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Here, ain and aout are the inlet and outlet concentrations of a reactive component, A, that reacts according to A products. Use the version of eq. (1-6) that contains the residence time function actually measured, W(t) or f(t). Equation (1-6) provides a unique estimate of reaction yields because the rstorder reaction extent depends only on the time that the molecule has spent in the system and not on interactions or mixing with other molecules. Reactions other than rst order give more ambiguous results because the RTD does not measure spatial mixing between molecules that can affect reaction yields.

Each of the parameters expects a number an integer, to be exact value, as shown in Table 10-1. The year parameter can be any full four-digit year, such as 1875 or 2675. You can also pass the Date constructor any integer value from 0 to 99, and ActionScript will interpret it to mean a date from 1900 to 1999. This means that a value of 100 will produce a Date object for the year 100, not 2000; but a value of 99 will result in a Date object for the year 1999, not 99. If you want to work with dates before the year 99, you need to actually

P1: KTU WY022-41

Sorting by a single field isn t always sufficient, particularly in a database where the sort field in several records might have the same value. In such cases, you might want to further organize the records by specifying additional sort fields. As an example, you might have several records for people having the same last name. Sorting only by the Last Name field will leave the first names in whatever order the records were in when you created them. (Can you imagine what a mess a metropolitan phone directory would be if it were sorted only by last name Try finding Jake Johnson in a 20-page listing of Johnsons where there was no secondary

Dividing by 2 and taking the first integral to the right gives the system of normal equations, with l 0, , m. (b) In the case of a polynomial we have

280 Catalysis Looks to the Future, National Research Council Reports National Academy Press, Washington, DC, 1992, p 11 281 F Asinger, Mono-Olefins, Chemistry and Technology, Pergamon Press, Oxford, 1968, 5, p 464 282 A Schriesheim and 1 Kirshenbaum, Chemtech 8, 310 (1978) 283 R H Rosenwald, in Kirk-Othmer Encyclopedia of Chemical Technology, 3rd ed, Vol 2, M Grayson and D Eckroth, eds, Wiley-Interscience, New York, 1978, p 50 284 G Stefanidakis and J E Gwyn, in Encyclopedia of Chemical Processing and Design, Vol 2, J J McKetta and W A Cunningham, eds, Marcel Dekker, New York, 1977, p357 285 D H Putney and O Webb, Jr, Petrol Refiner 38(9), 166 (1959) 286 Hydrocarbon Process 47(9), 164 (1968) 287 Hydrocarbon Process, Int Ed 59(9), 174-176 (1980) 288 L F Albright, Oil Gas J 88(46), 79 (1990) 289 H Lerner and V A Citarella, Hydrocarbon Process.

Undoubtedly the most powerful tool of all is the information shared generously among members of the international developer community. Developers at all levels of expertise from countries on all continents willingly solve problems and exchange knowledge and expertise. Rather than jealously guard trade secrets and nurse competitive advantage, FileMaker developers have a long history of collegiality, where problems are shared and solutions debated in open forums. I encourage you to build your skills and share them with others that you in turn may benefit from the collective expertise of FileMaker developers across the globe.

Figure 5-2: Small pieces of a complicated formula can be selected (in this case, the argument for ISERROR).

K2 = k2, 0 + k2,1z -1 + . . . k2, n( k ) z - n( k2 )