| 2 | 1/1 | 返回列表 |
| 查看: 459 | 回復(fù): 1 | |||
mfw553947967金蟲 (著名寫手)
|
[求助]
一段論文翻譯,求助,非常感謝
|
|
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]. |

|
本帖內(nèi)容被屏蔽 |
| 2 | 1/1 | 返回列表 |
| 最具人氣熱帖推薦 [查看全部] | 作者 | 回/看 | 最后發(fā)表 | |
|---|---|---|---|---|
|
[材料工程] 一志愿C9材料與化工專業(yè)總分300求調(diào)劑 +6 | 曼111 2026-03-24 | 7/350 |
|
|---|---|---|---|---|
|
[考研] 一志愿哈爾濱工業(yè)大學(xué)材料與化工方向336分 +3 | 辰沐5211314 2026-03-26 | 3/150 |
|
|
[考研] 304求調(diào)劑 +3 | 曼殊2266 2026-03-27 | 3/150 |
|
|
[考研] 308求調(diào)劑 +6 | 墨墨漠 2026-03-25 | 6/300 |
|
|
[考研] 食品工程專碩求調(diào)劑 +3 | 小張zxy張 2026-03-26 | 3/150 |
|
|
[考研] 294分080500材料科學(xué)與工程求調(diào)劑 +4 | 柳溪邊 2026-03-26 | 4/200 |
|
|
[考研] 材料考研求調(diào)劑 +3 | Dendel 2026-03-23 | 6/300 |
|
|
[考研] 297求調(diào)劑 +6 | 田洪有 2026-03-26 | 6/300 |
|
|
[考研] 315分求調(diào)劑 +5 | 26考研上岸版26 2026-03-26 | 5/250 |
|
|
[考研] 085600 材料與化工 329分求調(diào)劑 +9 | Mr. Z 2026-03-25 | 9/450 |
|
|
[考研] 一志愿上海交大生物與醫(yī)藥專碩324分,求調(diào)劑 +6 | jiajunX 2026-03-22 | 6/300 |
|
|
[考研] 318求調(diào)劑 +5 | plum李子 2026-03-21 | 8/400 |
|
|
[考研] 311求調(diào)劑 +3 | 冬十三 2026-03-24 | 3/150 |
|
|
[考研] 調(diào)劑 +4 | 13853210211 2026-03-24 | 4/200 |
|
|
[考研] 化工專碩求調(diào)劑 +3 | question挽風(fēng) 2026-03-24 | 3/150 |
|
|
[考研] 292求調(diào)劑 +4 | 鵝鵝鵝額額額額?/a> 2026-03-24 | 4/200 |
|
|
[考研] 291求調(diào)劑 +3 | HanBeiNingZC 2026-03-24 | 3/150 |
|
|
[考研] 305分求調(diào)劑(食品工程) +5 | Sxy112 2026-03-21 | 7/350 |
|
|
[考研] 361求調(diào)劑 +3 | Glack 2026-03-22 | 3/150 |
|
|
[考研] 0703化學(xué)297求調(diào)劑 +3 | Daisy☆ 2026-03-20 | 3/150 |
|