Nanoencapsulation of hexavalent chromium with nanoscale zero-valent iron: High resolution chemical mapping of the passivation layer

Solid phase reactions of Cr(Ⅵ) with Fe(0) were investigated with spherical-aberration-corrected scanning transmission electron microscopy(Cs-STEM) integrated with X-ray energy-dispersive spectroscopy(XEDS). Near-atomic resolution elemental mappings of Cr(Ⅵ)–Fe(0) reactions were acquired. Experimental results show that rate and extent of Cr(Ⅵ) encapsulation are strongly dependent on the initial concentration of Cr(Ⅵ) in solution. Low Cr loading in nZⅥ(1.0 wt%) promotes the electrochemical oxidation and continuous corrosion of n ZⅥ while high Cr loading(1.0 wt%) can quickly shut down the Cr uptake. With the progress of iron oxidation and dissolution, elements of Cr and O counter-diffuse into the nanoparticles and accumulate in the core region at low levels of Cr(Ⅵ)(e.g., 10 mg/L). Whereas the reacted n ZⅥ is quickly coated with a newly-formed layer of 2–4 nm in the presence of concentrated Cr(Ⅵ)(e.g., 100 mg/L). The passivation structure is stable over a wide range of pH unless pH is low enough to dissolve the passivation layer. X-ray photoelectron spectroscopy(XPS) depth profiling reconfirms that the composition of the newly-formed surface layer consists of Fe(Ⅲ)–Cr(Ⅲ)(oxy)hydroxides with Cr(Ⅵ) adsorbed on the outside surface. The insoluble and insulating Fe(Ⅲ)–Cr(Ⅲ)(oxy)hydroxide layer can completely cover the n ZⅥ surface above the critical Cr loading and shield the electron transfer. Thus, the fast passivation of nZⅥ in high Cr(Ⅵ) solution is detrimental to the performance of nZⅥ for Cr(Ⅵ) treatment and remediation.     

Morphology and electrical conductivity of PACS

ＩｎｔｒｏｄｕｃｔｉｏｎＰｏｌｙａｌｕｍｉｎｉｕｍｃｈｌｏｒｉｄｅ(ＰＡＣ) ,ａｋｉｎｄｏｆｉｎｏｒｇａｎｉｃｐｏｌｙｍｅｒｆｌｏｃｃｕｌａｎｔ,ｉｓｗｉｄｅｌｙｕｓｅｄｉｎｗａｔｅｒａｎｄｗａｓｔｅｗａｔｅｒｔｒｅａｔｍｅｎｔ.ＩｎｏｒｄｅｒｔｏｉｎｃｒｅａｓｅｔｈｅｃｏａｇｕｌａｔｉｏｎｅｆｆｅｃｔｏｆＰＡＣａｎｄｉｍｐｒｏｖｅｔｈｅｑｕａｌｉｔｙｏｆＰＡＣｐｒｏｄｕｃｔ,ｉｔｉｓｎｅｃｅｓｓａｒｙｔｏｒａｉｓｅｔｈｅｄｅｇｒｅｅｏｆｐｏｌｙｍｅｒｉｚａｔｉｏｎｏｆＰＡＣ .Ｇｅｎｅｒａｌｌｙ ,ｔ…     

不同生长期的Pseudomonas putida 5-x细胞对工业废水中Cu~(2+)的吸附

研究了不同生长阶段的Cu2 + 吸附细菌Pseudomonasputida 5 x对Cu2 + 的吸附容量 .结果表明在低硫培养基中 ,当P putida 5 x细胞生长刚进入对数生长期时 ,单位细胞对Cu2 + 的吸附溶量最低 .而当生长进入稳定生长期的后期或死亡期的早期时 ,单位细胞对Cu2 + 的吸附量最大 .实验结果还表明 ,高浓度的Cu2 + 对对数期细胞的吸附能力有一定的抑制 ,而对死亡期的细胞影响较小 .早期研究已证明细胞对重金属离子的吸附和细胞表面某些对重金属离子具有亲和性的功能基团 (如某些膜蛋白及羰基化合物 )有关 .利用透视电子显微镜观察了不同生长阶段的细胞表面结构及对铜离子的吸附效果 ,发现生长后期细胞表面吸附有较多的Cu2 + ,这表明生长后期的细胞表面可能含有较多的这类功能基团     

Impact of triazophos insecticide on paddy soil environment

ＩｎｔｒｏｄｕｃｔｉｏｎＲｉｃｅｉｓｔｈｅｓｔａｐｌｅｄｉｅｔａｒｏｕｎｄ 3 0 %ｏｆｔｈｅｗｏｒｌｄｐｏｐｕｌａｔｉｏｎａｎｄａｒｏｕｎｄ 60 %ｏｆｔｈｅＡｓｉａｎｐｏｐｕｌａｔｉｏｎ .Ｔｈｉｓｃｒｏｐｉｓｐｒｅｆｅｒｅｎｔｉａｌｌｙｏｒｇｅｎｅｒａｌｌｙｃｕｌｔｉｖａｔｅｄｕｎｄｅｒｓｕｂｍｅｒｇｅｄｓｏｉｌｃｏｎｄｉｔｉｏｎｓｆｏｒｒｅａｓｏｎｓｏｆｂｅｔｔｅｒｙｉｅｌｄｓａｎｄｔｏｐｏｇｒａｐｈｉｃａｌｓｉｔｕａｔｉｏｎｓ(Ｒｅｉｃｈａｒｄｔ,1 997) .Ｔｈｅｉｍｐｏｒｔａｎｃｅｏｆｓｏｉｌｍ…     

Stability analysis of alkaline nitrobenzene-containing wastewater by a catalyzed Fe-Cu treatment process

Iron and copper bimetallic system (catalyzed Fe-Cu process) is a promising technology for alkaline nitrobenzene-containing wastewater treatment. However, little is currently known about the changes of treatment efficiency with time going. This research investigated the long-term performance of the catalyzed Fe-Cu process to reduce nitrobenzene (NB) in alkaline wastewater. In addition, the changes of the metal surfaces morphologies and matters before and after the reaction were analyzed by scanning electron microscopy (SEM) in conjunction with energy-dispersion spectroscopy (EDS) and X-ray diffraction spectroscopy (XRD). The results showed that the surface properties of copper almost remained unchanged after weeks of operation, which spelled its strong chemical stability and resistance to poisoning. Moreover, the results indicated that there were two reasons for the treatment efficiency decreasing with time. One was the gradual iron element consumption due to corrosion. The other was iron reactivity weakened due to the precipitates accumulation on the surfaces that were mainly Fe₃O₄ and FeCO. __________ Translated from Environmental Pollution & Control, 2006, 28(10): 783–785 [译自: 环境污染与防治]     

烧结烟气应用电子束脱硫脱硝技术之利弊

介绍了电子束辐照烟气脱硫技术的原理、工艺流程、主要设备及其作用;中国工程物理研究院1.2万m^3/h电子束脱硫脱硝试验装置及试验结论;成都热电厂30万m^3/h脱硫示范装置的设计参数、运行情况;综合分析了烧结烟气脱硫应用电子束辐照烟气脱硫脱硝技术之利弊,认为烧结烟气脱硫应用电子束辐照烟气脱硫技术不失为一个可供选择且可行的技术.     

摩擦清洗修复铅污染土壤的参数优化及清洗效率评价

采用摩擦清洗法修复铅污染场地土壤,主要目的是将细颗粒和铅污染物从砂粒表面去除.通过正交实验优化清洗参数,并对3份不同铅含量土壤进行摩擦清洗实验.优化的清洗参数为:水土比70%干物质、温度25℃、搅拌时间30 min、搅拌速率1 200 r.mim-1.摩擦清洗前土壤经过筛分化验分析表明,3份土壤铅主要富集在砂粒和粉黏粒中;铅的分布与有机质有极大相关性.结果表明,经过摩擦清洗后,3份原状铅污染土壤砂粒的清洗效率分别为:67.61%、31.71%、41.01%,摩擦清洗从砂粒表面去除一部分细粒土壤和铅污染物,使铅浓缩至粉黏粒中;扫描电镜(SEM)分析表明,摩擦清洗后砂粒表面变光滑.以上结论说明摩擦清洗对于铅污染场地的砂粒土壤具有较好的清洗效果.     

电子供体对地下水中高氯酸盐生物去除的影响研究

通过静态实验,考察了电子供体类型及用量对厌氧条件下微生物去除地下水中高氯酸盐的影响.结果表明,电子供体醋酸盐和H₂的加入,可以明显提高ClO₄^-的去除率,驯化后的微生物去除ClO₄^-的速率比未加入电子供体时提高约1.4~3倍.Monod动态模型能很好地拟合两种电子供体环境下ClO₄^-的微生物去除过程,分别以醋酸盐和H₂作为电子供体时,基质半饱和常数K_s为12.6 mg·L^-1和2.2 mg·L^-1,最大比基质消耗速率V_m为0.45 d^-1和0.08 d^-1.动力学参数表明,本实验条件下,异养型混合菌去除ClO₄^-的效果明显优于自养型混合菌;在少数受高浓度ClO₄^-污染的地下水环境中,为了提高ClO₄^-的去除速率只有通过增加菌体浓度或提高微生物酶的活性来实现.随着电子供体醋酸盐用量增加,ClO₄^-的(比)消耗速率逐渐增大.当初始CH₃COO^-与ClO₄^-的比例为3.80 mg(COD)/mg(ClO₄^-)时,比消耗速率v最大(0.27 d^-1).     

浅析电子废弃物回收利用及危害解决办法

随着高科技的发展和人们需求的增长,电子产品不断推陈出新,电子废弃物成为世界上数量增长最快的垃圾."电子垃圾",主要包括各种使用后废弃的电脑、通信设备、电视机、电冰箱、洗衣机等电子电器产品.电子废弃物不规范回收处理易造成污染.电子废弃物中含有很多可回收再利用的有色金属、黑色金属、玻璃等物质.严格意义上讲,这些电子废弃物,不应称其为电子垃圾,而应称作电子旧货.伴随着电子工业的高速发展,电子废弃物污染不可避免地摆在了我们面前.电子废弃物具有危害性和可利用性.     

Groundwater contamination and natural attenuation capacity at a petroleum spilled facility in Korea

As a remedial option, the natural attenuation capacity of a petroleum contaminated groundwater at a military facility was examined. Hydrogeological conditions, such as high water level, permeable uppermost layer and frequent heavy rainfall, were favorable to natural attenuation at this site. The changes in the concentrations of electron acceptors and donors, as well as the relevant hydrochemical conditions, indicated the occurrence of aerobic respiration, denitrification, iron reduction, manganese reduction and sulfate reduction. The calculated BTEX expressed biodegradation capacity ranged between 20.52 and 33.67 mg/L, which appeared effective for the reduction of the contaminants levels. The contribution of each electron accepting process to the total biodegradation was in the order: denitrification > iron reduction > sulfate reduction > aerobic respiration > manganese reduction. The BTEX and benzene point attenuation rates were 0.0058-0.0064 and 0.0005-0.0032 day^-1, respectively, and the remediation time was 0.7-1.2 and 2.5-30 years, respectively. The BTEX and benzene bulk attenuation rates were 8.69 × 10^-4 and 1.05 × 10^-3 day^-1, respectively, and the remediation times for BTEX and benzene were 7.2 and 17.5 years, respectively. However, most of the natural attenuation occurring in this site can be attributed to dilution and dispersion. Consequently, the biodegradation and natural attenuation capacities were good enough to lower the contaminants levels, but their rates appeared to be insufficient to reach the remediation goal within a reasonable time frame. Therefore, some active remedial measures would be required.