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When you ve added beat markers to the audio in a project, you can synchronize video clips, titles, and other elements (such as cutaways) with the beat markers. To synchronize a video clip, click and drag it from the Event browser to the Project window so that it overlaps a beat marker. iMovie automatically adjusts the length of the clip so that it runs from that beat marker to the next beat marker. You can do the same thing with a still image by clicking and dragging it from the Photos browser to the Project window so that it overlaps a beat marker. To synchronize a title, cutaway, or other element that appears above the main line of video clips, click and drag it to align its beginning with a beat marker. The item then starts playing at the beat marker. You can also use the Precision Editor to synchronize a title, cutaway, or other element with a beat marker like this:

Set Variable [$start; Value:Get(CurrentTimeStamp)] Loop Pause/Resume Script [Duration (seconds): .1] Set Variable [$html; Value:GetLayoutObjectAttribute( YourViewer ; content )] Set Variable [$elapsed; Value:Get(CurrentTimeStamp) - $start] Exit Loop If [PatternCount($html; </body> ) or $elapsed > 9)] End Loop If [PatternCount($html; </body> ) < 1] Show Custom Dialog [ Timeout Error: Remote site not responding. ] Else # $html has been retrieved for processing: # etc... End If

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You can preview the results of your detail page in Live Data view, but be sure to set up the Live Data settings option first. Choose View Live Data Settings to begin. When the Live Data Settings dialog box is open, enter the URL parameter name in the Name column and the value you d like to test in the Value column. Make sure the Method option is set to Get, and click OK. Your preview should now include the specified record, just as if the user had chosen it.

In addition, you can view a line s values and in the case of variables, directly edit them by double-clicking the line in the Current panel. FileMaker displays the value in its entirety in a scrollable list in the Current Value dialog, as shown in Figure 18.6. The Current Value dialog is resizable, so you can use it to display long values without truncation. Moreover, you can select values in the Current Value dialog and copy them to the clipboard. However, you can use the other enabled Edit menu commands (Paste Cut and Clear) only to perform actions on variable values. Where referenced fields have repetitions, the repetitions containing a value are loaded into the Data Viewer s Current panel. Repetitions (for either fields or variables) are shown in the Data Viewer using array notation, such as YourField[3] for the third repetition of YourField.

5. Derive Eq. (8.5-1) for the phase shift of electromagnetic radiation passing through a plasma (hint: assume the phase shift is small).

Although InDesign has no default shortcuts for them, you can create keyboard shortcuts for the alignment and distribution buttons, as explained in 3. n

3.5 x 10

No exact method exists to assure successful scale-up of strongly coalescing systems. The following considerations are offered. Does the process require coalescing or noncoalescing conditions Extractions require coalescence; suspension and emulsion polymerization processes do not. Few industrial systems are rapidly coalescing. Impurities, salts, and residues often ensure slow coalescence. Coalescence rates can be characterized using either the static or dynamic method described in Section 12-3.1.5 and Table 12-3. Make the more viscous phase continuous if coalescence is to be minimized. Consider adding a thickener to the continuous phase. Suspending aids, such as polymeric suspending agents, detergents, or ne solids, reduce or stop coalescence. A static mixer in a recirculation loop can complement conventional agitation in the vessel. The use of multiple and larger diameter impellers can increase the effective dispersion zone. CFD can be used to examine ow eld details for both the small scale and the proposed larger scale vessels, and to map out regions of constant energy dissipation rate. The dispersion volume can be approximated as the region in which local / avg 3.0. Similarly, the coalescence region is where local / avg 0.1. The probability of success upon scale-up will improve if the volume ratio of the dispersion to coalescence regions is scale independent.

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