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Metal—atom reactor to form

The reaction of metals with energetic hydrogen or deuterium ions is important in nuclear reactors. Ion beams may be generated thermally and allowed to interact with the metal, and the reaction products then may be examined by matrix-isolation techniques. Alternatively, metal atoms are sputtered from a cathodic surface by a low-energy plasma. If or at low P is added to the discharge, then molecular species are formed by the interaction with the sputtered metal atoms. Applied to Cu this technique leads to the identification of CuH and CuD in Ar matrices by their IR spectra. The reacting species are believed to be atomic Cu and H or D formed in the hollow-cathode discharge . [Pg.315]

Cadmium slurries, formed from codeposition of Cd vapor with a solvent at 77 K followed by warming to RT, are sufficiently reactive toward RI in hexane, toluene, THF, dioxane or diglyme. Reactions do not proceed well with RBr e.g., only a 10% yield of propylcadmiums is obtained on refluxing in diglyme overnight. The presence of KI increases the reactivity of the slurries. Ethyl iodide reacts at — 196°C with a Cd slurry, obtained from simultaneous evaporation of PhMe and Cd in a metal-atom reactor" the yield of nonvolatile EtCdl is 55 %. [Pg.326]

Metals are widely u.sed in catalysis. In some specific cases they are applied in the form of gauzes, but usually a higher dispersion (even up to 90%) is aimed for. A major reason for this is the price of the metals (very often noble metals are used), in combination with an optimized use of the reactor volume. The ratio of number of surface atoms (ns) to the total number of atoms (nr) is called the dispersion , also known as D ... [Pg.66]

The reaction of metal atoms with 1,5-cyclooctadiene (1,5-COD) offer special scope for forming new naked metal systems [Wilke (142)] i.e., complexes in which the ligands are readily displaced. The desire to explore these reactions was the impetus to developing the rotary solution reactor (81) which facilitates the reaction of metal atoms with slightly volatile or involatile ligands and, most important, aids the isolation of thermally unstable compounds (Tdec -60°C) in a pure state. [Pg.66]

Another factor to be considered is the time required to fabricate additional liners if the initial supply is depleted. Recently, General Atomics claimed it was able to fabricate 20-mil thick liners of the required diameter for the reactor. General Atomics plans to float a precious-metal liner in a cylindrical Hastelloy pressure vessel and use cooled elastomeric O-rings that have performed satisfactorily on other SCWO systems to form the SCWO reactor. The annular space between the liner and the vessel wall will be monitored for leaks to indicate when change-out of the liner is required. No decision has been made yet on whether to use platinum or Pt-20%Ir. Because they have markedly different mechanical properties, these two liner materials may require significantly different fabrication methods. Platinum is relatively weak and very ductile Pt-20%Ir is less ductile but 10 times stronger. Final selection of the liner material for use at the NECDF was scheduled for early 2000. Fabrication... [Pg.31]

Ultrasonic nebulizers have also been employed in continuous flow systems as interfaces between sample preparation steps in the analytical process and detection by virtue of their suitability for operating in a continuous mode. Thus, preconcentration devices have commonly been coupled to atomic spectrometers in order to increase the sensitivity of some analytical methods. An enhancement factor of 100 (10 due to USNn and 10 due to preconcentration) was obtained in the determination of platinum in water using a column packed with polyurethane foam loaded with thiocyanate to form a platinum-thiocyanate complex [51]. An enhancement factor of 216 (12 with USNn and 18 with preconcentration) was obtained in the determination of low cadmium concentrations in wine by sorption of metallic complexes with pyridylazo reagents on the inner walls of a PTFE knotted reactor [52]. One special example is the sequential determination of As(lll) and As(V) in water by coupling a preconcentration system to an ICP-AES instrument equipped with a USN. For this purpose, two columns packed with two different resins selective for each arsenic species were connected via a 16-port valve in order to concentrate them for their subsequent sequential elution to the spectrometer [53]. [Pg.262]

In order to produce supported samples for STM or FEM study, clusters formed on the centerline of the condensation reactor are extracted through a 1 mm diameter capillary into a vacuum chamber typically kept at 10-5 Torr. The resulting supersonic free jet flow is collimated to form a molecular beam of metal clusters, uncondensed metal atoms and inert gas atoms. [Pg.331]

For many of the metallic constituents, the product form in the SCWO liquid effluent is dependent to some degree on pH. As the liquid effluent is near ambient temperature, general chemistry rules may be applied. Acidic conditions can lead to higher dissolved levels of certain metals. A common example is provided by nickel, which forms nickel oxide in the SCWO reactor due to feed oxidation or corrosion. When excess hydrochloric or sulfuric acid is present in the SCWO effluent, some of the nickel oxide dissolves to yield dissolved nickel. Many of the entries in Table 14 have not been reported in the literature, but are based on unpublished observations by MODAR and General Atomics. [Pg.437]

Some 5 gm of supported catalyst were used, which exposed some 10 metal atoms to the gas phase (measured by in situ chemisorption), on which an amount of C as varying between 1 and 8 x 10 atoms was deposited. The catalyst was contacted with a batch of some 2 x 10 ° COand6 x 10 ° H2 molecules, and the synthesis reaction was allowed lo proceed until some 1 X 10 hydrocarbon molecules had been formed. With mass spectrometry it was then verified whether these hydrocarbon molecules has been formed from the C j or from the CO,3 5, reservoir. A reactor with a minimized holdup of some 10 ml was used, 4 ml of it being catalyst pore volume. The reactant pressure initially exceeded 1 bar, while the number of reactant molecules was of the same order as the number of predeposited C as atoms. [Pg.203]


See other pages where Metal—atom reactor to form is mentioned: [Pg.480]    [Pg.332]    [Pg.70]    [Pg.79]    [Pg.26]    [Pg.33]    [Pg.221]    [Pg.157]    [Pg.143]    [Pg.430]    [Pg.179]    [Pg.231]    [Pg.404]    [Pg.1008]    [Pg.159]    [Pg.69]    [Pg.109]    [Pg.80]    [Pg.453]    [Pg.245]    [Pg.243]    [Pg.248]    [Pg.5930]    [Pg.176]    [Pg.143]    [Pg.257]    [Pg.294]    [Pg.155]    [Pg.359]    [Pg.109]    [Pg.1008]    [Pg.344]    [Pg.1008]    [Pg.173]   


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