零价铁-过二硫酸盐连续运行体系去除水中硝基苯

水中硝基苯(NB)的高毒性对人体健康具有极大的危害,因此,本文建立了零价铁-过二硫酸盐(Fe0-PS)连续运行体系以降解水中NB.研究结果表明,单独Fe0柱可还原降解NB,Fe0对不同浓度NB的还原效果均较好,随着流速的减慢及初始pH的降低,NB还原效果变好;但还原体系中总有机碳(TOC)基本没有去除,只是生成了中间产物苯胺(AN).Fe0-PS联合体系中,随着PS的投加,产生的Fe2+活化PS,发生了类Fenton反应,从而使还原产物AN得以氧化降解,TOC去除率可达54.8%;随着Fe0填充量的增加,氧化产物Fe2+随之增加,还原产物AN随之减少.可见,Fe0-PS连续运行体系,以Fe2+为媒介巧妙结合还原与氧化作用,能有效去除NB.     

铁镧复合氧化物纳米吸附剂的制备、表征及As（Ⅲ）吸附性能研究

本研究采用共沉淀法制备了一种新型铁镧复合氧化物吸附剂(Fe-La),并对其表面特性及As(Ⅲ)吸附行为进行了系统研究.扫描电镜(SEM)和透射电镜(TEM)结果表明,铁镧复合氧化物具有纳米结构,初级粒子粒径范围为20~200 nm.X-射线衍射仪(XRD)表征结果表明,铁镧复合氧化物具有类似氢氧化镧的晶型结构.N2吸附BET法结果表明,铁镧复合氧化物的比表面积为99.3 m2·g-1.盐加入法测得吸附剂的等电点为7.8.As(Ⅲ)吸附实验结果分析表明,铁镧复合氧化物对As(Ⅲ)具有良好的吸附效果,最大吸附量(pH 7.0)为58.2 mg·g-1,Langmuir吸附等温线可较好地拟合铁镧复合氧化物对溶液中As(Ⅲ)的吸附(R2=0.95);吸附速率较快,240 min内可完成吸附容量的80%,Elovich模型能较好地描述吸附过程(R2=0.97);溶液pH对铁镧复合氧化物吸附As(Ⅲ)的影响较为明显;共存阴离子对吸附影响的大小顺序为SO2-4相似文献   

还原共沉淀法制备Fe-Ti复合氧化物及其吸附水中As(Ⅴ)的研究

采用还原-共沉淀法制备了无定型纳米复合Fe-Ti氧化物(FFT)吸附剂,并研究其对水中低浓度As(Ⅴ)的去除性能.XRD表征结果表明,制备的纳米FFT物相为无定型,BET比表面积达325.3 m2·g-1,计算得到的BJH吸附平均孔径为2.46 nm(4V/A),颗粒分布均匀.同时,考察了纳米FFT吸附As(Ⅴ)的动力学、热力学、吸附等温线,以及温度、水中共存离子对其去除As(Ⅴ)的影响.结果发现,纳米FFT对As(Ⅴ)的吸附符合拟二级动力学模型,计算出的孔道扩散系数DP在10-11~10-13cm2·s-1之间,显示孔扩散是速率限速步骤.Langmuir、Freundlich和DubininRadushkevich(D-R)吸附等温式均可较好地拟合吸附行为,低浓度下Langmuir吸附模型计算出的Qm达到26.46 mg·g-1.最后,研究了地下水中常见的共存离子对吸附的影响,发现Ca2+、Mg2+能够促进吸附,H2PO-4和HCO-3则明显抑制吸附过程.     

镁离子对氧化亚铁硫杆菌生物合成次生铁矿物的影响

通过摇瓶实验,在Mg2+分别为48,4.8mg/L,其他元素组成与9K液体培养基一致的体系中,采用氧化亚铁硫杆菌A.ferrooxidans催化合成次生铁矿物.考察了Mg2+含量对生物合成次生铁矿物体系pH值、氧化还原电位(ORP)、Fe2+氧化率、总Fe沉淀率、次生铁矿物矿相及矿物晶体尺寸的影响.结果表明,经过48h培养,Mg2+浓度为48,4.8mg/L生物成矿体系pH值分别从原来的2.50降低至2.30,2.19,ORP分别从初始259mV增加至269mV,276mV.两体系Fe2+氧化率培养至第48h均达到100%,然而两体系总Fe沉淀率及矿物形态及却不尽相同.Mg2+浓度为48mg/L生物成矿体系,总Fe沉淀率为23.7%,次生矿物紧密粘附于三角瓶底部.而Mg2+浓度为4.8mg/L生物成矿体系,总Fe沉淀率达到32.2%,次生矿物却均匀分散于溶液中.两体系合成次生铁矿物均为黄铁矾与施氏矿物共存的混合物,Mg2+含量4.8mg/L体系合成黄铁矾单个晶体长度(~1.60μm)约为Mg2+含量48mg/L体系的1.2倍.     

Heterogeneous Fenton-like degradation of 4-chlorophenol using iron/ordered mesoporous carbon catalyst

Ordered mesoporous carbon supported iron catalysts(Fe/OMC) were prepared by the incipient wetness impregnation method and investigated in Fenton-like degradation of 4-chlorophenol(4CP) in this work. XRD and TEM characterization showed that the iron oxides were well dispersed on the OMC support and grew bigger with the increasing calcination temperature. The catalyst prepared with a lower calcination temperature showed higher decomposition efficiency towards 4CP and H2O2, but more metals were leached. The effect of different operational parameters such as initial pH, H2O2 dosage, and reaction temperature on the catalytic activity was evaluated. The results showed that 96.1% of 4CP and 47.4% of TOC was removed after 270 min at 30°C, initial pH of 3 and 6.6 mmol/L H2O2. 88% of 4CP removal efficiency was retained after three successive runs, indicating Fe/OMC a stable catalyst for Fenton reaction. 4CP was degraded predominately by the attack of hydroxyl radical formed on the catalyst surface and in the bulk solution due to iron leaching. Based on the degradation intermediates detected by high performance liquid chromatography, possible oxidation pathways were proposed during the 4CP degradation.     

Isolation, identification and arsenic-resistance of Acidithiobacillus ferrooxidans HX3 producing schwertmannite

Schwertmannite, a ubiquitous mineral present in iron oxyhydroxides formed in iron- and sulfate-rich acid media, favors incorporation of some toxic anions in its structure. We reported an iron-oxidizing bacterial strain HX3 from a municipal sludge that facilitates the formation of pure schwertmannite in cultures. Ferrous iron oxidation by the isolated strain HX3 was optimum at an initial pH of 2.0-3.3 and temperature of 28-35°C. Pure schwertmannite was found through bacterial oxidation of ferrous iron at an initial pH 2.8and temperature 28°C. Following 16 S rDNA gene sequence analysis the bacterial strain HX3 was identified as Acidithiobacillus ferrooxidans. The arsenic-resistance A. ferrooxidans HX3 showed the potential of environmental application in arsenic removal from the As（Ⅲ）- and iron-rich acid sulfate waters directly by As（Ⅲ） adsorption or the formation of schwertmannite in the environment.     

Graphene-supported nanoscale zero-valent iron：Removal of phosphorus from aqueous solution and mechanistic study

Excess phosphorus from non-point pollution sources is one of the key factors causing eutrophication in many lakes in China,so finding a cost-effective method to remove phosphorus from non-point pollution sources is very important for the health of the aqueous environment. Graphene was selected to support nanoscale zero-valent iron(nZVI)for phosphorus removal from synthetic rainwater runoff in this article. Compared with nZVI supported on other porous materials,graphene-supported nZVI(G-nZVI) could remove phosphorus more efficiently. The amount of nZVI in G-nZVI was an important factor in the removal of phosphorus by G-nZVI,and G-nZVI with 20 wt.% nZVI(20% G-nZVI)could remove phosphorus most efficiently. The nZVI was very stable and could disperse very well on graphene,as characterized by transmission electron microscopy(TEM) and scanning electron microscopy(SEM). X-ray photoelectron spectroscopy(XPS),Fourier Transform infrared spectroscopy(FT-IR) and Raman spectroscopy were used to elucidate the reaction process,and the results indicated that Fe-O-P was formed after phosphorus was adsorbed by G-nZVI. The results obtained from X-ray diffraction(XRD) indicated that the reaction product between nZVI supported on graphene and phosphorus was Fe3(PO4)2·8H2O(Vivianite). It was confirmed that the specific reaction mechanism for the removal of phosphorus with nZVI or G-nZVI was mainly due to chemical reaction between nZVI and phosphorus.     

Zn2+对铁氧化物吸附苄嘧磺隆的影响

研究2种人工合成的铁氧化物对磺酰脲类除草剂--苄嘧磺隆(bensulfuron-methyl,BSM)的吸附,以及Zn2 对供试样品吸附苄嘧磺隆的影响.实验结果表明,用Langmuir、Freundlich、Temkin等方程对供试样品加入Zn2 后吸附BSM的数据进行了拟合,发现供试样品吸附苄嘧磺隆的等温曲线较好地符合Freundlich方程.加入Zn2 后,铁氧化物吸附苄嘧磺隆的量较未加Zn2 有较大幅度的增加,但在苄嘧磺隆的平衡质量浓度较低(＜4 mg/L)时,氧化物吸附苄嘧磺隆的量不随Zn2 浓度的增加而增加;在苄嘧磺隆的平衡质量浓度较高(＞6 mg/L)时,氧化物吸附苄嘧磺隆的量随Zn2 浓度的增加而增加.这可能是Zn2 和苄嘧磺隆被吸附时存在竞争和协同交互作用的结果.     

骆马湖泥-水界面磷铁硫原位同步变化特征

利用薄膜梯度扩散（DGT）原位采样装置获取了骆马湖全湖8个典型湖区泥-水界面（SWI）活性磷（P）、铁（Fe）、硫（S）垂向分布信息，据此定量估算三者交换通量.结果表明，骆马湖沉积物剖面P、Fe、S浓度范围分别为0~2.05，0~11.10和0.01~0.63mg/L，并在微小尺度呈高度空间异质性.在水平方向上活性P、Fe主要表现为西北湖区高于东南湖区，而活性S则未表现出明显的分布规律；就垂直剖面而言，活性P、Fe、S自界面向下呈升高趋势，并在60mm深度内出现峰值，且活性P和Fe剖面呈明显的同步变化特征；活性P、Fe在多数点位具有显著的正相关性（r>0.65，P<0.01），且各采样点沉积物中的总铁与总磷比值[w（∑Fe）/w（∑P）]均高于15，这表明Fe的地球化学循环过程对于骆马湖内源磷释放起重要控制作用；8个采样点样品中活性P、Fe、S交换通量分别为0.066~0.698，1.671~5.592和0.007~0.071mg/（m²·d），表明P、Fe、S由沉积物向水体释放.西北湖区表现出较高的P通量和活性P浓度，这可能会增加南水北调过程中水质污染的风险，应予以重视.以上结果支持了P、Fe耦合释放机制，明确了骆马湖SWI的活性P、Fe、S迁移特征.     

含铜黄连素废水的铁碳微电解预处理及铜回收研究

利用铁碳微电解技术对含铜黄连素制药废水进行预处理,通过单因素试验确定了反应时间,铁粉和废碳投加量,pH等因素对处理效果的影响,并设计了回收金属铜的工艺流程.结果表明:采用铁碳微电解工艺处理初始Cu2+浓度约为20000mg/L,黄连素浓度为1 700～1 900mg/L的含铜黄连素制药废水,当废水pH为2.0～3.0,...