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As part of the process of managing data in your solutions, you may have call to synchronize disparate data sets in separate copies of the same solution (or in comparable solutions). For example, when your main database resides on the server at your office, and you go on offline field visits, taking a copy on your laptop (modifying records and adding new records as you go), a problem of synchronization of the two record sets (the server database and the laptop database) arises. On your return, you need to load the added and edited work from your laptop into the main solution file, but without deleting new records added by your colleagues while you were gone. An important feature of the import and export functionality in FileMaker is that it acts on the found set of records in the frontmost window showing a layout based on the Table Occurrence from which you re importing. To import only the new records you added while on your field trip:

ffice 2007 includes several new fonts, and the default font has been changed for all the Office applications. In the past, Excel s default font was 10-point Arial. In Excel 2007, the default font for the Office theme is 11-point Calibri. Most people will agree that Calibri is much easier to read, and it gives the worksheet a more modern appearance. If you use Excel 2007 to open a workbook created in a previous version, the default font will not be changed, even if you apply a document style (by choosing Page Layout Themes Themes). But here s an easy way to update the fonts in a workbook that was created using an older version of Excel: 1. Press Ctrl+N to open a new, empty workbook. The new workbook will use the default document theme. 2. Open your old workbook file. 3. Choose Home Styles Cell Styles Merge Styles. Excel displays its Merge Styles dialog box. 4. In the Merge Styles dialog box, select the new workbook that you created in Step 1. 5. Click OK. 6. Click Yes in response to Excel s question regarding merging styles that have the same name.

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Where you choose the desired format varies based on the operating system. On the Mac, use the Enable pop-up menu. In Windows, use the Save as Type pop-up menu.

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The first part of this section explains some of the greatest mysteries and unlocks some of the deepest secrets that surround strokes. If that sounds at all boring, take a look at the figures in this chapter. I created most of them by using strokes, not filled paths. You create most effects with strokes by overlaying several strokes on top of each other. By using the Appearance panel s popup menu to add a new stroke, you place an exact duplicate of the original path on top of itself. Changing the weight and color of the top stroke gives the appearance of a path that s a designer, or custom, stroke. You can add strokes on top of or under the original stroke to make the pattern more complex or to add more colors or shapes.

Without adequate agitation, solid particles less dense than the liquid will oat. Also, ne solids such as our or powders may entrap large amounts of air, which reduces the effective density, causing them to oat. Sometimes the solids are dif cult to wet with the liquid and may form large clumps with entrapped air. Below is a brief summary of work reported in the open literature. This is offered as a guide but with the advise that in almost all cases, lab and pilot testing will be required for meaningful scale-up and design. Studies using 10 wt% polyethylene in tap water and others using cork or polypropylene particles in water or corn syrup solutions (Joosten et al., 1977; Hemrajani et al., 1988; Thring, 1990; Siddiqui, 1993) indicate that formation of a controlled vortex is the key to achieving a complete dispersion and suspension of oating solids. The controlled vortex is obtained by using various partial baf es in the vessel rather than no baf es at all. All these studies indicate that dispersion of oating solids requires more energy than for settling solids. The Froude number, NFr , is a predominant correlating parameter in these systems, where liquid surface behavior is so important. Joosten et al. (1977) have developed a correlation that has been used successfully to design a commercial mixing system for suspending oating solids in a 50 m3 vessel. The correlation is D 3.65 l s 0.42 (10-14) NFr = 3.6 10 2 T l where NFr = N2 D gc