base appears at the icon s lower right.) 3. Click, drag, and then release the mouse button to create the direction line that determines the slope of the next segment. 4. Move the Pen pointer to where you want to establish the next anchor point and then click and drag to complete the curved segment.
sent. For more information, refer to the sidebar titled Declaring the Encoding Type (Enctype) in this chapter. Finally, the Target field tells the server which frame or window to use when displaying a response to the form. If you don t specify a target, any response displays in the current frame or window.
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