利用铜矿尾砂研制低强度可控性填料

利用铜矿尾砂、粉煤灰、水泥以及加气剂等,混合搅拌成泥浆体,振动成型,制备出低强度可控性填料(CLSM).试验表明:以水泥12.9％、铜矿尾砂(细集料)22.6％、加气剂3.2％、粉煤灰12.9％等工业废弃物,加水48.4％,固液比控制在(14～15):(15～16)之间,制得的CLSM制品,抗压强度0.35～2.00 ...     

滇池蓝藻快速热解液化制取生物油的初步研究

文章采用实验室规模的固定床反应器作为实验平台,对蓝藻快速热解液化制取生物油的可行性进行了探讨,并对影响液化性能的诸多因素,如热解温度(300～700℃)、载气流量(0～400 mL/min)、原料粒径(d＜0.08 nn,0.15＜d＜0.25 mm,0.25＜d＜0.38 mm,0.38＜d＜3.35 mm,d＞3....     

土著微生物修复城市小型湖泊实验研究

利用生物制剂及生物修复技术对鞍山市英泽湖进行了净化治理.研究结果表明,经过8～30 d的生物净化,该湖水中的COD、植物营养元素浓度及浊度都有了大幅度的下降.其中COD降至20 mg/L以下,去除率达到70%以上;氨氮降至0.2 mg/L以下,去除率达97%;总磷降低至0.02 mg/L以下,去除率达到60%以上;浊度...     

稀土磁盘水处理方案技术经济比较

文章针对日照钢铁集团公司2150热轧水处理工程浊环水处理方案选择,对传统沉淀过滤法和先进的稀土磁盘法进行了对比和分析,稀土磁盘法在效果、占地、投资和运行维护费用上有较多优势,最终选用该工艺。     

吸附树脂负载铁酞菁催化降解硝基苯的研究

在可见光照射下,采用吸附树脂负载铁酞菁催化过氧化氢降解硝基苯.考察了光照、催化剂投加量、双氧水投加量、温度及pH值等因素对催化效果的影响.结果表明,在功率为50W卤钨灯照射下,硝基苯溶液初始质量浓度为200 mg/L,初始pH值为3,催化剂投加量为1.5 g/L,双氧水投加量为1.0 mL/L,温度为35℃下反应10h,硝基苯去除率可达到79.9％.     

聚硅酸对不同形态铝沉积行为的影响

针对给水管网中残余铝沉积和再溶解现象可能引起的水质问题,研究了聚硅酸对不同水解聚合形态铝沉积、再溶解的影响,并以石英微晶天平为表征手段,初步探讨了聚硅酸对不同形态铝沉积、再溶解过程影响的机理.结果表明,聚硅酸能显著改变不同水解聚合形态铝的沉积、再溶解行为.聚硅酸可与3种水解聚合形态的铝迅速结合而生成可沉积产物,但产物性质不同.以单体形态为主的Al_0与聚硅酸的反应产物性质较稳定,部分以溶解态存在,部分以非溶解态(可沉积态)存在;尽管铝的两种聚合形态Al_(13)和Al_(30)与聚硅酸反应也生成了部分可沉积产物,但随着时间的推移,这些产物又逐渐向溶解态转化.铝硅比对Al_0体系中铝的沉积溶解行为影响较小,而对Al_(13)和Al_(30)影响较大,且在0.2∶20(以Al和SiO_2计的质量比)时,沉积态铝的溶解速率最快.     

模拟水体硝态氮对黄菖蒲生长及其氮吸收的影响

为了对挺水植物在水环境与水生态修复中的应用提供参考依据,选取黄菖蒲(Iris pseudacorus L.)为对象,通过模拟水培实验,对比研究了6种水体硝态氮质量浓度(10.68、23.88、42.22、63.33、82.92、97.13 mg·L~(-1))下,黄菖蒲地上和地下生物量、根冠比、叶绿素含量、氮累计吸收量以及对硝态氮去除效果的差异,以期明确模拟水体硝态氮质量浓度对黄菖蒲生长及其氮吸收能力的影响.结果显示,首先,不同硝态氮质量浓度对黄菖蒲地上部分(茎叶)生长的影响大于地下部分(根);当硝态氮质量浓度为10.68 mg·L~(-1)时,黄菖蒲的根冠比增加;当硝态氮质量浓度为42.22~97.13 mg·L~(-1)时,黄菖蒲的根冠比减少.其次,黄菖蒲适宜生长的硝态氮质量浓度为23.88~63.33 mg·L~(-1);硝态氮质量浓度低于10.68 mg·L-1或高于82.92mg·L-1时,均会对黄菖蒲的叶绿素合成产生抑制作用.再次,黄菖蒲对氮的累积量随硝态氮质量浓度增加而增加,且地下部分对氮的累积能力优于地上部分;6种浓度下,单株黄菖蒲的氮累计吸收量为10.56~75.43 mg,其地下部分依次为地上部分的7.2、2.3、2.5、2.1、1.6以及1.5倍.此外,黄菖蒲对氮的利用效率与硝态氮质量浓度之间成显著的幂函数关系,且地上部分的氮利用效率高于地下部分.最后,黄菖蒲对硝态氮的去除率随硝态氮质量浓度增加而增加,6种浓度下黄菖蒲对硝态氮的去除率介于94.9%和99.3%之间,且水体中硝态氮质量浓度随时间延续呈指数函数降低.结果表明,黄菖蒲对硝态氮有很好的去除效果,但黄菖蒲的生长及其对氮的吸收与去除效率受水体硝态氮质量浓度影响显著,且地上部分较地下部分更为敏感.     

三峡库区(重庆-宜昌段)沉积物中钒的污染特征及生态风险评价

为全面了解三峡库区(重庆—宜昌段)干支流沉积物中钒的含量水平、空间分布、赋存形态、污染程度,在三峡库区采集水体沉积物样品67个,测定了沉积物中钒的含量及其化学赋存形态,并采用地积累指数法和潜在生态危害指数法进行分析和评价.结果表明:1三峡库区研究区范围内沉积物中钒的含量范围为89.4~175.2 mg·kg-1,平均值为123.7 mg·kg-1,略高于长江沉积物背景值;2库区沉积物中钒的空间分布特征主要呈现库区干流含量大于支流,干流下游沉积物中钒含量高于上游;3沉积物中钒含量的极值点出现在较发达县(区)附近,考虑其来源可能是人为源汇入;4库区沉积物中钒的赋存形态主要以残渣态为主,所占质量分数为80%~89%,并与总量呈现显著正相关关系;5沉积物中钒污染程度较小,潜在环境危害影响较弱.     

Effects of metal and acidic sites on the reaction by-products of butyl acetate oxidation over palladium-based catalysts

Catalytic oxidation is widely used in pollution control technology to remove volatile organic compounds. In this study, Pd/ZSM-5 catalysts with different Pd contents and acidic sites were prepared via the impregnation method. All the catalysts were characterized by means of N2 adsorption- desorption, X-ray fluorescence （XRF）, HE temperature programmed reduction （H2-TPR）, and NH3 temperature programmed desorption （NH3-TPD）. Their catalytic performance was investigated in the oxidation of butyl acetate experiments. The by-products of the reaction were collected in thermal desorption tubes and identified by gas chromatography/mass spectrometry. It was found that the increase of Pd content slightly changed the catalytic activity of butyl acetate oxidation according to the yield of CO2 achieved at 90%, but decreased the cracking by-products, whereas the enhancement of strong acidity over Pd-based catalysts enriched the by-product species. The butyl acetate oxidation process involves a series of reaction steps including protolysis, dehydrogenation, dehydration, cracking, and isomerization. Generally, butyl acetate was cracked to acetic acid and 2- methylpropene and the latter was an intermediate of the other by-products, and the oxidation routes of typical by-products were proposed. Trace amounts of 3-methylpentane, hexane, 2-methylpentane, pentane, and 2-methylbutane originated from iso4merization and protolysis reactions.     

Mo-modified Pd/Al2O3 catalysts for benzene catalytic combustion

Mo-modified Pd/Al2O3catalysts were prepared by an impregnation method and tested for the catalytic combustion of benzene. The catalysts were characterized by N2 isothermal adsorption, X-ray diffraction（XRD）, X-ray photoelectron spectroscopy（XPS）, temperatureprogrammed desorption of NH3（NH3-TPD）, H2temperature-programmed reduction（H2-TPR）, and high-angle annular dark-field scanning transmission electron microscopy（HAADF-STEM）. The results showed that the addition of Mo effectively improved the activity and stability of the Pd/Al2O3catalyst by increasing the dispersion of Pd active components, changing the partial oxidation state of palladium and increasing the oxygen species concentration on the surface of catalyst. In the case of the Pd-Mo/Al2O3catalyst,benzene conversion of 90% was obtained at temperatures as low as 190°C, which was 45°C lower than that for similar performance with the Pd/Al2O3catalyst. Moreover, the 1.0% Pd-5% Mo/Al2O3catalyst was more active than the 2.0% Pd/Al2O3catalyst. It was concluded that Pd and Mo have a synergistic effect in benzene catalytic combustion.