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mfw553947967½ð³æ (ÖøÃûдÊÖ)
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The efficiency of removing organic substances from source water by coagulation in clarifiers does not exceed 50¨C70%. The use in clarifiers of imported flocculants (among which are neutral ones like Accoflock No. 100, weakly cationite ones like Accoflock C-483, and anionite ones like Accoflock A-110 and Accoflock A-130) and domestically produced flocculants (PAA and VPK-402) allows the throughput capacity of clarifiers to be increased by 15¨C20% and the efficiency of removing organic matter to be improved by 10-20%. Metering powdered activated carbon into clarifier also somewhat increases the extent of removing organic impurities, but this operation requires up to 0.5 kg/t of activated carbon. In addition, the treatment of water in clarifiers requires bulky equipment and has well-known drawbacks as far as control and closed-loop regulation of its operation are concerned. Gellike ion-exchange materials made using polystyrene as a basic component (AB-17-8) decrease to some extent the concentration of organic compounds in the water being treated, but they themselves are ¡°poisoned¡± by these compounds. This is manifested in the working capacity dropping, the quality of filtrate deteriorating, and the consumption of water for washing increasing. Anionites having macroporous and isoporous structures feature a higher capacity with respect to organic contaminants and resistance to ¡°poisoning.¡± Sequential treatment of water with weakly and strongly alkaline anionites, e.g., JRA-67 and JRA-900, allows as much as 80¨C90% of organic matter to be removed. However, this technology requires a large consumption of alkali, because 30% of the spent regeneration solution for the secondstage anionite filter has to be discharged; it involves periodic recovery-cleaning operations carried out using salt and salt-alkaline solutions, and the relevant operating conditions need to be individually adjusted [2]. |
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mfw553947967: ½ð±Ò+30, ·ÒëEPI+1, ¡ï¡ï¡ïºÜÓаïÖú 2013-04-26 21:10:20
°®ÓëÓêÏÂ: ½ð±Ò-30, ·ÒëEPI-1 2013-04-26 21:44:52
°®ÓëÓêÏÂ: ½ð±Ò-30, ·ÒëEPI-1 2013-04-26 21:44:52
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2Â¥2013-04-26 19:35:36














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