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Pellet shell

A year ago, Hevl-Steel was Introduced to Increase the range of an effective shot with smaller pellets. Shells use a layer of steel beneath a layer of higher density tungsten-matrix shot. All of the pellets have the approximate same ballistic performance there are just more of them in Hevi-Metal shells. By contrast, Hevl-Steel pellets all have the same density, about 20 percent denser than steel. [Pg.67]

Activated carbon is an amorphous solid with a large internal surface area/pore strucmre that adsorbs molecules from both the liquid and gas phase [11]. It has been manufactured from a number of raw materials mcluding wood, coconut shell, and coal [11,12]. Specific processes have been developed to produce activated carbon in powdered, granular, and specially shaped (pellet) forms. The key to development of activated carbon products has been the selection of the manufacturing process, raw material, and an understanding of the basic adsorption process to tailor the product to a specific adsorption application. [Pg.239]

The frozen shells were ground in a cold mortar with 50 mM sodium acetate buffer, pH 5.8, containing 10 mM EGTA and 0.2 M NaCl, then the mixture was centrifuged. The pellets were re-extracted with the same buffer, and centrifuged. All supernatants were combined, and the photoprotein was precipitated with ammonium sulfate. The photoprotein in the precipitate was purified by four steps of column chromatography at near 0°C. Due to the instability of the photoprotein, efforts were made to reduce the time required for purification. [Pg.309]

Diffusion effects can be expected in reactions that are very rapid. A great deal of effort has been made to shorten the diffusion path, which increases the efficiency of the catalysts. Pellets are made with all the active ingredients concentrated on a thin peripheral shell and monoliths are made with very thin washcoats containing the noble metals. In order to convert 90% of the CO from the inlet stream at a residence time of no more than 0.01 sec, one needs a first-order kinetic rate constant of about 230 sec-1. When the catalytic activity is distributed uniformly through a porous pellet of 0.15 cm radius with a diffusion coefficient of 0.01 cm2/sec, one obtains a Thiele modulus y> = 22.7. This would yield an effectiveness factor of 0.132 for a spherical geometry, and an apparent kinetic rate constant of 30.3 sec-1 (106). [Pg.100]

A final category of encapsulating materials consists of reaction products of the nucleus material and a reagent. For example, pellets of nitronium perchlorate have been encapsulated in shells of the less reactive amm perchlorate (AP) by exposing the pellets to ammonia gas. The fragile AP shells were usually further protected by a top-coating of A1 or a polymer film (Ref 2). The most familiar example of this process is the natural one wherein A1 powders (or articles) become coated with a protective coating of A1 oxide thru exposure to atmospheric air... [Pg.142]

Capsules— These are primarily intended for oral administration and are solid preparations with hard or soft shells comprised of gelatin or hydrox-ypropyl methyl cellulose and small amounts of other ingredients such as plasticizers, fillers, and coloring agents. Their contents may be powders, granules, pellets, liquids, or pastes. [Pg.680]

Reetz et al. have used N-(octyl)4Br-stabilized Pd colloids (typical size, e.g., 3nm) as precursors to form so-called cortex-catalysts, where the active metal forms an extremely fine shell of less than lOnm on the supports (e.g., AI2O3). Within the first 1-4 s, the impregnation of AI2O3 pellets by dispersed nanostructured metal colloids leads to the time-dependent penetration of the support which is complete after 10 s. Cortex catalysts were reported to show a threefold higher activity in olefin hydrogenation than conventionally prepared catalysts of the same metal loading (5% Pd on AI2O3) [388]. [Pg.38]

Since many metallic catalysts have high adsorption affinities, we often find that certain poison molecules are adsorbed in an immobile form after only a very few collisions with the catalyst surface. In this situation, the outer periphery of the catalyst particle will be completely poisoned while the inner shell will be completely free of poison. The thickness of the poisoned shell grows with prolonged exposure to poison molecules until the pellet is completely deactivated. During the poisoning process, the boundary between active and deactivated regions is relatively sharp. [Pg.466]

Erroneous use of aluminium instead of alumina pellets in a hydrogen chloride purification reactor caused a vigorous exothermic reaction which distorted the steel reactor shell. [Pg.34]

Natural resources are also affected by environmental lead contamination, and some wildlife species numbers may be reduced as a result. For example, waterfowl deaths resulting from the ingestion of spent lead shot pellets from shotgun shells were discovered more than 100 years ago in Italy and in the United States since then, lead poisoning of waterfowl has occurred in 20 countries (Pain et al. 1995). In North America alone, approximately 3000 tons of lead shot are expended annually into lakes, marshes, and estuaries by several million waterfowl hunters (USFWS 1986,... [Pg.236]

SPHER [Shell Pellet Heat Exchange Retorting] A process for extracting oil from shale. The process is conducted in a fluidized bed in which heat is transferred by inert pellets of two... [Pg.251]

A shell of radii r and r + Sr within the solid pellet particle of radius R may be considered. Making a material balance for the reactant, then ... [Pg.277]

Fig. 6 (a) 2-D 7) maps, (b) their 1-D central cross sections, and (c) the 1-D profiles of hexachloroplatinate dianion distributions obtained by electron probe analyzer measurements. S-2 and S-3 identify different porous alumina pellets, both prepared with an egg-shell distribution of hexachloroplatinate dianion the dianion is located towards the external surface of the pellet). S-2 and S-3 differ in terms of their nominal diameter and their pore-size and surface-area characteristics. Reprinted with permission from ref. 24. Copyright (2000) American Chemical Society. [Pg.294]

Decomposition of hydrogen sulfide. Mo 2 catalytic pellets packed on the shell side of the reactor. [Pg.125]

Dehydrogenation of ethylbenzene to styrene. Lio.5Fe2.4Cro.1O4 with 12wt.% K2O and 3wt.% V2O3 catalytic pellets packed on reactor shell side. [Pg.128]


See other pages where Pellet shell is mentioned: [Pg.429]    [Pg.189]    [Pg.334]    [Pg.260]    [Pg.429]    [Pg.189]    [Pg.334]    [Pg.260]    [Pg.1702]    [Pg.242]    [Pg.287]    [Pg.202]    [Pg.159]    [Pg.24]    [Pg.1205]    [Pg.1223]    [Pg.2015]    [Pg.2103]    [Pg.173]    [Pg.251]    [Pg.276]    [Pg.330]    [Pg.421]    [Pg.194]    [Pg.170]    [Pg.695]    [Pg.28]    [Pg.356]    [Pg.115]    [Pg.83]    [Pg.431]    [Pg.447]    [Pg.458]    [Pg.198]    [Pg.23]    [Pg.194]    [Pg.272]    [Pg.297]    [Pg.76]   
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Shell pellet heat exchange retorting

Shell pellet heat exchange retorting SPHER)

Shell pellet heat exchange retorting process

Shell pellet heat exchange retorting retort

Shell pellet heat exchange retorting shale

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