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Shortly after Flash 4 was released, Macromedia wrote a Flash Writer plug-in for Illustrator 8 that enabled the direct export of .SWF files. This free download from the Macromedia Web site bypasses many problems with using .EPS and .AI files in Flash 4 and 5. Notably, the Flash Writer plug-in can convert EPS blends into Flash gradients. After you download the plug-in from Macromedia, you ll receive an e-mail with a serial number so that you can run the installation on your system. To export .SWF files in Illustrator 8, follow these steps: 1. Run the Illustrator application and open your artwork file. 2. Access the Export command in the File menu, and select Flash Player .SWF in the Format drop-down menu of the Export dialog. Select a folder or directory to store your .SWF file, and type a name for the file. Make sure you specify .SWF at the end of the filename. Click Save. 3. In the Flash Writer dialog (shown in Figure 31-7), select the options for your .SWF file. The dialog contains these options: Image Settings: These options control the compression of any placed bitmaps in your Illustrator file. We recommend setting the compression type to JPEG (lossy) at Medium or Medium-High quality, and the dpi setting at 72 to reduce file size. File and Objects: Use these options to set the Flash version (2, 3, or 4), and to control how the artwork structures are mapped to Flash gradients and frames. If you re not planning to bring the .SWF back into Flash for further editing, you ll want to enable the Export File as Protected option.

The support for the inverse rule is exactly the same as the support for the original rule, because the two rules have the same combination of products. Perhaps more surprising, the lift for the two rules is the same as well. This is not a coincidence; it comes from the definition of lift. The formula simplifies to:

Panel Files Assets Keyboard Shortcut F8 F11 Description Manages the files in your local, remote, and testing sites. Gives you access to many components that make up your site, including images, colors, URLs, Flash and Shockwave objects, movies, scripts, templates, and library items. Detailed Information See 5 See the following: Images: 9 Colors: 8 URLs: 10 Flash: 24 Shockwave: 24 Movies: 25 Scripts: 6 Templates: 27 Library: 28 See 8

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properties can be identi ed and quanti ed. Care should be taken that rheology measurements can be and are made at shear rates appropriate to those that will be found in the mixing system being investigated. The instrument should also allow the sensitivity of uid rheology to temperature (over the range to be experienced in the laboratory) to be investigated. Rheometers should be serviced and calibrated regularly.

When you set percentage sizing with the height and width properties, you declare the values with a percentage expression, such as 50%. This Label control s width is 50 percent of the available space within its container:

Some names, such as James and Gordon, George and John, Kim and Kelly and Lindsey, are common as both first and last names. Other names, though, almost always fall in one or the other categories. When the FIRSTNAME column contains values such as ABRAHAMSOM, ALVAREZ, ROOSEVELT, and

responsibility of the process researcher and/or process engineer to determine the pertinent and speci c process needs. Sometimes, results associated with other mixing operations blending, gas liquid, liquid liquid, heat transfer, and so on may be more important. Therefore, it is essential to consider and understand, early in the process development stage, all the physical and chemical phenomena necessary to achieve the desired process results. In particular, how these phenomena are in uenced by the process chemistry, the properties of the solid and liquid phases, and the operational variables of mixing must be understood. The key considerations include the: 1. Mode of process operations: batch, semibatch [continuous addition to batch (con-add)], or continuous 2. Phases solid, liquid, and/or gas phases that are present or occur from the beginning to the end of the process 3. Properties of the solid and liquid phases, including stickiness and tendency to agglomerate 4. Unit operations involved from the beginning to the end of the process 5. Vessel geometry and internals 6. Mixing parameters: local or average uid velocity or ow, local or average shear rates, blend time, power input, and so on.

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