Photochemically enhanced degradation of phenol using heterogeneous Fenton-type catalysts

The degradation of phenol was carriced out using heterogeneous Fenton-type catalysts in the presence of H2O2 and UV.Catalysts were prepared by exchanging and immobilizing Fe^2 in zeolite 13X,silica gel or Al2O3.The concentration of phenol solution was 100mg/L.The amount of H2O2 added was the stoichiometric amount of H2O2 required for the total oxidation of phenol.Under the irradiation of medium pressure light(300W)phenol was mineralized within 1 h in the presence of Fe^2 /zeolite 13X.The COD removal rate was enhanced in the presence of Fe^2 /zeolite 13X compared to that of Fe^2 /silica gel of Fe^2 /Al2O3.Analogous homogenous photo-Fenton reaction with equivalent Fe^2 was also carried out to evaluate the catalysis efficiency of Fe^2 /zeolite 13X.Results showed that the COD removal rate was near to that of homogeneous Fenton,while heterogeneous Fe^2 /zeolite 13X catalyst coule be recycled.     

Simultaneous oxidation of Mn(II) and As(III) on cupric oxide (CuO) promotes As(III) removal at circumneutral pH

Oxidation of Mn(II) or As(III) by molecular oxygen is slow at pH < 9, while they can be catalytically oxidized in the presence of oxide minerals and then removed from contaminated water. However, the reaction mechanisms on simultaneous oxidation of Mn(II) and As(III) on oxide mineral surface and their accompanied removal efficiency remain unclear. This study compared Mn(II) oxidation on four common metal oxides (γ-Al₂O₃, CuO, α-Fe₂O₃ and ZnO) and investigated the simultaneous oxidation and removal of Mn(II) and As(III) through batch experiments and spectroscopic analyses. Among the tested oxides, CuO and α-Fe₂O₃ possess greater catalytic activity toward Mn(II) oxidation. Oxidation and removal kinetics of Mn(II) and As(III) on CuO indicate that O₂ is the terminal electron acceptor for Mn(II) and As(III) oxidation on CuO, and Mn(II) acts as an electron shuttle to promote As(III) oxidation and removal. The main oxidized product of Mn(II) on CuO is high-valent MnO_x species. This newly formed Mn(III) or Mn(IV) phases promote As(III) oxidation on CuO at circumneutral pH 8 and is reduced to Mn(II), which may be then released into solution. This study provides new insights into metal oxide-catalyzed oxidation of pollutants Mn(II) and As(III) and suggests that CuO should be considered as an efficient material to remediate Mn(II) and As(III) contamination.     

Fe2+对大豆幼苗生理特性的影响

以大豆为试验材料,设置了不同的质量分数的Fe2 处理,研究Fe2 对大豆幼苗根系形态特征及其生理特性的影响。结果表明,浸种w(Fe2 )为5mg·kg-1时对大豆幼苗的发育最有利。用低w(Fe2 )(0或0.01mg·kg-1)时,根系生长受阻,氧化物酶活性随Fe2 的升高而上升,脯氨酸、丙二醛的含量变化幅度不大;w(Fe2 )过高(50~100mg·kg-1),则会引发植物体的抗逆性反应,表现为脯氨酸、可溶性糖、丙二醛等渗透调节物大量积累、过氧化物酶活性降低;当w(Fe2 )高达75mg·kg-1和100mg·kg-1时,会引起植物重金属中毒,表现为幼苗的脯氨酸、可溶性糖、丙二醛含量、过氧化物酶活性都大幅度地降低。     

磷胁迫对水稻基因型根系形态及吸收铁锰铜锌的影响

采用营养液培养方法研究了缺磷胁迫下4种水稻基因型(90-90—1、金23A、90-68-1、CDR22)的根系形态变化情况及其吸收微量元素铁、锰、铜、锌的影响。结果表明，(1)磷胁迫下，每个基因型在磷胁迫下其根系形态发生了明显变化、如根长、根冠比均呈增加趋势，并且根表有红棕色铁氧化物膜包被。(2)磷胁迫下根系形态的变化影响了水稻对生长介质中铁、锰、铜、锌的吸收：正常水稻植株中铁、锰、锌的含量高于磷胁迫植株，其中磷营养状况对水稻吸收铁、锰影响最明显；而磷营养状况对水稻植株铜含量的影响与铁、锰、锌正好相反，且影响程度较小。     

选择性萃取方法在生物膜上铁、锰氧化物分离中的应用

1　IntroductionSurfacecoatings (biofilmsandassociatedminerals)existonallkindsofsolidphasesinnaturalaquaticenvironments.FeandMnoxideswerefoundedtobethemostimportantcomponentsofsur facecoatingsfortheirhighadsorptioncapacity[1—3].Tostudytherelativeroleofdif…     

有机肥与植物种类对铁肥形态转化及其有效性的影响

通过盆栽试验的方法,研究了牛粪和植物种类对石灰性土壤中铁肥形态转化及其有效性的影响。结果表明,牛粪施用改变了土壤中铁(含外源铁)的有效性及其在各形态铁间的分配。从长期的观点来看,牛粪施用能提高土壤铁的有效性,有利于土壤铁有效供给的维持。与花生相比,油莱对土壤铁具有更高的利用和活化能力,种植油菜后,土壤交换态铁被耗竭,而有效铁、氧化锰结合态铁和无定形氧化铁结合态铁的含量明显提高。有机肥的合理施用和铁效率差异性植物间的轮作或间作是增加、维系土壤铁有效性的重要农艺措施。     

铜锰钴复合氧化物催化剂对环己烷或苯深度氧化的催化活性

本文应用了研究相图与床层温差评价催化活性的方法，研究了在催化深度氧化环己烷或苯的反应中，铜、锰、钴三元氧化物催化剂体系的组成与催化活性的关系。用反应物在催化剂上起燃温度的等温图，描绘出该体系氧化物催化剂对环己烷或苯的催化氧化活性的分布。所得结果指导了用于净化苯系物废气所需催化剂的研制。     

印染废水治理技术

论述了以铁碳过滤 +SBR为主要工艺的印染废水处理技术。该技术在实际工程中连续运行 8a的结果表明 :该工艺用于印染废水的治理切实可行、经济可靠 ,出水水质稳定能够达到国家一级排放标准 ,并能全部实现回用     

水溶液中2,4-二氯苯酚的光降解研究

研究不同光源下2,4 二氯苯酚直接光解,以及水溶液中Fe(Ⅲ) OH络合物对2,4 二氯苯酚光解的影响,并考虑了光强、浓度、pH值等一些影响因素。     

高浓度薛佛氏盐生产废水的资源化处理工艺研究

提出了一种薛佛氏盐生产废水处理工艺 ,其方法是 :首先用 730 1树脂—磺化煤油络合萃取回收废水中的 R盐 ,萃取后的废水再用 H2 O2 / Fe2 +催化氧化处理 ;研究了影响萃取效率的主要因素。实验表明 ,R盐回收率可达 98%以上 ;催化氧化后的废水可达标排放