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Percolators continuous

The topology and connectivity of the two types of domain is expected to change according the nature of the ions. Relatively small alkyl side chains form discontinuous nonpolar pockets dispersed in a percolating (continuous) ionic network. As the... [Pg.173]

Actually, this presentation is over-simplified. In a column the mathematics are far more complex because as the percolation continues, the concentration of adsorbed substance steadily increases in all portions of the carbon bed, and the increase moves as a wave from the entrance of the column to the exit. [Pg.334]

A chromatogram (so-named by its Polish inventor, Tswett, because he used the technique to separate plant pigments) consists of two immiscible phases. One phase is kept stationary by either being held on an inert microporous support or being itself a microporous or particulate adsorbent solid the other phase is percolated continuously through the stationary phase. Various phase pairs are possible although liquid-solid and gas-liquid are the most common. [Pg.13]

Eor pesticides to leach to groundwater, it may be necessary for preferential flow through macropores to dominate the sorption processes that control pesticide leaching to groundwater. Several studies have demonstrated that large continuous macropores exist in soil and provide pathways for rapid movement of water solutes. Increased permeabiUty, percolation, and solute transport can result from increased porosity, especially in no-tiUage systems where pore stmcture is stiU intact at the soil surface (70). Plant roots are important in creation and stabilization of soil macropores (71). [Pg.223]

Further down, ca 75 cm below the electrode tips, the mix is hot enough (2200—2500°C) to allow the lime to melt. The coke does not melt and the hquid lime percolates downward through the relatively fixed bed of coke forming calcium carbide, which is Hquid at this temperature. Both Hquids erode coke particles as they flow downward. The weak carbide first formed is converted to richer material by continued contact and reaction with coke particles. The carbon monoxide gas produced in this area must be released by flowing back up through the charge. The process continues down to the taphole level. Material in this area consists of soHd coke wetted in a pool of Hquid lime and Hquid calcium carbide at the furnace bottom. [Pg.461]

Use of Desiccants and Chemical Means to Remove Water. Another means to remove the water of esterification is calcium carbide supported in a thimble of a continuous extractor through which the condensed vapor from the esterification mixture is percolated (41) (see Carbides). A column of activated bauxite (Elorite) mounted over the reaction vessel has been used to remove the water of reaction from the vapor by adsorption (42). [Pg.376]

It is classification by contacting method that provides the two principal categories into which leaching equipment is divided (I) that in which the leaching is accomphshed oy percolation and (2) that in which particulate solids are dispersed into a hquid and subsequently separated from it. Each includes batch and continuous units. Materials which disintegrate during leaching are treated in equipment of the second class. [Pg.1673]

Percolation In addition to being applied to ores and rock in place and by the simple technique of heap leaching (usually on verv large scale see Wadsworth, loc. cit.) percolation is carried out in batcJi tanks and in continuous or dump extractors (usually on smaller scale). [Pg.1673]

Continuous Percolators Coarse sohds are also leached by percolation in moving-bed equipment, including single-deck and nmlti-deck rake classifiers, bucket-elevator contactors, and horizontal-belt conveyors. [Pg.1673]

Screw-Conveyor Extractors One type of continuous leaching equipment, employing the screw-conveyor principle, is strictly speaking neither a percolator nor a dispersed-solids extractor. Although it is often classed with percolators, there can be sufficient agitation of the solids during their conveyance by the screw that the action differs from an orthodox percolation. [Pg.1675]

Leaching Cycle and Contact Method As is true generally, the choice between continuous and intermittent operation is largely a matter of the size and nature of the process of which the extraction is a part. The choice of a percolation or solids-dispersion technique depends principally on the amenability of the extraction to effective, sufficiently rapid percolation. [Pg.1676]

Initial Extraction Technique Continuous extraction apparatus was employed, including an extractor designed to contain the starting plant materials, a distillation flask to hold the solvent mixture, the flask being equipped with a reflux condenser, a drip device to facilitate the removal of the volatilized mixture from the condenser and to percolate it through the continuous extractor, and a Soxhiet type return. Means for heating the continuous extraction system were provided. [Pg.396]

The remarkably ordered behavior of N, 2)-nets derives principally from the appearance of a connected frozen core of sites, each element of which remains frozen in a fixed stattn This frozen core creates percolating walls of constancy that effectively partition the not into a dynamically static subset and (dynamically) isolated islands of sites that continue evolving but are incapable of communicating through the frozen core. [Pg.432]

The main notion of the percolation theory is the so-called percolation threshold Cp — minimal concentration of conducting particles C at which a continuous conducting chain of macroscopic length appears in the system. To determine this magnitude the Monte-Carlo method or the calculation of expansion coefficients of Cp by powers of C is used for different lattices in the knots of which the conducting par-... [Pg.129]

In the case of the filler localization in one of the polymer components of the mixture, an increase of the portion of the second unfilled polymer component in it entails sharp (by a factor of lO10) rise of a in the conducting polymer composite. In this case the filled phase should be continuous, i.e. its concentration should be higher than the percolation threshold. [Pg.137]


See other pages where Percolators continuous is mentioned: [Pg.540]    [Pg.568]    [Pg.110]    [Pg.159]    [Pg.327]    [Pg.540]    [Pg.568]    [Pg.156]    [Pg.184]    [Pg.476]    [Pg.387]    [Pg.156]    [Pg.540]    [Pg.568]    [Pg.540]    [Pg.568]    [Pg.110]    [Pg.159]    [Pg.327]    [Pg.540]    [Pg.568]    [Pg.156]    [Pg.184]    [Pg.476]    [Pg.387]    [Pg.156]    [Pg.540]    [Pg.568]    [Pg.368]    [Pg.488]    [Pg.90]    [Pg.118]    [Pg.331]    [Pg.334]    [Pg.388]    [Pg.1673]    [Pg.1674]    [Pg.412]    [Pg.311]    [Pg.384]    [Pg.373]    [Pg.427]    [Pg.430]    [Pg.735]    [Pg.140]    [Pg.402]    [Pg.130]    [Pg.37]    [Pg.328]    [Pg.86]   


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