實驗中所使用的觸媒是在實廠流體化床反應槽中製備而成，鐵氧化物經分析結果發現，大部分為非結晶態的鐵氧化物。在分解過氧化氫及氧化苯胺的可行性及動力方面研究，是以批次反應進行實驗。

　　在未添加苯胺時，過氧化氫分解的二階反應常數在B1及W1系統中分別為2.11×10-4 1/min‧gB1及6.65×10-4 1/min‧gW1。

　　苯胺分解實驗中發現，苯胺的分解與鐵氧化物、過氧化氫劑量、初始pH值、溫度、觸媒表面溶出鐵有關。動力探討方面，Langmuir- Hinshelwood模式來表示，在B1系統中所求得反應常數k值及吸附常數K值分別為9.45μM min-1及8.49×10-4μM-1，而活化能為13.64　kcal/mole；在W1系統中求得的反應常數k值及吸附常數K分別為20.08μM min-1及6.02×10-4μM-1，活化能E=15.49kcal/mole。

　　The catalyst in this study is prepared in a fluidized bed reactor. The components coated on the surface were identified as amorphous iron oxides. The feasibility and kinetics discussion about the decomposition of H2O2 and aniline oxidation were studied in a batch reactor.

　　When the H2O2 decomposition was in the absence of Aniline, the second order reaction constant in B1 and W1 system were 2.11×10-4 1/min‧gB1 and 6.65×10-4 1/min‧gW1 respectively.

　　We found that the initial pH value, temperature, H2O2 and catalyst concentration would effect the degradation of aniline. we used Langmuir- Hinshelwood model to explain the kinetics of reaction. In the B1/Aniline system, the　reaction constant k is 9.45μM min-1 and the adsorption constant K is 8.49×10-4μM-1 and the activity energy is　13.64 kcal/mole. In the W1/Aniline system, the reaction constant k is 20.08μM min-1 and the adsorption constant K is 6.02×10-4μM-1 and the activity energy E is　15.49kcal/mole .

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