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Powered activated carbon

Ying, W.C., R.R. Bonk and S.A. Sojka. Treatment of Landfill Leachate in Powered Activated Carbon Enhanced Sequencing Batch Bioreactors. In Proc. of the 18th Mid-Atlantic Ind. Waste Conference, Technomic Publishing Company, Inc., Lancaster, Pennsylvania, 1986. [Pg.169]

The city of Columbus, Ohio, installed a PACT water treatment system for 1.2 million. The system was purchased to remove atrazine (a pesticide) from the water supply. In 1997, Columbus spent 150,000 on powered activated carbon. Additional monitoring costs were estimated to be over 10,000 per year (D19947H, p. 11). [Pg.1083]

Adsorption of Radionuclides. Other appHcations that depend on physical adsorption include the control of krypton and xenon radionuchdes from nuclear power plants (92). The gases are not captured entirely, but their passage is delayed long enough to allow radioactive decay of the short-hved species. Highly rnicroporous coconut-based activated carbon is used for this service. [Pg.535]

Ishikawa, M., Sakamoto, A., Morita, M., Matsuda, Y. and Ishida, K., Effect of treatment of activated carbon fiber cloth electrodes with cold plasma upon performance of electric double layer capacitors, J. Power Sources, 1996, 60(2), 233 238. [Pg.118]

The adsorbers are usually built of steel, and may be lagged or left unlagged the horizontal type is shown in Figure 28. The vapor-laden air is fed by the blower into one adsorber which contains a bed of 6- to 8-mesh activated carbon granules 12 to 30 inches thick. The air velocity through the bed is 40 to 90 feet per minute. The carbon particles retain the vapor only the denuded air reaches the exit, and then the exhaust line. The adsorption is allowed to continue until the carbon is saturated, when the vapor-laden air is diverted to the second adsorber, while the first adsorber receives low-pressure steam fed in below the carbon bed. The vapor is reformed and carried out by the steam. The two are condensed and if the solvent is not miscible with water, it may be decanted continuously while the water is run off similarly. After a period which may be approximately 30 or 60 minutes, all the vapor has been removed, the adsorbing power of the charcoal has been restored, and the adsorber is ready to function again, while adsorber No. 2 is steamed in turn. [Pg.300]

Gunnerson, Gary. Using Activated Carbon for Pretreatment in the Power Industry. Ultrapure Water, Tall Oaks Publishing, Inc., USA, October 1998. [Pg.766]

Activated carbons possess sufficient volumetric conductivity for electrolyte/collector current interchange. However, contact resistance between carbon particles in the electrode limits charge/discharge currents of the porous volumetric system and therefore EC s power capability. [Pg.44]

Summarizing the above, it may be stated that activated carbons and pseudocapacitive materials in EC electrode structure are responsible for the energy storage parameters (specific energy), while non-active highly conductive carbon additives are responsible for the electrode internal resistance (EC specific power). [Pg.45]

Qu D., Studies of the activated carbons used in double-layer supercapacitors, J. Power Sourc. 2002 109 403-411. [Pg.95]

Iliev I., Mrha J., Gamburzev S., Kaisheva A., On the effect of various active carbon catalysts on the behaviour of carbon gas-diffusion air electrodes, Journal Power Sources 1976/77 1 35-46. [Pg.156]

In Moscow Power Engineering Institute (TU) portable air aluminum batteries with saline electrolyte were developed [7, 18, and 20], In our devices, the air electrodes consist of two layers. Diffusion layer contains PTFE, carbon black and metal screen active layer consists of activated carbon and PTFE. At 293 K and the range of current density 2-25 mA/ cm2 dependence of cathode potential E (in H-scale) upon current density J (Figure 2) may by written by the Tafel equation (12). [Pg.165]

Delay for Decay A process for trapping radioactive gases (e.g., xenon, krypton, iodine) from nuclear power plants until their radioactivities have decayed to acceptable levels. Activated carbon is the usual adsorbent, and the gases are first dried with a zeolite. [Pg.82]

ELCOX A flue-gas desulfurization process in which the sulfur dioxide is oxidized elec-trochemically to sulfuric acid, using an organometallic catalyst (e.g., cobalt phthalocyanine) adsorbed on activated carbon. Developed by the Central Laboratory of Electrochemical Power Sources, Sofia, Bulgaria. [Pg.97]


See other pages where Powered activated carbon is mentioned: [Pg.123]    [Pg.111]    [Pg.36]    [Pg.39]    [Pg.454]    [Pg.123]    [Pg.111]    [Pg.36]    [Pg.39]    [Pg.454]    [Pg.286]    [Pg.498]    [Pg.535]    [Pg.158]    [Pg.161]    [Pg.109]    [Pg.184]    [Pg.198]    [Pg.339]    [Pg.301]    [Pg.36]    [Pg.373]    [Pg.46]    [Pg.633]    [Pg.204]    [Pg.45]    [Pg.64]    [Pg.72]    [Pg.96]    [Pg.97]    [Pg.105]    [Pg.130]    [Pg.131]    [Pg.205]    [Pg.219]    [Pg.360]   
See also in sourсe #XX -- [ Pg.142 ]




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