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One advantage of using indicator variables is that they are easy to change. For instance, changing the limit of 1000 to 500 only requires changing the indicator variable, rather than making multiple changes in several places that might (or might not) be consistent. Indicator variables are only one example of using subqueries to name variables. Throughout the book, there are many other examples. The purpose is to make the queries understandable to humans, relatively easy to modify, and might, with luck, help us remember what a query written six months ago is really doing.

The Outline button creates small sections of paths wherever paths cross and colors the strokes by using the fill of the path they were part of and giving the strokes a weight of 1 point. Outline is useful for spot color trapping because it automatically creates the sections that need to be chosen for overprinting, although the colors are often incorrect. (Trapping is a process whereby colors are printed slightly beyond the edge of an object so that there won t be white gaps between adjacent colored areas when the document is printed on a commercial printing press.) Outline creates smaller path pieces than Divide does; but instead of making each section a closed path, each path maintains its individuality, becoming separate from adjoining paths. The result of outlining is several small stroke pieces. Instead of maintaining the fill color of each piece, each piece is filled with None and stroked with a fill color.

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Regardless of which layer is the active layer, you can select, move, and modify objects on any visible, unlocked layer. You can even select objects on different layers and manipulate them.

achieved at high throughput when the ow is divided into a large number of parallel ow paths High capacity and uniform product treatment are achieved, but only when ow is divided equally to all tubes It is important to recognize that the mixing elements achieve their effect only within the individual tubes treating partial ows With isolated ow paths, there is no radial mixing effect over the entire product stream as with the monotube design This is proved not to be a problem in heating applications where the viscosity decreases as temperature is increased At a moderate pressure drop, a properly designed multitube viscous heat exchanger is self-correcting under conditions of decreasing viscosity Size (number of parallel tubes) can be increased to handle whatever maximum heat load and throughput are required Heat exchanger scale-up is much more dif cult for cases where the viscosity increases during the process.

This is the case in many viscous cooling applications and for polymerization reactions where viscosity can increase by several orders of magnitude The maldistribution effect in multitube designs occurs when one or several of the parallel tubes behave a little differently than the others There are numerous causes for this Maybe there is a maldistribution in the feed stream; or resistance to ow may be minimally different due to slightly different surface roughness or slightly different diameter within tolerance limits; or heat transfer may be slightly different due to minor differences in coolant ow around the tube If for some reason an individual tube cools a little faster than the others, its effective viscosity will increase at a greater rate, causing higher resistance to ow Since the pressure drop must be the same over all parallel tubes, the ow through the offending tube will decrease.

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This results in a longer residence time, an even lower temperature, and still higher viscosity At greatly diminished ow, the tube could eventually reach the temperature of the cooling uid, and if.

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