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the center of a spread rather than from the left-hand page), you can move the zero point by clicking and dragging it to a new location. The X and Y values in the Control panel and Transform panel update as you click and drag the zero point so that you can place it precisely. The zero point is document-wide, so it changes for all pages or spreads in the document. To restore the zero point to the upper-left corner of the leftmost page, double-click the intersection of the rulers in the upper-left corner. After the zero point is moved, all the objects on the page display new X and Y values even though they haven t moved. Objects above or to the left of the zero point have negative X and Y values, and the X and Y values of other objects do not relate to their actual position on the page or spread. The effects of changing the zero point can be confusing, especially if you re in a workgroup with other users who may change the zero point and forget to restore it to the upper-left corner. To prevent this problem, you can lock the zero point, making it more difficult for users to change it. To lock the zero point, Control+click or right-click the zero point and choose Lock Zero Point from the contextual menu. Of course, a user determined to change the zero point can simply choose Unlock Zero Point from the contextual menu. But doing so is a conscious act on their part, and the fact that you locked the zero point usually sends the message that you want to keep it that way.



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The effective frequency load (EFL) quanti es how loaded each frequency available in the system is [18]. It is independent of the frequency reuse and of the TRX con guration deployed. It can be calculated as EFL(%) = or EFL(%) = which can be translated to EFL(%) = ErlBH Tot#freq 1 TSL Ave# TRX Frequency load FAR LHW Reff





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13-2.2.1 Pipes. The simplest mixed chemical reactor is a pipe with reactant injectors at one end. The reactants mix as they ow toward the outlet, forming a tubular reactor. There are two measures of mixing in a pipe: (1) the degree of uniformity of the average concentration in the radial direction, and (2) the mean square of the level of concentration uctuations (referred to as segregation) at various locations across the pipe. The perfect reactor analysis assumes that there is no radial distribution of concentration and the reaction occurs with time along a length with no radial effect. This reduces the analysis to a simple differential equation with time or, at constant velocity, with length. This is the ideal plug ow assumption. When there is only a single reactant, radial concentration gradients are small if the velocity pro le is nearly at, as in high Reynolds number turbulent ow. For multiple reactants it takes a nite time for them to achieve radial uniformity at the molecular scale where chemical reactions occur, so the ideal plug ow assumption does not hold and mixing rates must be considered. Pipe reactors can be operated in laminar or turbulent ow. In laminar ow radial diffusivity is molecular only, which is very slow, particularly if the viscosity is high. In turbulent ow the radial uctuating velocity component produces the radial turbulent diffusivity which is much faster than molecular diffusivity. Many devices have been developed to promote fast radial mixing in laminar ow, such as static mixers, which are discussed below and in 7. Besides static mixers, a number of methods exist to promote faster radial mixing in turbulent ow, since even in turbulent ow it takes 50 to 100 pipe diameters to achieve

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RSS_ENTRY_TMPL = <item> <title>%(entry.title)s</title> <link>%(entry.link)s</link> <pubDate>%(entry.modified)s</pubDate> <guid isPermaLink= false >%(entry.id)s</guid> <description>%(entry.content)s</description> </item>

to jump one word to the right or left, or one paragraph up or down. The Home and End keys let you jump to the beginning or end of a line; add or Ctrl to jump to the beginning or end of a story. (A story is text within a text frame or that is linked across several text frames, as described in 18.) Note that if your story begins or ends in a text frame on another page, InDesign brings you to that page.

Calculating the deciles for the lift and chi-square uses the window functions:

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