过渡金属催化剂对邻二氯苯的催化氧化研究

以过渡金属的氧化物制得催化剂系列 ,研究其对邻二氯苯的氧化活性 ,考察反应温度、催化剂负载量、空间速度对氧化过程的影响 ,过渡金属氧化物对邻二氯苯的氧化活性顺序为 :CrOx>CuOx >VOx >MnOx >MoOx。 5wt.%V 1 0wt.%Mo3wt.%Mn/Al2 O3催化剂在 350℃时对邻二氯苯转换率达到了 90 %以上。     

关于多氯联苯测定的探讨

对PCB测定中所使用的Aroclor和单体标准品的区别、联系和使用进行了分析阐述,并对PCB测定中的气相色谱法、气相色谱质谱联用法、生物分析法、免疫分析法的优点、局限性进行了比较.对今后的PCB的测定提出了建议。     

Evaluation of the technoeconomic feasibility of electrochemical hydrogen peroxide production for decentralized water treatment

• Gas diffusion electrode (GDE) is a suitable setup for practical water treatment. • Electrochemical H₂O₂ production is an economically competitive technology. • High current efficiency of H₂O₂ production was obtained with GDE at 5–400 mA/cm². • GDE maintained high stability for H₂O₂ production for ~1000 h. • Electro-generation of H₂O₂ enhances ibuprofen removal in an E-peroxone process. This study evaluated the feasibility of electrochemical hydrogen peroxide (H₂O₂) production with gas diffusion electrode (GDE) for decentralized water treatment. Carbon black-polytetrafluoroethylene GDEs were prepared and tested in a continuous flow electrochemical cell for H₂O₂ production from oxygen reduction. Results showed that because of the effective oxygen transfer in GDEs, the electrode maintained high apparent current efficiencies (ACEs,>80%) for H₂O₂ production over a wide current density range of 5–400 mA/cm², and H₂O₂ production rates as high as ~202 mg/h/cm² could be obtained. Long-term stability test showed that the GDE maintained high ACEs (>85%) and low energy consumption (<10 kWh/kg H₂O₂) for H₂O₂ production for 42 d (~1000 h). However, the ACEs then decreased to ~70% in the following 4 days because water flooding of GDE pores considerably impeded oxygen transport at the late stage of the trial. Based on an electrode lifetime of 46 days, the overall cost for H₂O₂ production was estimated to be ~0.88 $/kg H₂O₂, including an electricity cost of 0.61 $/kg and an electrode capital cost of 0.27 $/kg. With a 9 cm² GDE and 40 mA/cm² current density, ~2–4 mg/L of H₂O₂ could be produced on site for the electro-peroxone treatment of a 1.2 m³/d groundwater flow, which considerably enhanced ibuprofen abatement compared with ozonation alone (~43%–59% vs. 7%). These findings suggest that electrochemical H₂O₂ production with GDEs holds great promise for the development of compact treatment technologies for decentralized water treatment at a household and community level.     

新型生物脱氮技术的工艺研究

以上流式厌氧污泥床反应器（ Ｕ Ａ Ｓ Ｂ） 作为厌氧氨氧化（ａｎａｍ ｍｏｘ） 反应器,用无机盐培养液完成了反应器的启动,并稳态运行ａｎａｍ ｍｏｘ 反应器．采用生物膜反应器作为生物硝化反应器,以无机盐培养液完成反应器的启动．将硝化反应器和ａｎａｍｍｏｘ 反应器组合在一起构成新型生物脱氮系统,以硝化反应器的出水作为ａｎａｍｍｏｘ反应器的进水,同时补充相应数量的 Ｎ Ｈ４ ＋ Ｎ．整个系统的总氮容积去除率可达１ ５７７ ｍｇ Ｌ－ １ ｄ － １ ．该新型生物脱氮系统能同时去除 Ｎ Ｈ４ ＋ Ｎ 和 Ｎ Ｏ Ｘ－ Ｎ,并且对高浓度的 Ｎ Ｈ４ ＋ Ｎ 去除具有较大的潜力．     

Seaweed sex pheromones and their degradation products frequently suppress amphipod feeding but rarely suppress sea urchin feeding

Summary. A diverse group of brown seaweeds produce bouquets of C₁₁ metabolites, some of which act as pheromones that cue gamete release or attract sperm to eggs following release. We demonstrate that these C₁₁ metabolites and their degradation products also frequently and strongly deter feeding by the herbivorous amphipod Ampithoe longimana, but rarely by the herbivorous sea urchin Arbacia punctulata. Across the range of concentrations tested, seven of twelve C₁₁ metabolites or mixtures that we tested deterred feeding by the amphipod, but only two of eleven deterred the sea urchin. For those compounds where we could rigorously contrast the magnitude of deterrence against the amphipod with the magnitude of deterrence against the urchin, the amphipod was deterred significantly more than the urchin by five of six metabolites. Thus, C₁₁ compounds were more frequently and more strongly deterrent to the amphipod than to the sea urchin. These findings for C₁₁ metabolites conflict with previous investigations, where other classes of seaweed chemical defenses have been shown to deter feeding by large mobile herbivores like urchins and fishes but to be relatively ineffective against mesograzers, especially the species of amphipod that we used here. Our results suggest that C₁₁ metabolites are unusual among the known seaweed chemical defenses in that they are especially effective against mesograzers, which often consume seaweed spores, zygotes, and juveniles. The high concentrations of C₁₁ metabolites in brown algal eggs could allow these defenses to be especially important in defending gametes, zygotes, or young sporelings from herbivorous mesograzers. Received 26 February 1998; accepted 9 April 1998.     

衍生化气相色谱法测定黄磷诱发氧化水中苯酚降解产物

利用衍生化气相色谱法对黄磷诱发氧化苯酚降解产物进行了研究，在磷酸存在下，以甲醇作酯类衍行生试剂，分别和ＳＥ－５２和ＨＰ－１７石英毛细管双柱结合ＧＣ－ＭＳ进行分离定性定量，黄磷诱发氧化苯酚降解产物以羧酸为主，在反应温度５０℃时，表现为一级反应特征，速率常数（Ｋ）：０．０７７ｍｉｎ＾－１，半衰期（ｔ１／２）：９．０ｍｉｎ。     

响应面法分析Fenton氧化处理采油废水的过程

采用Fenton氧化对采油废水进行研究,选取双氧水与二价铁离子的摩尔比、初始pH值和反应时间为自变量,以废水的COD去除率为响应值,通过Box-Behnken设计方法进行实验设计,进行了3因素3水平共15个实验点的实验。使用响应面分析法对实验结果进行模拟及分析,建立了响应值与3个自变量的二次多项式方程模型。Fenton氧化的优化工艺条件:n(H2O2):n(Fe2+)=0.8,pH=3.0以及反应时间60 min。在该优化条件下,废水的COD去除率可达72.8%,经实验验证,实际值与模型预测值拟合性好,偏差仅为0.5%。实验结果证实了该模型分析采油废水处理运行参数的准确性。优化工艺后的处理水质COD值完全满足油田废水达标排放的要求。通过总离子色谱图和质谱检索分析原油中的成分变化情况,证实Fenton方法对原油组分的降解效果。     

硫酸盐生物还原过程中涉硫组分代谢特性

通过硫酸盐生化代谢过程中涉硫组分（SO42-、SO32-、H2S、S2-、S2O32-、微生物含硫）等代谢特性模式研究,揭示了代谢过程中的主要限速步骤及过程代谢产物演替规律。SRB还原过程中限速步骤主要为亚硫酸根转化为硫化氢的过程,利用氮气吹脱硫化氢后,反应终点时各涉硫组分占总硫的51.38%,硫离子的量增加了2.09倍,硫酸根的去除率从83.5%提高到91.24%,亚硫酸根浓度呈现出降低的趋势;pH明显上升,并最终达到8.31,而无吹脱硫化氢的反应器最终pH为6.87。反应器中脱硫弧菌为优势菌,硫化氢被吹脱后,微生物在目、科、属水平上优势菌得到提高,硫化氢的存在抑制了优势菌的增殖。     

电解氧化法处理黄金冶炼厂选冶废水

采用电解氧化法处理同时含有高浓度氰化物与COD的黄金冶炼厂选冶废水,主要考查了外加电压、溶液pH、电解时间及极板间距等因素对氰化物和COD去除率的影响,充分利用原水中Cl^-的阳极氧化效应,深入探讨了电化学氧化过程及污染物氧化去除机理。结果表明,随着外加电压和电解时间的增大,氰化物和COD去除率逐渐增大。以石墨为阳极,钛合金为阴极,采用一阴两阳电解体系对废水进行氧化,当电压为4.5 V、初始pH为7、电解时间为3 h、极板间距为1.5 cm的条件下,总氰化物 (CN_T) 、COD、SCN^-及Cu的去除率最高可达99.6%、96%、99.9%与99.2%。电解过程中体系pH逐渐降低,电场作用下定向迁移至阳极附近的污染物去除主要归因于HClO及ClO^-的间接氧化作用,当pH大于5.0时以HClO的氧化为主,ClO^-的氧化为辅,而pH小于5.0时则主要是HClO的氧化。电解氧化过程中约有36.17%的Cu与SCN^-形成CuSCN沉淀而被除去,剩余的铜则扩散至阴极沉积析出。GC-MS分析表明,烷烃类、酯类、酮类等大分子的C=C键、酯基、羰基等化学键和官能团被氧化断链成小分子物质,随后继续被氧化为H₂O、CO₂和N₂。     

贵金属催化剂活性组分分布对催化湿式氧化处理非达霉素提炼废水的影响

采用均匀型和蛋白型Ru/TiO₂催化剂为湿式氧化催化剂,应用于催化湿式氧化非达霉素提炼废水,以出水COD和TOC去除率作为指标来评价2种催化剂的催化活性差异;采用实验室连续评价装置对柱状颗粒催化剂在不同pH、不同废水流量和不同温度下处理非达霉素提炼废水进行了优化评价。结果表明：在265 ℃、pH=4.1、废水流量为10 mL·h⁻¹时,催化剂的催化活性最高,故确定此条件为该废水处理的最优条件;同时对比均匀型和蛋白型2种催化剂,蛋白型催化剂具有更高的催化效率;结合SEM及N₂-物理吸附结果,推断蛋白型催化剂活性组分集中分布在催化剂颗粒的较浅层,有利于降低反应过程中的扩散阻力,提高贵金属活性组分的利用率,进而提高催化剂的催化活性。以上结果对开发高效湿式氧化催化剂,充分利用贵金属活性组分降低催化剂成本具有十分重要的意义。