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北京石油化工学院2026年研究生招生接收调剂公告
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mfw553947967

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[求助] 一段论文翻译,求助,非常感谢

The efficiency of removing organic substances from
source water by coagulation in clarifiers does not
exceed 50–70%. 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 15–20% 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 80–90% 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: 金币+30, 翻译EPI+1, ★★★很有帮助 2013-04-26 21:10:20
爱与雨下: 金币-30, 翻译EPI-1 2013-04-26 21:44:52
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