荷电超滤膜对天然有机物去除及膜污染行为的影响

以Aldrich 腐殖酸溶液为水样,研究比较了溶液环境(pH值、离子强度和钙离子)对荷电改性再生纤维素超滤膜和传统中性未改性再生纤维素超滤膜过滤过程的影响.结果表明, ①pH值主要通过质子化作用影响荷电膜以及腐殖酸分子的荷电量,进而影响荷电超滤过程.溶液pH值从7.5下降到3.5时,荷电超滤膜对腐殖酸的截留率从92%减少到79%,超滤4 h时,膜通量下降从26%增加到36%.②离子强度的改变是通过影响腐殖酸分子的物化性质和静电屏蔽作用来影响超滤过程的.当溶液离子强度为0、 3和100 mmol/L时,初始截留率依次降低,分别为92%、 87%和48%,超滤4 h时,荷电超滤膜的通量下降依次增加,分别为26%、 35%和63%.③Ca2+浓度的影响,需要综合考虑静电屏蔽作用、Ca2+的架桥作用以及滤饼层的压实性等各方面的影响.④pH值、离子强度和钙离子对中性超滤膜过滤行为的影响趋势与荷电超滤膜相似,但其影响程度有着较大的差别.研究结果对荷电超滤膜技术在实际应用中选择合适环境条件提供了参考.     

腐殖酸及酸雨对贫铀在土壤中迁移的影响研究

 利用经过完善的贫铀迁移模型,研究腐殖酸(HA)及酸雨对贫铀在土壤中迁移的影响.结果表明,对照组(北京地区土壤)DU迁移到达9~11cm,分别添加2%、5%、10%HA的实验组DU迁移依次降低,分别为21~23cm、15~17cm、11~13cm,说明腐殖酸促进了DU迁移; pH值为4.0和3.0的模拟酸雨,分别使贫铀迁移至29~31cm及35cm以上,说明酸雨促进了贫铀迁移;在酸雨和腐殖酸综合作用下贫铀迁移仅到5~7cm,说明腐殖酸和酸雨综合作用抑制了贫铀迁移.     

Effects of Cu（Ⅱ） and humic acid on atrazine photodegradation

This work was designed to explore the characteristics of photodegradation of herbicides in the copper-polluted water body. The results showed that Cu(II) alone could induce a photo Fenton-like reaction to enhance the degradation of atrazine, in which hydroxyl radical ( OH) was a main active species. Humic acids restrained atrazine degradation, nevertheless, when introducing Cu(II), the photodegradation was accelerated, in which singlet oxygen (1O2) replaced OH acting as the prevailing species. A feasible mechanism for the photochemical process was also proposed, which is helpful for better understanding the environmental photochemistry of atrazine in the copper-polluted water.     

Evaluation of adsorption capacities of humic acids extracted from Algerian soil on polyaniline for application to remove pollutants such as Cd(Ⅱ), Zn(Ⅱ) and Ni(Ⅱ) and characterization with cavity microelectrode

The adsorption capacities of new humic acids isolated from Yakouren forest (YHA) and Sahara (Tamenrasset: THA) soils (Algeria) and commercial humic acid (PFHA) on polyaniline emeraldine base (PEB) were studied at pH 6.6. Also the adsorption of heavy metals such as Cd2+, Zn2+ and Ni2+ on humic acid-polyaniline systems (HA-PEB) was investigated at the same conditions. HA-PEB compounds were characterized by scanning electron microscopy (SEM), infrared spectrometry and cavity microelectrode. In addition, batch adsorption and cavity microelectrode were used in the adsorption study of Cd2+, Zn2+ and Ni2+ on HA-PEB. To develop biocaptors of polluting metals using a cavity microelectrode modified by HA-PEB systems, the adsorption kinetic and adsorption capacity were investigated. The SEM analysis showed that the presence of humic acid affected the PEB surface and caused the formation of a granular morphology. The maximum adsorption capacities (qmax) of PFHA, THA and YHA determined by adsorption isotherms were 91.31, 132.1 and 151.0 mg/g, respectively. Batch adsorption results showed that qmax of Cd2+, Zn2+ and Ni2+ on HA-PEB followed the order: THA-PEB > YHA-PEB > PFHA-PEB. The voltammograms obtained with HA-PEB modified cavity microelectrode showed the appearance of new redox couples reflecting the adsorption of HA on PEB. Metal-humic acid-polyaniline voltammograms were characterized by appearance of oxidation-reduction couples or reduction wave corresponding to metal. Finally, the result may be exploited to develop a biocaptor based on the cavity microelectrode amended by THA-PEB and YHA-PEB.     

Efficacy of natural biocide on control of microbial induced corrosion in oil pipelines mediated by Desulfovibrio vulgaris and Desulfovibrio gigas

We compared the efficacy of a natural biocide with four chemical tetrakishydroxymethyl phosphonium sulfonate, benzyl trimethyl ammonium chloride, and formaldehyde, glutaraldehyde, to control microbial induced corrosion in oil pipelines. The efficacy of biocides were monitored against Desulfovibrio vulgaris and Desulfovibrio gigas in experimental pipes by measuring cell counts, H2S production, Fe(II) production, production of extracellular polymeric substances and structure of biofilm. The treatment with cow urine had minimum planktonic cell counts of 3 102 CFU/mL as well as biofilm cell counts of 9 101 CFU/mL as compared with tetrakishydroxyl methyl phosphonium sulfonate, benzyl trimethyl ammonium chloride, formaldehyde and glutaraldehyde. Sulfide production was the lowest with cow urine (0.08 mmol/L), followed by tetrakishydroxymethyl phosphonium sulfonate 0.72 mmol/L. On day 90 of treatment, Fe(II) production was also found to be the lowest with cow urine. The scanning electron microscopic studies indicated that the biofilm bacteria were killed by cow urine. These results demonstrate the cow urine mediated control of microbially induced corrosion, and this is indicative of its potential as a viable substitute of toxic biocides. To the best of our knowledge, this seems to be the first report which screens possible biocidal activity by cow urine as compared to the most common biocides which oil industry is currently using.     

不同含磷物质对重金属污染土壤-水稻系统中重金属迁移的影响

通过水稻盆栽试验研究磷酸氢二钠(DSP)和羟基磷灰石(HAP)对污染土壤中重金属(Pb、Cd、Zn)向水稻迁移的影响.结果表明,①DSP和HAP都显著提高了土壤pH值和有效磷含量(p0.05),降低了土壤中Pb、Cd、Zn交换态含量,且HAP降低重金属交换态的效果较DSP好.水稻地上部分重金属含量与土壤中重金属交换态含量呈明显正相关关系,说明DSP和HAP通过降低土壤中重金属交换态含量从而达到减少重金属向水稻中迁移的目的.②DSP和HAP明显降低了水稻各器官Pb、Cd的含量,同时使水稻根、壳、糙米中Zn含量降低,但增加了茎叶中Zn的含量.与对照相比,DSP和HAP分别使糙米中Pb、Cd、Zn最大降低了48.72%、22.22%、25.35%和62.82%、66.67%、39.88%,但是糙米中Pb、Cd含量仍未达到食品卫生标准限值(GB2762—2012).③DSP和HAP处理都使水稻根干重逐渐减少,使茎叶、壳、糙米干重先增加后降低,在0.12 g·kg-1时使水稻糙米产量最大.综上,DSP和HAP都能有效控制土壤中Pb、Cd、Zn向水稻中迁移,且HAP效果比DSP好,但磷添加量不宜过高.     

胞外聚合物磷酸盐形态对生物除磷过程的影响研究

以不同DO条件下污泥龄(SRT)分别为10 d和30 d的两组实验室A/O-SBR反应器活性污泥为研究对象,探讨了胞外聚合物(EPS)磷酸盐形态对生物除磷过程的影响.结果表明,污泥絮体中的磷主要分布于EPS中,PO3-4-P和聚磷酸盐(Poly-P,包括低分子量聚磷酸盐LMW PolyP和高分子量聚磷酸盐HMW Poly-P)是EPS磷的主要形态;EPS对生物除磷的影响明显大于细菌细胞,EPS磷的厌氧降低量和好氧升高量为胞内磷变化量的2.8~6.4倍.EPS中的LMW Poly-P和HMW Poly-P含量均表现厌氧降低和好氧升高的变化规律;对于相同SRT的污泥,中DO(2.5~3.5 mg·L-1)条件较低DO(0.7~1.0 mg·L-1)条件下EPS的LMW Poly-P和HMW Poly-P有更大的厌氧降低量和好氧升高量,对应着更明显的生物除磷过程,说明EPS不仅是生物除磷过程的中转站,而且参与了生物聚磷过程.     

Fe-Ce/GAC催化臭氧降解高浓度腐殖酸废水

采用浸渍焙烧法制备了Fe-Ce/GAC催化剂,并用于催化臭氧降解模拟高浓度腐殖酸废水.以废水COD、腐殖酸浓度为考察指标,研究了Fe-Ce/GAC催化剂的前驱体无机铁盐种类、焙烧温度、铁盐浓度、助剂稀土元素种类及浓度、分散剂硝酸钾浓度等不同制备条件对催化臭氧降解腐殖酸的效果.试验表明,在腐殖酸浓度为3.00 g·L~(-1)、pH值约8.0、温度为25℃、臭氧投量为1.24 g·h~(-1),反应40 min后COD、腐殖酸去除率仅为17.1%、43.0%;添加以2.0%硝酸铁、1.5%硝酸铈、1.0%硝酸钾溶液浸渍,经350℃焙烧3 h后制备的Fe-Ce/GAC催化剂,可使COD、腐殖酸去除率分别提高40.3%、31.8%.且Fe-Ce/GAC催化剂具有较好的稳定性,重复使用5次后,COD、腐殖酸去除率仅小幅降低了4.2%、9.1%.SEM图象显示活性炭经改性后,比表面积明显增大,有利于活性物质的负载;EDS分析表明催化剂负载了大量的Fe、Ce等金属物质;XRD图谱显示催化剂含有Fe_2O_3、CeO_2等多种活性物质.Fe-Ce/GAC催化臭氧的机理可解释为:活性成分氧化铁在催化过程中生成的羟基氧化铁会促进羟基自由基的生成,而铈元素在催化过程中不仅会提高催化剂的活性,而且生成的化学吸附氧可促进对有机物的吸附及氧化.     

掺杂聚乙烯醇的壳聚糖小球对铜离子-腐殖酸的单一和连续吸附行为

以三聚磷酸钠作为离子交联剂,合成了一种掺杂聚乙烯醇的壳聚糖小球,采用SEM和FTIR表征了小球的表面性能及官能团分布情况,进一步研究了这种小球对腐殖酸和铜离子的单独吸附行为、连续吸附行为及两者共存状态下的吸附行为,并通过XPS能谱分析了吸附过程的机理.结果表明:在单独吸附过程中,壳聚糖小球与腐殖酸和铜的作用方式主要是通过静电引力和络合作用;在连续吸附过程中,先吸附了腐殖酸的小球,后续对铜离子的吸附效果变弱;而先吸附了铜离子的小球,后续对腐殖酸的吸附能力变强,说明这种小球在吸附过程中可以被连续使用.而在腐殖酸和铜离子共存的吸附实验中发现,壳聚糖小球除了会吸附溶液中的铜离子和腐殖酸外,还导致它们的聚集沉降.     

电子束辐照降解水中氯霉素的研究

本研究对氯霉素(CAP)在不同条件下的电子束辐照降解进行了研究.结果表明,电子束辐照可有效去除水中CAP,低浓度CAP在酸性条件下的辐照降解更为显著,且降解过程符合准一级动力学模型.通过添加不同的自由基清除剂,发现HO·在CAP降解中起关键作用,此外,CAP分子也会吸收辐照而发生分解.水中共存的阴离子和腐殖酸(HA)对CAP辐照降解均有抑制作用,这跟其与HO·的反应速率常数大小有关,并且反应速率越大,其抑制能力越强.CAP在去离子水中的去除率高于其他实际水体,但辐照剂量为4 k Gy时,污水厂污水过滤水和胶体浓缩液中的CAP也可分别去除89.1%和81.7%.利用GC-MS检测到辐照后溶液中有6种中间产物,主要是通过脱水、不对称中心断键和脱酰胺作用形成.此外,IC检测有Cl-、NO-3和NO-2的产生,并且TOC在一定程度上降低,说明部分CAP被矿化.