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Color Settings is accessed from the Edit menu (Figure 12-1) or Ctrl+Shift+K (Windows), +Shift+K (Mac OS). The dialog box is divided into five logical parts: Working Spaces, Color Management Policies, Conversion Options, Advanced Controls, and Description. The settings in each part can be customized and the four parts saved as one custom setting and then selected from the Settings pop-up menu at the top of the dialog box.

near the mounting location. When dynamic loads are considered acceptable static de ections become disturbing motions, similar to those experienced aboard a ship at sea. Such motions are disturbing to the operators of the mixer but can also accelerate damage to gears and bearings and even lead to catastrophic failure of a shaft or support component. To handle dynamic loads, the structure must be stiff in all directions. Two parallel beams like the major ones shown in Figure 21-43 may be stiff along their length. However, without the cross bracing shown in Figure 21-43, the structure is exible in the direction normal to the main beam lengths. End, lateral, and angled bracing strengthen the structure in all directions and a minimum spacing between the beams of 15% of the tank diameter or the width of the mixer drive provides the basis for a stiff support.

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The Hamiltonian and Hamiltonian density have the same dimensions as the Lagrangian and Lagrangian density, respectively, and the action is dimensionless in natural units. From the free field equations (see $2.3), we can then infer the dimensions of various fields. For a spinor field

This calculation is so poorly formed that you could be forgiven for thinking I made it up to illustrate a point. Not so; I copied both the examples in this section directly from a real (albeit poorly designed) solution. As you can see, the latter example requires evaluation of the Sum(Invoices:: BalancePayable) expression a minimum of 4 times and up to a maximum of 11 times, depending on the cumulative amount owing for a given customer record. In this instance, I recast the expression as

(4.3-59)

The bene ts of improved mixing have been known for a long time. Following the introduction of medium consistency mixer technology in the 1980s, a CPPA survey documented chemical savings averaging 10 to 15% (Berry, 1990). Mills that took advantage of the improved mixing technology saw their capital investment returned in as little as three months. The situation is no different in mills today, and signi cant chemical savings can be achieved through improved mixing. However, mixing quality must be measured to know the degree to which it can be improved. The chemical savings potential is readily demonstrated in Figure 20-25. Here, the mixing performance curves for a kraft pulp deligni ed using a D0 (EO) sequence (a chlorine dioxide stage followed by extractive oxidation stage) are given. The curve for perfect mixing (M = 0.0) was determined in the laboratory under ideal mixing conditions. The other curves were calculated with these data assuming a normal distribution of chemical throughout the suspension following mixing. The mixing index is de ned using eq. (20-37). To illustrate the bene ts of improved mixing, assume that an existing mixer achieves a mixing quality of M = 0.40 (which is typical of many installations; see Tables 20-5

Arve Bersvendsen (http://www.virtuelvis.com/archives/145.html) realized that since Opera 7 was the only browser currently supporting Media Queries, they could be used to pass styles exclusively to that browser. Media Queries are, at their heart, a logical statement. Only if the statement evaluates to true are the declared styles rendered. To ensure that all Opera 7 browsers can see a style, use a Media Query that always is true:

After you ve created the required resources locally, they can be referenced directly (for example, in a Web viewer) by dynamically inserting path references as URLs, using a calculation construction such as

Refresh one or more external data source connections View when an external data source connection was last refreshed View the status of refresh operations Cancel a refresh operation

1.5 1.0 0 0.2 0.4 0.6 0.8 1 1.2

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