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Since phenanthrene is not hydrogenated, a carbocation stabilized by two phenyl rings is required for reduction. Benzene, naphthalene, and their alkylsubstituted derivatives are not reduced by this reagent, and the CF3COOH + Et3SiH system is not active, either 30 These compounds, however, readily exchange hydrogen with D20-BF3,241 demonstrating that the hydride abstraction step must be ratedetermining. In contrast, a reaction system consisting of H20-BF3, the soluble transitionmetal reagent [ptCI2(MeCNh], and hydrogen gas is active even in the hydrogenation of benzene and naphthalene: 242

Before going into the details of the data manipulations, there are some key ideas in designing customer signatures. These ideas ensure that they work well for analytic purposes, and that they can be generated to be as-of arbitrary points in time.

apply stabilization to previously analyzed clips you add to the Project window, you can apply stabilization manually. This is handy when you need to control which clips receive stabilization and which don t.

Figure 38-1: The HTML settings in the Publish Settings dialog box. If you use the Flash Only template to publish an HTML page and open the HTML code in a text editor, you will see something that looks like the following. The bolded code is responsible for actually adding the Flash movie to the page.

StyleManager.loadStyleDeclarations(...style file...);

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Box 5.1 introduces the four types of fundamental tools (methodological approaches) available to environmental microbiologists: microscopy, cultivation, physiological incubations, and biomarkers. All four of the approaches can be brought to bear on the goal of taking a census of microorganisms present in a liter of lake water, in a gram of soil, and/or in the biosphere at large.

The procedure for editing Find requests in the Edit Saved Finds dialog is comparable to the familiar process used to manage Finds and Find criteria associated with script and button commands, such as Enter Find Mode[ ] and Perform Find[ ]. In all, the saved Find requests feature adds utility and convenience to the user interface of your FileMaker solutions and provides a useful supplement to the functionality that can be provided via the use of FileMaker s scripting capabilities.

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Higher alkenes alkylation with, 239 manufacture of, 49 H2 0-BF3, in ionic hydrogenation, 654 Hoechst process, for manufacture of acetaldehyde, 509 1,3-benzenedisulfonic acid, 585 polyethylene, 772 HOF.CH 3CN, as oxidant, 435, 454, 528 H-Oil process, for hydroprocessing, 59 Homologation, of alkenes, with methane, 253 Homometathesis, 696 Horiuti-Polanyi mechanism, 185, 186,621 Houben-Hoesch synthesis, 417 Houdriforming, 42 Houdry process, 31 H2 PtCI 6-2-propanol, in hydrosilylation, 322 H2 PtCI 6-PtCll-, in heterosubstitution, 596 Huels process for hydrocarboxymethylation, 385 for manufacture of cis,trans,trans-l,5,9-cyclododecatriene, 733 poly(1-butene), 774 for oxidation of cyclododecane, 505 Hydeal process, for hydrodealkylation, 57 Hydration, 284 of acetylene, 290 of alkenes, 285, 288, 336 indirect, 285, 288 of alkynes, 287 of dienes, 286 Hydride abstraction in alkane isomerization, 166 in catalytic cracking, 34, 35 in polymerization, 725, 738 Hydride complexes, in hydrogenolysis, 678 Hydride shift in alkane isomerization, 167 in alkylation, 219 in catalytic cracking, 35 in dimerization of alkenes, 725 in isomerization of aromatics, 173 Hydride transfer in alkane isomerization, 165, 166 in alkylation, 218-220, 223, 224 in carboxylation, 384 Hydroalanation, 321, 345 Hydroalumination, see Hydroalanation Hydroamination, 312, 339 of alkenes, 312, 339, 340 of alkynes, 314, 340 of dienes, 313, 340 Hydroboration, 315, 341

Turbine and hydrofoil impellers operating in the turbulent and transitional regimes rely on entrainment to move uid from the impeller region to the vessel walls and surface. As the viscosity of the uid increases, primary ow generated by the impeller and level of entrainment are reduced until the regions away from the impeller become stagnant. In the transitional regime the dimensionless blend time, N , is inversely proportional to Reynolds number. As the uid s viscosity increases (and Reynolds number decreases) a value is reached where the dimensionless blend time becomes more sensitive to changes in viscosity. At this value of Reynolds number, the decision of whether to use a turbine impeller or to change to an

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