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You should get in the habit of immediately naming all components. Every time you create a component, it gets added to the Library. You can double-click the name of this component to rename it, ensuring that you give it a descriptive label that aids both you and your Flex developer later in referring to and using it in your application. Names of components can contain only letters, numbers, and underscores, and need to begin with a letter. In addition, names are case-sensitive. Most Flex developers rely on a system known as camel casing for naming items, whereby multiple-word names are combined into a single word, with the first letter of the name in lowercase and the first letter of each additional word capitalized. For example, a name such as Home Address would be written homeAddress.

Step 4: If you selected the option Embed additional SWF or text files in the previous step, you will now be able to choose those files from the interface shown in the following figure. These files need to be in the same directory as the starter .SWF file of the screensaver or in a subdirectory. Make sure that your Flash actions use relative paths to these files. Click Continue.

To add an expression to the list, click the green + button to invoke the Edit Expression window shown in Figure 24-4. (Compare the Edit Expression window with the very familiar Edit Calculation dialog the similarities are intentional.) Clicking the Monitor button adds the expression to the Data Viewer window.

T+ T-

Acetaldehyde and Acetone The direct palladium-catalyzed oxidation of ethylene to acetaldehyde 507 ,867,921-926 is an important industrial processes The similar oxidation of propylene to acetone,915,927,928 though practiced, is less important,915,929 due to other large-scale processes for the manufacture of acetone (dehydrogenation of 2-propanol, the cumene oxidation process; see Section 954) A single-stage technology (Hoechst process,922,925 for oxidation with oxygen) and a two-stage process (Wacker process,922,925 for oxidation with air) have been developed The homogeneous oxidation of alkenes in aqueous solution to carbonyl compounds by palladium salts results in the concomitant reduction of Pd(II) to metallic palladium In the catalytic process a suitable oxidant, usually CuCl 2 is used to regenerate Pd(II), and CU2Cl2 thus formed is reoxidized with oxygen (see Section 924) In the single-stage operation the alkene and oxygen are fed into the aqueous solution of PdCl 2 containing a large excess of CuCI 2.

Proposition 8.8 asserts that the matrix S(7t, 7t N 2 1) has an inverse and Gaussian elimination determines the taps (c1, c2, . . . , cN21, cN). Cribbing stream enciphered ASCII plaintext tests a value of N and a position t in the plaintext with two possible outcomes: 1. If N is correct and the crib starts as the tth character in the plaintext, then (a) The matrix S(t, t N 2 1) is invertible determining taps (c1, c2, . . . , cN21, cN) and (b) Backward and forward recursion will determine the entire key stream and plaintext. 2. If N is incorrect or if the crib does not start as the tth character in the plaintext, then (a) The matrix S(t, t N 2 1) may fail to be invertible, or (b) The matrix (t, t N 2 1) may be invertible determining taps (c1, c2, . . . , cN21, cN), but backward and forward recursion will determine a large percentage of nonprintable plaintext ASCII characters. The cribbing strategy is to test if S(7t, 7t N 2 1) has an inverse for some interval of N, t-values Test [widths] for N : N1 to N2; Test [positions] for t : t1 to t2; If S(7t, 7t N 2 1) has an inverse If YES, compute c and use the forward or backward recursions to compute a segment of the key stream and plaintext s(7(t N k)); s(7(t N k 1)); . . . ; s(7(t N 1)) | {z }

Oxidation of the alkene to the carbonyl compound and regeneration of the catalyst system occur in the same reactor (120-130 C, 3 atm) This process requires the use of highpurity ethylene (997%) and oxygen (99%) In the two-stage process the alkene is reacted with the catalyst system (100110 C, 10 atm) The reduced catalyst solution containing CU2Cl2 is reoxidized with air in a second reactor under the same conditions In both cases about 95% oxo yield is achieved at 95-99% alkene conversion Because of the explosion hazard of mixing ethylene or propylene with pure oxygen, most commercial operations favor the less hazardous two-stage process Vinyl Acetate.