Enhanced adsorption of phosphate by loading nanosized ferric oxyhydroxide on anion resin

Ferric oxyhydroxide loaded anion exchanger （FOAE） hybrid adsorbent was prepared by loading nanosized ferric oxyhydroxide （FO） on anion exchanger resin for the removal of phosphate from wastewater. TEM and XRD analysis confirmed the existence of FO on FOAE. After FO loading, the adsorption capacity of the hybrid adsorbent increased from 38.70 to 51.52mg.g-1. Adsorption processes for both FOAE and anion resin were better fit to the pseudo first order model. Batch adsorption experiments revealed that higher temperature （313K）, higher initial phosphate concentration （50 mg.L-1） and lower solution pH （pH value of 2） would be more propitious to phosphate adsorption. Competition effect of coexisting anions on phosphate removal can be concluded as sulfate 〉 nitrate 〉 chloride. Freundlich isotherm model can describe the adsorption of phosphate on FOAE more accurately, which indicated the heterogeneous adsorption occurred on the inner-surface of FOAE.     

根表铁膜的形成和添加硒对水稻吸收转运无机汞和甲基汞的影响

为了研究根表铁膜和硒对水稻吸收、转运不同形态的汞的影响,用Fe2+溶液诱导根表形成铁膜后,将水稻植株分别暴露于无机汞(Hg Cl2)、甲基汞(Me Hg Cl)、无机汞和亚硒酸钠(Hg Cl2+Na2Se O3)混合溶液、甲基汞和亚硒酸钠(Me Hg Cl+Na2Se O3)混合溶液的培养液中继续培养72 h。用DCB(dithionite-citrate-bicarbonate)提取根表铁膜,并用电感耦合等离子体质谱(ICP-MS)测定DCB溶液中Fe、Hg含量及水稻根、茎叶中Hg含量。结果表明:水稻根表铁膜对Me Hg Cl和Hg Cl2均有吸附,对Me Hg Cl的吸附作用高于Hg Cl2。根表铁膜的形成显著降低了汞暴露水稻根、茎叶中汞的含量;铁膜的形成也显著降低了Hg Cl2和Me Hg Cl从水稻根部到茎叶部分的转运效率。硒的存在可增加铁膜对Hg Cl2和Me Hg Cl的吸附,降低水稻对Hg Cl2和Me Hg Cl的吸收和转运。研究结果表明:根表铁膜和硒单独或联合作用能显著抑制水稻对无机汞和甲基汞的吸收和转运,进而可以减少汞在稻米中的蓄积。研究的开展对于提高汞污染区稻米的质量和保证粮食安全具有一定的现实意义。     

Cation exchange resin supported nanoscale zero-valent iron for removal of phosphorus in rainwater runoff

Self-made cation exchange resin supported nanoscale zero-valent iron （R-nZVI） was used to remove phosphorus in rainwater runoff. 80% of phosphorus in rainwater runoff from grassland was removed with an initial concentration of 0.72 mg. L-1 phosphorus when the dosage of R-nZVl is 8 g per liter rainwater, while only 26% of phosphorus was removed when using cation exchange resin without supported nanoscale zero-valent iron under the same condition. The adsorption capacity of R-nZVI increased up to 185 times of that of the cation exchange resin at a saturated equilibrium phosphorous concentration of 0.42 mg. L-1. Various techniques were implemented to characterize the R-nZVI and explore the mechanism of its removal of phosphate. Scanning electron microscopy （SEM） indicated that new crystal had been formed on the surface of R-nZVI. The result from inductive coupled plasma （ICP） indicated that 2.1% of nZVI was loaded on the support material. The specific surface area was increased after the load of nanoscale zero-valent iron （nZVI）, according to the measurement of BET-N2 method. The result of specific surface area analysis also proved that phosphorus was removed mainly through chemical adsorption process. X-ray photoelectron spectroscopy （XPS） analysis showed that the new product obtained from chemical reaction between phosphate and iron was ferrous phosphate.     

Using crosslinked polyvinyl alcohol polymer membrane as a separator in the microbial fuel cell

Separator between anode and cathode is an essential part of the microbial fuel cell （MFC） and its property could significantly influence the system perfor- mance. In this study we used polyvinyl alcohol （PVA） polymer membrane crosslinked with sulfosuccinic acid （SSA） as a new separator for the MFC. The highest power density of 7594-4 mW-m-2 was obtained when MFC using the PVA membrane crosslinked with 15% of SSA due to its desirable proton conductivity （5.16 x 10-2 S.cml）. The power density significantly increased to 11064- 30 mW.m-2 with a separator-electrode-assembly config- uration, which was comparable with glass fiber （11704- 46 mW.m-2）. The coulombic efficiencies of the MFCs with crosslinked PVA membranes ranged from 36.3% to 45.7% at a fix external resistance of lO00f2. The crosslinked PVA membrane could be a promising alter- native to separator materials for constructing practical MFC system.     

石板楼盖后浇内圈梁与石墙界面受力性能试验

针对石结构中石板楼盖整体性差及支撑长度不足等抗震薄弱环节,提出在石楼板底部周边沿承重石墙增设内圈梁的加固方法。制作了6个在条石侧面后浇混凝土内圈梁的试件单元,通过在内圈梁上施加偏心荷载,以研究植入U型锚固筋的用量、U型锚固筋表面特征和偏心距对内圈梁的破坏形态及抗剪承载力的影响。试验结果表明:(1)增加U型锚固筋的用量可以有效提高内圈梁的抗剪承载力;(2)采用带肋锚固筋的内圈梁的抗剪承载力比采用光圆锚固筋的内圈梁的抗剪承载力高;(3)内圈梁抗剪承载力随偏心距的减小而增大。在对试验结果和受力机理分析的基础上,提出了内圈梁抗剪承载力计算公式。研究结果可为石板楼盖加固提供参考。     

制备斜发沸石和零价铁复合材料处理水中的六价铬污染

为了更好地降低我国地下水中六价铬污染给公众的健康带来的危害,本研究以渗透反应墙为处理地下水六价铬污染的主要方法,沸石和零价铁为反应材料,结合沸石虽价格低廉,但经长时间运行后吸附的六价铬有可能发生解吸,零价铁虽能完全去除六价铬但成本很高的特点,研发出了斜发沸石和零价铁的复合材料,以作为渗透反应墙的填充材料.研发主要分三个步骤:1)遴选出吸附效果较好的斜发沸石;2)确定最优表面活性剂及最优施用浓度;3)确定沸石与零价铁的复合工艺方法.最终方案为斜发沸石、六烷基三甲基溴化铵、还原铁粉、斜发沸石粉和超纯水按比例均匀混合后加热至90℃.由此制得的复合材料,具有良好的反应性能和便于装填的形状,生产成本也比较低廉,可以作为修复六价铬污染的反应墙填充材料.     

新型生物电Fenton法降解偶氮染料：铁复合碳毡阴极研究

传统电Fenton反应通过电化学方法产生H2O2,需外加电源,能耗大,成本高。基于MFC持续产电并可驱动阴极电Fenton系统运行的特点,本研究以铁复合碳毡为阴极电极,构建了微生物燃料电池驱动的生物电Fenton系统,探讨了铁复合碳毡及阴极pH对偶氮染料(金橙I号)脱色的影响。结果发现,铁复合碳毡脱色效果均好于普通碳毡。当pH为3时,4 h后Fe@Fe2O3/CF阴极脱色率达91.7%,明显高于α-FeOOH/CF和FeAlSi/CF的83.4%和69.9%。扫描电镜发现,Fe@Fe2O3以微粒状结构附着于碳毡表面,比表面积增大,可能是Fe@Fe2O3/CF脱色性能改善的主要原因。研究表明,低pH有利于生物电Fenton反应的进行。当pH由3.0提高至5.0时,Fe@Fe2O3/CF阴极脱色率降低至47.1%。阴极室染料脱色与阳极室废水TOC削减呈线性相关,说明阳极生物氧化是驱动阴极生物电Fenton反应的原动力。本研究提供了一种能自我维持、无需外源电力的生物电Fenton系统,为印染废水脱色提供了崭新的途径。     

砷-铅交互作用对水稻根表铁膜富集及根系吸收砷铅的影响

采用土-砂联合培养方法诱导水稻根表自然形成铁氧化物膜,研究了As-Pb交互作用对水稻根表铁膜吸附砷铅及根系吸收As和Pb的影响.结果表明,As和Pb的添加显著地影响水稻根表铁膜对As和Pb的吸附,并且As-Pb交互作用显著地影响水稻根系对两元素的吸收及根表铁膜对As的吸附.添加Pb可促进水稻根系对As的吸收.当As浓度为25μmol.L-1时,浓度为25μmol.L-1Pb处理与对照相比导致水稻根系吸收As提高了53.3%.同样,施用As也可以促进水稻根系对Pb的吸收,当Pb的浓度为25μmol.L-1和50μmol.L-1时,50μmol.L-1As处理与对照相比,水稻根系吸收Pb分别提高20.2%和28.6%.添加As显著地促进Pb由铁膜向根系中转运,而添加Pb对As由铁膜向根系中的转运影响不大.因此,在重金属复合污染情况下,水稻根表铁膜对重金属的吸附及根系对重金属的吸收均存在着复杂的交互作用.     

双酚A对小鼠肝脏和肾脏细胞的氧化损伤

为探究双酚A(BPA)的氧化毒性,分别以剂量为20、40和80mg·kg~(-1)·d~(-1)的BPA对雄性昆明小鼠灌胃处理1周,并测定了小鼠体内活性氧自由基(ROS)水平、还原型谷胱甘肽(GSH)含量、丙二醛(MDA)含量和DNA-蛋白质交联系数(DPC)。与对照组相比,各BPA暴露组小鼠肝脏和肾脏细胞中的ROS生成量、MDA含量和DPC系数均升高,而GSH含量下降(P<0.05或P<0.01)。ROS生成量、GSH含量和DPC系数均显示出剂量-效应关系。研究表明,BPA可扰乱小鼠肝脏和肾脏细胞的氧化应激平衡,诱导细胞氧化损伤。     

粒状铁与甲醇支持的生物-化学联用法去除富氧地下水中硝酸盐

针对富氧地下水中硝酸盐,采用粒状铁和甲醇支持的生物-化学联用法开展了批实验研究,优化了脱氮反应参数,初步探讨了脱氧脱氮的能力及途径。结果表明,该法的优化参数是粒状铁种类为GI-北京,m（粒状铁）∶m（水）为3∶800,粒状铁粒径为0.425~1.0 mm,反应时间为5 d,甲醇用量为210.59 mg.L-1。生物-化学法、粒状铁和好氧异养菌完全脱氧所需的时间分别是174、206和2 746 min。生物-化学法脱氧依赖于粒状铁化学还原和好氧异养菌有氧呼吸,并且前者起着关键作用。随着反应时间的增加,异养脱氮、自养脱氮和化学还原各自引起的NO3-去除率亦增加。当反应时间≤5 d时,自养脱氮和化学还原的去除率均〈10%,而当反应时间为5 d时,生物-化学法的NO3-去除率达到近100%。生物-化学法内存在异养脱氮、自养脱氮和化学还原3种脱氮途径,其中异养脱氮是最主要的途径,且三者存在共生、协同和促进作用。生物-化学法脱氮期间硝酸盐还原速率≥亚硝酸盐还原速率。生物-化学法去除地下水中硝酸盐是有效可行的。