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Metallic area

In particular, emphasis will be placed on the use of chemisorption to measure the metal dispersion, metal area, or particle size of catalytically active metals supported on nonreducible oxides such as the refractory oxides, silica, alumina, silica-alumina, and zeolites. In contrast to physical adsorption, there are no complete books devoted to this aspect of catalyst characterization however, there is a chapter in Anderson that discusses the subject. [Pg.740]

Table 10-7 shows suggested tie rod count and diameter for various sizes of heat exchangers, as recommended by TEMA . Other combinations of tie rod number and diameter with equivalent metal area are permissible however, no fewer than four tie rods, and no diameter less than /g-in., should be used. Any baffle segment requires a minimum of three points of support. [Pg.31]

Overload resulting from severe impact kinking, dantage, localized wear, weakening of one or more strands, or rust-bound condition and [OSS of. elasticify. Loss of metallic area due id broken wires caused by severe bending. [Pg.614]

System Metal Area which Is Predominantly Anodic ... [Pg.1273]

Metal area in contact with the lower concentration... [Pg.153]

High-voltage coating-testing equipment When cathodic protection is applied to a structure which has a protective coating, the current required is proportional to the bare metal area on the structure. Thus whenever a protective coating is applied it should be of good quality, with very few failures or pin holes in it, so that the cathodic-protection system may be economic. [Pg.255]

For a complete panel replacement, the refinisher starts with a panel preprimed in the appropriate stoving primer. For spot repairs or larger repairs without replacement of metal, there will be areas which have to be rubbed through to clean metal. Any indentations then have to be filled with a stopper or spray filler, probably based on unsaturated polyester resins and styrene, with cure initiated by mixing in an organic peroxide. After sanding, remaining bare metal areas are sprayed with a two-pack etch primer. [Pg.627]

It is at the anode that oxidation takes place, with the anodic metal suffering a loss of negatively charged electrons. The resulting positively charged metal ions dissolve in the water electrolyte and metal wastage occurs. In the corrosion cell, the metal or metal area having the lowest electrical potential becomes the anode. [Pg.149]

Each metal or metal area will develop an electrode with a measurable electrical potential. This potential can be referenced to that of a standard hydrogen electrode, which by convention is set at zero. Thus, all metals have either a higher or lower potential compared to hydrogen, and a comparative list of metals can be produced indicating their relative nobility. This list is the galvanic or electrochemical series and measured as an electromotive force (EMF). [Pg.150]

Many late transition metals such as Pd, Pt, Ru, Rh, and Ir can be used as catalysts for steam reforming, but nickel-based catalysts are, economically, the most feasible. More reactive metals such as iron and cobalt are in principle active but they oxidize easily under process conditions. Ruthenium, rhodium and other noble metals are more active than nickel, but are less attractive due to their costs. A typical catalyst consists of relatively large Ni particles dispersed on an AI2O3 or an AlMg04 spinel. The active metal area is relatively low, of the order of only a few m g . ... [Pg.302]

How can the active metal area of a supported catalyst be measured and distinguished from the total surface area ... [Pg.407]

The Ru metal area was determined by volumetric H2 chemisorption in the quartz U-tube of an Autosorb 1-C set-up (Quantachrome) following the procedure described in ref. [16]. Prior to chemisorption, the catalysts were activated by passing 80 Nml/min high-purity synthesis gas (Pnj / Phj -1/3) from a connected feed system through the U-tube and heating to 673 K for alkali-promoted catalysts or to 773 K for alkali-free catalysts with a heating rate of 1 K/min. The BET area was measured by static N2 physisorption in the same set-up. [Pg.318]

Catalyst H2 monolayer / /rmol H2/g Metal area / m /g Dispersion /% Particle size / nm... [Pg.319]

Comparison of oxygen reduction mass and specific activity of a series of carbon supported Pt catalysts with varying metal area as cathodes in MILAs. Activity at 900 mV, 150 kPa O2, 100% RH, 0.4 mg (Pt) cm . ... [Pg.20]

As mentioned, the solution (oxidizer) plays a difficult and dominating role in the metal slurry. On one hand, the selectivity between different metal layers should be close to unity. On the other hand, the selectivity between metal and oxide should be as large as possible. Further, on one hand, the polish rate for metal needs to be higher than 3000 A/min. On the other hand, dishing or plug recession must be minimized at the metal areas on the patterned wafers. [Pg.149]

ICE technology is not designed to remove or treat chlorinated vapors that can produce an offgas stream containing hydrochloric acid. This technology does not treat nonvolatile compounds or heavy metals. Areas with low-permeability soils where minimal flow rates are expected may not be appropriate for this technology. [Pg.913]

As the catalytic reaction proceeds at the surface of the metal particles, the catalysts have been prepared to expose a large metal area, typically 10 - 100 m per gram of catalyst. [Pg.59]

N-methylation with methanol. These results can be obtained without increasing the partial hydrogen pressure as was observed for unpromoted catalysts. On the other hand we noticed that these compounds don t modify the metallic area but decrease the reducibility which means that copper oxide and chromium (VI) oxide are only partially reduced. Moreover as the highly adsorbed hydrogen is also inhibited and as these catalysts are more stable in the presence of H2O or NH3 than unpromoted catalysts, one can also deduce that one of the important roles of the hydrogen during the reaction is to prevent the modification of catalysts or/and the amination reaction by ammonia and water. [Pg.350]

A final alternative for metal patterning is the use of lasers to selectively and accurately etch small metal areas. Lasers are routinely used to trim thin-film resistors (126) they may also be used to repair defects or etch conductor lines by direct ablation in an inert atmosphere (127,129) or by laser-initiated etching in a reactive gas or liquid (128). [Pg.493]

These activities were based on activities per unit metallic area rather than on activities per gram, as in the results of Fischer and Tropsch. Rostrup-Nielsen suggests that the low activity of the cobalt may be due to the fact that the reaction was carried out under conditions when the cobalt can be oxidized by the steam of the reaction mixture. For the methanation reaction, Fischer, Tropsch, and Dilthey49 give the following order of activities for the Group VIII metals ... [Pg.13]


See other pages where Metallic area is mentioned: [Pg.276]    [Pg.106]    [Pg.56]    [Pg.743]    [Pg.516]    [Pg.578]    [Pg.786]    [Pg.152]    [Pg.204]    [Pg.385]    [Pg.433]    [Pg.438]    [Pg.319]    [Pg.514]    [Pg.178]    [Pg.19]    [Pg.185]    [Pg.136]    [Pg.414]    [Pg.133]    [Pg.113]    [Pg.372]    [Pg.106]    [Pg.478]    [Pg.88]    [Pg.162]    [Pg.22]    [Pg.23]   
See also in sourсe #XX -- [ Pg.22 , Pg.99 , Pg.118 , Pg.195 , Pg.196 , Pg.198 ]




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Area-selective metallization

Calculation of Metal Surface Area, Dispersion, and Particle Diameter

Chemisorption metal surface area

High Surface Area Metal Fluorides as Catalysts

High-surface-area alkaline earth metal oxides

Hydrogen-oxygen titration metal surface area

Metal Surface Area, Crystallite Size, and Dispersion

Metal area

Metal area

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Relationships Between Metal Dispersion, Surface Area, and Crystallite Size

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Synthesis of High-Surface-Area Alkaline Earth Metal Oxides

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