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The output of an LFSR s0(0), s0(1), . . . may be generated by more than one characteristic polynomial and initial state. Example 8.6 The LFSRs with characteristic polynomials and initial states p1 (z) 1 z z3 z4 , p2 (z) (1 z z3 )(1 z z3 z4 ), s(0) (1, 1, 0, 1) s(0) (1, 1, 0, 1, 1, 0, 1)

Color Palette: When adding colors to objects, you can now specify one of three color palettes to use. (If you are creating cross-platform databases or ones you intend to publish with the Web Companion and believe that some of your visitors will be using either older machines or older Web browser versions, select the Web palette.)

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Bit Depth 1 2 4 Number of Colors 2 4 16 Description Black and white, corresponding to the on or off possible with one bit. Typically, computers with two-bit color depth (usually handhelds or portables) display four shades of gray. The minimum color depth of VGA (Video Graphics Adapter) displays, the most common computer display technology.

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A few years ago, there were a number of programs that would let you make a fair use backup of the video on your commercial DVDs. These programs, while their good intent was shaky both morally and legally, worked fairly well. The most popular company was 321 Studios, which was shut down by the legal hounds of the MPAA. Their DVDXCopy utility (see Figure 10-11) converted the popular DeCSS program into a functional, easy to use, Windows-based application that let you make one-click backups of your DVD collection. The result was a DVD without the CSS encryption used on DVDs to prevent unlawful copying.

1. Choose File Publish Settings. 2. Click the Flash tab. 3. In the drop-down list, click Playback Security. 4. Click OK.

Click the box in the upper-right corner Double-click the panel tab Enter (Return) Shift+ Enter (Return) Tab Shift+Tab Click the label or double-click the current value Highlight field, Highlight field, Highlight field, Shift+ Highlight field, Shift+ Drag the panel tab within another panel Drag the panel tab to the bottom of another panel Drag the panel tab from the current panel

unit volume has to be increased substantially Scale-up at constant Reynolds number is also not feasible since in this case the Pg /V value is reduced by a factor of 104 at the large scale Equal impeller tip speed can be used, although the reduction in the Pg /V value by a factor of 10 also results in lower kL a values Also, in this case there is a 10 fold increase in the circulation time Equal kL a and vvm and equal kL a and vs are also commonly used for scale-up One of the consequences of using the former scale-up criterion rather than the latter is that the power consumption is lower due to the higher super cial gas velocity, and this results in higher circulation times.

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It is important to note that regardless of the choice of scale-up criterion (except scale-up at equal impeller speed or mixing time, both of which are economically unrealistic), there is an increase in the circulation time at the large scale This increase, coupled with high oxygen demands, can cause severe oxygen gradients, and coupled with the addition of concentrated reagents for pH control and nutrient availability, can have a signi cant impact on fermentation yield It is clear from Table 18-1 that different scale-up criteria result in entirely different process conditions at the larger scale It is impossible to maintain similarity of all aspects of the microenvironment at different scales The scale-up criteria are system speci c and it is therefore necessary to select a scale-up basis depending on the transport property most critical to the performance of the bioprocess.

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