| 研究生: |
洪啟昌 Hong, Chi-Chang |
|---|---|
| 論文名稱: |
次磷酸溶液處理方法之研究
-化學混凝法、吸附法與氧化法 Study on the Treatment of Hypophosphite Solution by Chemical Coagulation、Adsorption and Oxidation |
| 指導教授: |
黃耀輝
Huang, Yao-Hui |
| 學位類別: |
碩士 Master |
| 系所名稱: |
工學院 - 化學工程學系 Department of Chemical Engineering |
| 論文出版年: | 2005 |
| 畢業學年度: | 93 |
| 語文別: | 中文 |
| 論文頁數: | 133 |
| 中文關鍵詞: | 鐵氧化物 、氧化 、異相 、芬頓 、吸附 、化學混凝 |
| 外文關鍵詞: | Oxidation, Iron Oxide, Fenton, Heterogeneous, Chemical Coagulation, Adsorption |
| 相關次數: | 點閱:68 下載:5 |
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本研究針對次磷酸探討其處理方法,在化學混凝法與吸附法方面,發現它們對次磷酸的處理效果都不佳;另一方面,它們對亞磷酸與磷酸則有相當好的處理效果。所以,本研究嘗試利用芬頓試劑與鐵氧化物異相催化觸媒來氧化次磷酸,成為亞磷酸與磷酸,再分別以化學混凝法和吸附法將磷去除。
在化學混凝法方面,研究結果發現於pH4時對亞磷酸與磷酸的處理效果最佳,在1mM磷下,Fe(III)對磷酸莫耳比為1.5時可將磷酸完全去除,對亞磷酸則莫耳比2.0時可達放流水排放標準;在芬頓法氧化次磷酸方面,其最佳操作條件為pH介於2.5~3.0之間,針對1 ~100 mM的次磷酸,試劑莫耳比次磷酸:Fe(II):H2O2 =1:1.5:3下,其去除率可高達99%以上。
另一方面,本研究嘗試利用覆膜鐵氧化物(B1)為過氧化氫的觸媒來氧化次磷酸,此觸媒是經過實廠流體化床-芬頓(FBR-Fenton)反應槽中製備而成,經由XRD與FTIR的分析研判其為針鐵礦、纖鐵礦與水合鐵礦的混合體,pHzpc為5.38,比表面積為132.4m2/g。其對磷酸的最大吸附量達0.7 mmole/g-B1,而對亞磷酸(pH2.5)與磷酸(pH3)的吸附熱分別為13.1 kJ/mole與16.7 kJ/mole。在異相催化氧化方面,針對pH效應討論其次磷酸氧化率與總磷的去除效變化。論由實驗的結果提出簡化的反應機說明次磷酸的氧化途徑。另外,異相催化氧化1 mM次磷酸的結果顯示,在pH4時,可在五個小時內將次磷酸濃度降到0.1mM以下。
This study investigated the treatment methods of hypophosphite. We found that neither chemical coagulation nor adsorption could remove hypophosphite from water. On the other hand, they showed excellent removal efficiency in treating phosphite and phosphate. According to these results, we try to treat hypophosphite by Fenton’s reagent or heterogeneous catalyst oxidation. After it is oxidized to phosphite or phosphate it can be easily removed by chemical coagulation or adsorption.
This investigation reveals that phosphite and phosphate can be easily removed at pH4. The optimum Fe(III) dosages are 2.0 and 1.5 in molar ratio for phosphite and phosphate, respectively. For 1-100 mM hypophosphite, Fenton’s reagent can remove phosphorus almost completely at pH2.5-3.0 with the molar dose of hypophosphite : Fe(II) : H2O2 = 1 : 1.5 : 3. The effects of Fe2+, H2O2, hypophosphite, and solution pH on hypophosphite oxidation are demonstrated in detail. Increasing the dose of iron(II) enhances the hypophosphite oxidation. The optimal levels of H2O2 required for the process are also examined.
On the other hand, we try to use a novel supported iron oxide (B1), prepared through a fluidized-bed reactor (FBR-Fenton), as a catalyst for the heterogeneous oxidation of hypophosphite. the results of XRD and FTIR show that it is composed of goethite , lepidocrocite and ferrihydrite. The pHzpc of B1 is 5.38 and its specific surface area is 166.1 m2/g by BET analysis. The maximum adsorption capacity of phosphate is 0.7 mmole/g-B1, and the ΔHads is 13.1 kJ/mole for phosphate at pH2.5, and 16.7 kJ/mole for phosphate at pH=3.0. The effect the solution pH on the oxidation of hypophosphite and total phosphorus removal efficiency is elucidated in detail. A simplified mechanism of hypophosphite decomposition that is consistent with the experimental findings is proposed. In addition, result of Fenton like showed that hypophosphite can be oxidized effectively at pH4, it can remove phosphorus to 0.1mM after five hours.
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