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Masks based on the brightness values of an image are very useful for tonal corrections. They can limit the corrections to the highlights or the shadows. Furthermore, they can be created from the brightness values belonging to the composite channel or an individual channel. To give one example of their use, you can limit a Curves adjustment to just the highlights by taking the following steps: 1. Ctrl-click (Windows), -click (Mac OS) on the composite channel to load the luminosity mask, or Ctrl+Alt+Tilde (Windows), +Opt+Tilde (Mac OS). The Tilde key is the one marked with a ~ sign. To be precise, you are using the grave accent ` key, but tilde is commonly used to refer to the key. 2. Choose Layer New Adjustment Layer Curves, or click the Create New Fill or Adjustment icon in the Layers palette and then choose Curves. Photoshop creates an adjustment layer and an accompanying mask thumbnail and includes a grayscale image of the composite channel in the mask. 3. In the Curves dialog box, adjust the curve and click the OK button to exit. When you make any adjustments in the Curves dialog box, the changes made to the highlights show in accordance with the density of the mask, but the changes applied to the shadows are masked. To affect the shadows, press Ctrl+Shift+I (Windows), +Shift+I (Mac OS) after step 1 to invert the mask, or you can click the mask thumbnail at any time and invoke the preceding shortcut. After becoming aware of this technique, you can quite easily find other uses for it. For example, you can use it to confine the effect of layer blends, Hue/Saturation adjustments, global sharpening, colorized layers, or sepia-like effects.

To simplify this code a bit, all of the business of sending out instant messages is handled by the sendIMwithTemplate() function, the implementation of which is offered in Listing 4-13. Go ahead and define this function next.

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If you re working on a simple, one-page publication, such as a business card, a poster, or an ad, you ll probably use the Character panel to format the text elements. However, if you re producing a multipage publication a newsletter, magazine, catalog, or newspaper, for example you should take advantage of styles: both paragraph styles to set both character and paragraph formatting in one place to apply to entire paragraphs (see 21) and character styles to apply character formatting to apply to text selections within paragraphs. Using styles saves you time and makes your job a whole lot easier. Even if you do use styles for a particular publication, you ll probably also do some local formatting. For example, you would probably use the Character panel to format the type on the opening spread of a feature magazine article and then use styles to quickly format the remainder of the article.

Although the subject of this chapter is general mixing in the ne chemical and pharmaceutical industries, much of the focus is on reactions and their associated operations, since they present a wide range of mixing challenges In addition, multipurpose plants are designed with a series of vessels that are used for reactions as well as extraction, distillation, crystallization, and so on, and in some applications, these operations may all be performed in the same vessel A major challenge for mixing in stirred vessels for the pharmaceutical and ne chemical industries is, therefore, the variety of functions that must be performed often simultaneously, such as heat transfer, reaction, mixing and so on To make matters worse for the development and design engineer, mixing that may be good for one aspect of an operation may be deleterious to another A central question is: Can one set of operating conditions [eg.

You should exercise extreme care when working directly with server files. In most situations, it is strongly advised that you work with Dreamweaver s defined site structure, particularly if other designers are working on the site. Without some sort of revision control, such as Dreamweaver s Check In/Check Out feature, it is entirely possible that work can be inadvertently lost.

, impeller(s), rotational speed(s), power input, baf es, internals, control systems] cover all requirements Consider a reacting solid liquid gas system with mass transfer occurring among the phases The operations involved may include chemical reaction and mass transfer for gas absorption The solids are reagents that are dissolving as the reaction proceeds The operations are solids suspension and solids dissolution The products or by-products, whose physical and purity characteristics are important in downstream processing, are crystallizing out of solution The operations are mass transfer and crystal growth Overall, the system is highly complex Furthermore, it should be apparent that no single set of design correlations can cover this range of simultaneous interactions, even though it might be possible to design adequate systems for each of the operations.

One simple solution to the problem would be to specify a mixing system with enough energy to exceed the requirements for the most dif cult individual operation Often, this is done A pilot plant version of the process may even run satisfactorily using this design strategy However, for scale-up to the manufacturing plant, this strategy may give detrimental results due to overmixing eg, overmixing with regard to crystallization and possible production of excessive nes, emulsions, or intractable foam from vapor-phase incorporation In some cases, it may not be possible to accomplish the most dif cult individual operation on the scale required by the manufacturing facility It may then be necessary to use a specialty design such as a continuous in-line device or other special mixing system.

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