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Inert carbon

Hydrocarbons Inert Carbon Polymer Caustic Surfactant gases dioxide polymer... [Pg.356]

In the previous Sections (2.1-2.3) we summarized the experimental and computational results concerning on the size-dependent electronic structure of nanoparticles supported by more or less inert (carbon or oxide) and strongly interacting (metallic) substrates. In the following sections the (usually qualitative) models will be discussed in detail, which were developed to interpret the observed data. The emphasis will be placed on systems prepared on inert supports, since - as it was described in Section 2.3 - the behavior of metal adatoms or adlayers on metallic substrates can be understood in terms of charge transfer processes. [Pg.88]

Although the FTS is considered a carbon in-sensitive reaction,30 deactivation of the cobalt active phase by carbon deposition during FTS has been widely postulated.31-38 This mechanism, however, is hard to prove during realistic synthesis conditions due to the presence of heavy hydrocarbon wax product and the potential spillover and buildup of inert carbon on the catalyst support. Also, studies on supported cobalt catalysts have been conducted that suggest deactivation by pore plugging of narrow catalyst pores by the heavy (> 40) wax product.39,40 Very often, regeneration treatments that remove these carbonaceous phases from the catalyst result in reactivation of the catalyst.32 Many of the companies with experience in cobalt-based FTS research report that these catalysts are negatively influenced by carbon (Table 4.1). [Pg.52]

H2/CO = 2 small amounts of inert carbon species on the cobalt active phase regeneration required to maintain activity ... [Pg.53]

The cyclic voltammetry procedure reported by Kohen and others (2000) evaluates the overall reducing power of low-molecular-weight antioxidants in a biological fluid or tissue homogenate. The electrochemical oxidation of a certain compound on an inert carbon glassy electrode is accompanied by the appearance of the current at a certain potential. While the potential at which a cyclic voltammetry peak appears is determined... [Pg.291]

The reaction of (TPP)Rh with terminal alkenes or alkynes is of special interest due to the cleavage of the carbon-carbon bond adjacent to either the alkene or the alkyne functionality and results in the ultimate formation of (TPP)Rh(R). This overall reaction implies activation of a relatively inert carbon-carbon bond, especially for the case of the terminal alkene. However, the ultimate formation of (P)Rh(R) is not surprising if one considers the relative stability of the rhodium carbon bond in this species(17). [Pg.457]

The reactor vents are due to the non-condensables in both the chlorine and ethylene feeds. In the case of chlorine, the non-condensables are largely the oxygen and inerts (carbon dioxide and nitrogen) as produced from the electrolysers. In the case of ethylene, the non-condensables are largely ethane, which is unreactive. The vent is also saturated with EDC vapour at the vent condenser temperature. [Pg.283]

To recover aluminum metal, AI2O3 is first converted to AICI3. Then an electrolysis of molten AICI3 is performed using inert carbon electrodes. [Pg.586]

The neutron bursts take place in helium burning shells surrounding the inert carbon-oxygen core. The neutrons released here are grafted onto iron and its kin. [Pg.167]

Polyhydroxyalkanoates (PHAs) are biological polyesters that are produced by a wide variety of bacteria as osmotically inert carbon- and energy-storage compounds that accumulate in the form of granules (see Fig. 1). [Pg.24]

The ordinary dry cell (Leclanche cell) is a primary cell that is used in flashlights. In this cell, oxidation occurs at a zinc anode, and reduction at an inert carbon +" cathode (graphite). The space between the cell is filled with a moist paste of Mn02, ZnCl2 and NH CI. The half-reaction at the anode is as follows ... [Pg.160]

Boron-doped chemical-vapor-deposited diamond is an exceptionally inert carbon electrode with a very wide potential window and very low voltammetric background current. [A. E. Fischer, Y. Show, and G. M. Swain, Electrochemical Performance of Diamond Thin-Film Electrodes from Different Commercial Sources, Anal. Chem. 2004, 76, 2553.]... [Pg.675]

The concept of mechanical fixation of metal on carbon makes catalytic applications at high temperatures possible. These applications require medium-sized active particles because particles below 2nm in size are not sufficiently stabilised by mechanical fixation and do not survive the high temperature treatment required by the selective etching. Typical reactions which have been studied in detail are ammonia synthesis [195, 201-203] and CO hydrogenation [204-207]. The idea that the inert carbon support could remove all problems associated with the reactivity of products with acid sites on oxides was tested, with the hope that a thermally wellconducting catalyst lacking strong-metal support interactions, as on oxide supports, would result. [Pg.142]

Camacho cell — This was a - chromic acid battery with zinc anodes, and a construction that the chromic acid solutions flowed through the cathode compartment housing the inert carbon electrodes. See also - Daniell cell, - zinc, - Zn2+/Zn electrodes, - Zn2+/Zn(Hg) electrodes, - zinc-air batteries (cell), and - Leclanche cell. Ref [i] Hauck WP (1883) Die Galvanischen Batterien, Accumulatoren und Thermosaulen, 2nd edn. Hartleben s Verlag Wien... [Pg.67]

Fig. 3 SEM micrograph of a nickel film deposited on a polished inert (carbon) substrate, in conditions A2. The film has been scratched from the substrate with a pliers. Fig. 3 SEM micrograph of a nickel film deposited on a polished inert (carbon) substrate, in conditions A2. The film has been scratched from the substrate with a pliers.
High modulus C-fibers from special pitch 1st step polymerization > 300 C to mcsophase pitch 2nd step melt spinning 3rd step oxidative crosslinking 4th step inert carbonization at 1500 to 3000"C... [Pg.382]

Some divalent ions, such as Mg > Co and Mn A are activators of the enzyme, and is a constituent metal ion. The correct ratio of Mg VZn ions is necessary to avoid displacement of Mg and to obtain optimal activity. Phosphate, borate, oxalate, and cyanide ions are inhibitors of ALP activity. Variations in and substrate concentrations change the pH optimum. The type of buffer present (except at low concentrations) affects the rate of enzyme activity. Buffers can be classified as inert (carbonate and barbital), inhibiting (glycine and propylamine), or activating (2-amino-2 methyl-l-propanol [AMP], tris (hydroxymethyl) aminomethane [TRIS], and diethanolamine [DBA]). [Pg.608]

The amine section absorbs most of the hydrogen sulfide from the gas while coabsorbing as little carbon dioxide as possible. These acid gases are recycled to the inlet of the Claus unit and become part of its feed. Because the solvent selects hydrogen sulfide and rejects most of the carbon dioxide, the size of the Claus SRU is increased by only 5-6% because of recycling inert carbon dioxide. [Pg.119]

Figure 3 illustrates different relations of Foxygen to Fcarbon, which depend on stoichiometry, and kinetics of reaction. The normal calc-silicate decarbonation trend applies if all minerals in the rock are fully equilibrated during a reaction such as 4 or 5, in which case all carbon in the rock is liberated as CO2 (Fcarbon 0), while only 40% of the oxygen is released (Foxygen 0.6). However, if the rock has (for example) 50% excess silicates that are not involved in the reaction, but which still equilibrate isotopically, then F xy 0.8 as Fcarbon 0.0 along the 50% inert oxygen trend and the amount of Or°0 depletion will be smaller. Likewise, if 50% of a rock s carbon does not participate due to stoichiometric excess, a 50% inert carbon trend will be followed and the depletion of will also be less. In practice any trend is possible from -100%... [Pg.422]

Figure 3. Values of F(carbon) vs. F(oxygen) along various reaction paths. F is the mole fraction of O or C remaining in the rock after reaction. Most marbles, if equihbrated, will follow a F-F path intermediate between 50% inert oxygen and 50% inert carbon (from Valley 1986). Figure 3. Values of F(carbon) vs. F(oxygen) along various reaction paths. F is the mole fraction of O or C remaining in the rock after reaction. Most marbles, if equihbrated, will follow a F-F path intermediate between 50% inert oxygen and 50% inert carbon (from Valley 1986).
Czimczik, C., Schmidt, M. W. I., Glaser B., Schulze E.-D. (2000). The inert carbon pool in boreal soils—char black carbon stocks in pristine Siberian Scots pine forest. Proceedings of the Boreal Forest Conference. Edmonton, May 2000. [Pg.14]

Many earlier geotechnical studies exist of the electroosmotic effect in soils and clays with an emphasis on dewatering in this chapter we limit the discussion to the more recent activities aimed at decontamination of pollutants. Most laboratory tests have used a onedimensional geometry and inert carbon electrodes. [Pg.632]


See other pages where Inert carbon is mentioned: [Pg.40]    [Pg.203]    [Pg.279]    [Pg.551]    [Pg.551]    [Pg.540]    [Pg.133]    [Pg.692]    [Pg.24]    [Pg.25]    [Pg.83]    [Pg.264]    [Pg.284]    [Pg.14]    [Pg.257]    [Pg.310]    [Pg.274]    [Pg.205]    [Pg.382]    [Pg.289]    [Pg.711]    [Pg.65]    [Pg.60]    [Pg.108]    [Pg.257]    [Pg.170]    [Pg.175]   
See also in sourсe #XX -- [ Pg.160 ]




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