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14 Calculations and Computations
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Starting with the step furthest from the building, Push/Pull upward and enter the value 6 . This will create a step with a 6 riser (Fig. 6-20). Hover over the next step with Push/Pull and double-click. Push/Pull will automatically repeat the last command entered. The two steps are now the same height. Double-click again. This will Push/Pull the face another 6 above the first step (Fig. 6-21). Repeat this step for the other stair surfaces until they are all 6 above the adjacent steps, ascending toward the building.
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1: Introducing Dreamweaver MX 2004 . . . . . . . . . . . . . . . . . . . . . . . . . . 3 2: A Dreamweaver Workflow Example . . . . . . . . . . . . . . . . . . . . . . . . . 35 3: Touring Dreamweaver . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 57 4: Setting Your Preferences . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 137 5: Setting Up Sites and Servers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 177
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uV (E) Cd43 (25)(y) Cd43 (23) (a),
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Nonsterile Optional (alternative to mitomycin C treatment): gamma or X-ray irradiator Low-speed refrigerated centrifuge Procedure (a) Seed NIH 3T3 broblasts in 25-cm2 or 75-cm2 tissue culture asks in DMEM10FB/GASP). (b) When the cells just reach con uence, add MMC (5 g/mL) for 2 h at 37 C. (c) Trypsinize and plate the cells at a density of 2 104 cells/cm2 in 3.5-cm dishes or six-well plates. (d) As an alternative to MMC, con uent cultures of 3T3 cells may be irradiated with 60 Gy, using 60 Co or an X-ray source. The cells are amitotic but still living and can be used as a feeder layer.
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5. When your iMac connects, the Screen Sharing window showing your office Mac
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You can use Flash Builder 4 s new event handler generation capabilities to create the handler function automatically. When you auto-complete the result event in the HTTPService MXML declaration, Flash Builder prompts you to generate the result handler. It then creates the event handler function with the method signature described in the preceding step. n
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between Ho= -10.1 and _14.1.350 For both systems the best alkylation conditions were those at an acid strength of about Ho = - 10.7, giving calculated research octane numbers of 89.1 (triflic acid-TFA) and 91.4 (triflic acid-water). Isobutane-isobutylene alkylation was studied in liquid CO 2 with various acids (anhydrous HF, PPHF, conc. H2S04, triflic acid) in the temperature range of 0_50 c. 35J For HF and triflic acid, higher optimum research octane numbers were obtained in CO 2 than in the neat acids (95.6 for HF and 88.0 for triflic acid). Moreover, these reactions required less acid catalyst and afforded increased selectivities to trimethylpentanes. A novel liquid acid catalyst composed of a heteropoly acid (phophotungstic acid or silicotungstic acid) and acetic acid was used in the alkylation isobutane with butenes 52 A viscous, oily phase separating during the early stages of the reaction showed catalytic performance comparable to that of sulfuric acid. Concentrated sulfuric acid and hydrogen fluoride are still mainly used in commercial isoalkane-alkene alkylation processes 53 Because of the difficulties associated with these liquid acid catalysts (see Section 5.1.1), considerable research efforts are still devoted to find suitable solid acid catalysts for replacement.354-356 Various large-pore zeolites, mainly X and Y, and more recently zeolite Beta were studied in this reaction. Considering the reaction scheme [(Eqs (5.3)-(5.5) and Scheme 5.1)] it is obvious that the large-pore zeolitic structure is a prerequisite, since many of the reaction steps involve bimolecular bulky intermediates. In addition, the fast and easy desorption of highly branched bulky products, such as trimethylpentanes, also requires sufficient and adequate pore size. Experiments showed that even with large-pore zeolite Y, alkylation is severely diffusion limited under liquid-phase conditions 57 Brpnsted acid sites serve as the active sites for the alkylation reaction. Higher acid site density, obviously, increases the reaction rate, providing higher concentration of carbocations and, hence, hydride transfer necessary for the desorption of the alkylated carbocationic intermediates becomes faster. Since alkane formation is a more demanding reaction requiring two adjacent acid sites, the alkane: alkene ratio was found to increase with increasing acid site density 55 The ratio of trimethylpentanes to dimetylpentanes also increases with increasing acid site density. This is due to the fact that the formation of the desired highly branched trimethylpentanes includes two hydride transfer steps whereas that of dimetylpentanes has only one. The major problem of the application of zeolites in alkane-alkene alkylation is their rapid deactivation by carbonaceous deposits. These either strongly adsorb on acidic sites or block the pores preventing the access of the reactants to the active sites. A further problem is that in addition to activity loss, the selectivity of the zeolite-catalyzed alkylation also decreases severely. Specifically, alkene formation through oligomerization becomes the dominant reaction. This is explained by decreasing ability of the aging catalyst to promote intermolecular hydride transfer. These are the main reasons why the developments of several commercial processes reached only the pilot plant stage 56 New observations with Y zeolites reconfirm the problems found in earlier studies 58,359
541. Natura! Gas Conversion II, Studies in Surface Science and Catalysis, Vol. 81, H. E. Curry-Hyde and R. E Howe, eds., Elsevier, Amsterdam, 1994, pp. 125-283. 542. Natura! Gas Conversion IV, Studies in Surface Science and Catalysis, Vol. 107, M. dePontes, R. L. Espinoza, C. P. Nicolaides, J. H. Scholtz, and M. S. Scurrell, eds., Elsevier, Amsterdam, 1997, pp. 291-394. 543. S. Pak, P. Qui, and J. H. Lunsford, J. Cata!. 179,222 (1998). 544. J. 1. Kong, J. S. Jung, J. G. Choi, and S. H. Lee, App!. Cata!., A 204, 241 (2000).
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The Hand tool (shortcut H) lets you scoot pages around to view a different portion of a page or another page entirely. The Hand tool is an entirely visual method of scrolling, allowing you to see the page contents at all times. To use the Hand tool, click and drag in any direction. You can access the Hand tool temporarily without actually switching tools by pressing Option+spacebar or Alt+spacebar. (See 2.)
The following code defines an MXML component designed to collect login information, and it might be saved as a file named LoginWindow.mxml:
Note that the first-order real image moves outward by almost 75 mm, and the first-order virtual image moves inward by only 60 mm. The relevant cascaded mathematical expression is now
< php // File Backup $dirs = array( /var/www/vhosts/example.org/myfiles ); $backupDir = /var/www/vhosts/example.org/backups ; $date = date( m-d-y ); foreach($dirs as $dir) { $dir = preg_replace( /\/$/ , , $dir); $archiveName = preg_replace( /^(.*)\/.* / , , $dir); $tgzName = {$archiveName}-{$date}.tgz ; $tgzFile = {$backupDir}/{$tgzName} ; $backupCmd = tar czf {$tgzFile} {$archiveName} ; $result = system($backupCmd . 2>&1 ); print Command: . $backupCmd . <br /> ;
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Wireless network provides packet data transfer capabilities that are used by transport and application protocols for exchange of information. At transport level, there are several protocols that can be used, depending on the service. For error-free message delivery, TCP is
Building customer signatures is about bringing data together from disparate data sources. Figure 12-4 shows conceptually what needs to be done. Some data is already in the right format, and at the right granularity. This data merely needs to be copied. Some fields are keys into other tables, where information can be looked up. Other data is in the format of regular time series that can be pivoted. Irregular time series, such as transactions, need to be summarized. This section describes these operations in the context of building customer signatures.
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