高效复合微生物菌剂对聚丙烯酰胺的无害化降解

聚丙烯酰胺(PAM)对环境的污染日趋严重,尤其是降解后的单体丙烯酰胺对人类的神经系统有很大的危害。筛选出的优势菌可对PAM溶液有良好的降解效果,降解率达到89%。但是,PAM不能成为菌种的最佳营养物,添加基础营养液可使其达到最佳降解的目的。通过对培养条件的优化,提高了菌种的降解能力。本复合菌剂在降解PAM的同时,迅速降解掉脱落的丙烯酰胺单体,不会对环境造成二次污染。     

用复合絮凝剂处理含乳化油废水的试验研究

本文对处理含乳化油废水所用的破乳絮凝剂进行了试验研究.分别采用电解质、无机高分子聚合物及电解质与高分子聚合物复合处理含乳化油废水.结果表明,与采用单一药剂相比,电解质与无机高分子聚合物复合处理含乳化油废水具有投药量小、药剂费用低、处理效果好、pH值适用范围宽等特点.本文还探讨了电解质与无机高分子聚合物复合破乳的机理,并且提出处理不同浓度的含乳化油废水时电解质与高分子聚合物的最佳复配比例及配比规律.还讨论了投加聚丙烯酰胺(PAM)的协同作用.这些为工业应用提供了必要的技术参数.     

混凝沉淀——SBR工艺处理染料废水

采用混凝沉淀－序批式活性污泥法（SBR）工艺处理染料化工废水，处理出水达到GB8978－1996《污水综合排放标准》二级排放标准。工程实践表明：该处理系统具有运行管理简单，工程投资省，运行费用低等特点。     

城市生活垃圾的堆肥研究

城市生活垃圾经动态式堆肥翻堆机处理制成腐熟堆肥，并最终试制成有机复混颗粒肥，二者先后在茶树、数种花卉作物和数种叶菜类蔬菜上进行田间试验，证明有较好的肥效，且成本较低廉，在农业生产上有实际应用的价值。从环境保护角度上看：这种方法是将城市生活垃圾转化为资源化、无害化的一项有意义的举措。     

阳离子淀粉-双氰胺-甲醛絮凝剂的合成及其絮凝性能

以阳离子淀粉、双氰胺、甲醛为主要原料,以硫酸铝为催化剂,并引入添加剂合成了阳离子淀粉 双氰胺 甲醛脱色絮凝剂。探讨了阳离子淀粉用量、甲醛用量、催化剂用量、反应温度、反应时间及添加剂对阳离子淀粉 双氰胺 甲醛树脂混凝脱色性能的影响,并对印染废水进行了混凝脱色试验。实验结果发现,当双氰胺23 5g、阳离子淀粉5 6g、甲醛57 8g、硫酸铝4 8g、添加剂12 5g、反应温度(70±1)℃、反应时间为1 5小时。试验表明产品的混凝脱色性能良好,CODCr去除率≥91%,脱色率≥99%。并对制得的产品进行了絮凝性能试验,结果表明该产品具有良好的絮凝性能。     

Constitutive and herbivore‐induced volatiles in pear,alder and hawthorn trees

Summary. Qualitative and quantitative differences among pear cultivars were found in constitutive and Cacopsylla-induced volatiles, depending on experimental treatment of the trees (i.e., uninfested and partly or completely infested by psyllids). Blend differences were also found between pear cultivars and wild-type pear, alder and hawthorn–the latter trees are frequently present in pear orchard hedgerows. ?Interesting differences were found in the presence of methyl salicylate and (E,E)-α-farnesene, two compounds previously found to mediate attraction of predatory bugs towards psyllid-infested pear trees. Methyl salicylate is expressed constitutively and is induced systemically by infestation in the whole plant of all four cultivars. (E,E)-α-farnesene on the other hand showed also systemic induction in Bartlett, NY10355 and Beurré Hardy, but in partially infested Conference trees it was induced locally, only in herbivore-damaged leaves. No methyl salicylate or (E,E)-α-farnesene were identified in honeydew. In field collected headspace samples of alder leaves infested by aphids and leaf beetles we found methyl salicylate but no (E,E)-α-farnesene, whereas in uninfested hawthorn neither were identified. Insight in the variability of damage-related pear volatiles will have important implications for integrated pest management in the field. Received 27 August 2002; accepted 28 November 2002 R1D=" Correspondence to: Petru Scutareanu, e-mail:scuterea@science.uva.nl     

Cu/γ-Al2O3的制备及对活性艳红X-3B的脱色性能研究

为实现活性染料X-3B废水在常温常压下高效地脱色,以过渡金属为活性组分、活性氧化铝(γ-Al_2O_3)为载体,采用等体积浸渍法制备了一系列M/γ-Al_2O_3(M=Cu2+、Fe3+、Zn2+、Mn2+)负载型催化剂,并考察其对活性艳红X-3B模拟染料废水的脱色性能,同时考察了活性组分、焙烧温度、负载量、催化剂投加量、氧化剂用量及pH值等因素对活性艳红X-3B脱色性能的影响规律。结果表明,常温常压下,以Cu2+为活性组分,焙烧温度为350℃、负载量为4%(质量分数)、氧化剂H_2O_2浓度为58 mmol/L、催化剂投加量为1.2 g/L、pH值为5~7、反应50 min时,催化剂对活性艳红X-3B废水的脱色效果最佳,脱色率可达95%以上。平行试验表明,Cu2+的存在可增加载体表面的吸附中心,H_2O_2可分解产生HO·,当两者共存时,活性艳红X-3B在催化剂表面主要发生化学吸附与催化氧化两种反应过程,且染料在Cu/γ-Al_2O_3上发生的吸附作用明显大于H_2O_2分解产生HO·而引发的催化氧化作用。动力学试验表明,活性艳红X-3B反应过程动力学模型与初始质量浓度有关,大于等于200 mg/L时,符合准一级动力学方程。     

TiO2-assisted photo-catalysis degradation process of dye chemicals

ＩｎｔｒｏｄｕｃｔｉｏｎＡｓｏｎｅｏｆｔｈｅｍａｉｎ ｐｏｌｌｕｔｉｏｎｓｏｕｒｃｅｓｉｎＣｈｉｎａ ,ｔｈｅｔｅｘｔｉｌｅｄｙｅｉｎｇａｎｄｆｉｎｉｓｈｉｎｇｉｎｄｕｓｔｒｙａｎｎｕａｌｌｙｃｒｅａｔｅｓ 9— 12× 10 8ｍ3ｗａｓｔｅｗａｔｅｒｗｉｔｈｈｉｇｈｏｒｇａｎｉｃｓｔｒｅｎｇｔｈａｎｄｃｏｌｏｕｒ(Ｌｉ,1999ｂ) .Ｄｙｅｓａｒｅｔｈｅｍｏｓｔｉｍｐｏｒｔａｎｔｃｌａｓｓｏｆｓｙｎｔｈｅｔｉｃｏｒｇａｎｉｃｃｈｅｍｉｃａｌｓ.Ｉｎ ｇｅｎｅｒａｌ,ｃｏｎｖｅｎｔｉｏｎａｌｂｉｏｌｏｇｉｃａｌｔｒｅ…     

TiO_2/beads as a photocatalyst for the degradation of X_(3B) azo dye

ＩｎｔｒｏｄｕｃｔｉｏｎＥｎｖｉｒｏｎｍｅｎｔａｌｐｒｏｔｅｃｔｉｏｎｅｘｐｅｒｔｓｉｎｍａｎｙｃｏｕｎｔｒｉｅｓｐａｙｈｉｇｈａｔｔｅｎｔｉｏｎｔｏｔｈｅｄｉｓｐｏｓａｌｏｆｔｈｅｗａｓｔｅｗａｔｅｒｗｉｔｈｄｙｅｏｒｗｉｔｈｄｅｅｐｃｈｒｏｍａ.Ｔｈｏｕｇｈａｔｐｒｅｓｅｎｔｂｉｏｄｅｇｒａｄａｔｉｏｎｉｓｕｓｅｄｉｎｔｈｅｄｉｓｐｏｓａｌｏｆｔｈｅｗａｓｔｅｗａｔｅｒ,ｔｈｅｃｏｎｃｅｎｔｒａｔｉｏｎａｎｄｃｈｒｏｍａｉｎｔｈｅｄｉｓｐｏｓｅｄｗａｔｅｒａｒｅｓｔｉｌｌｖｅｒｙｈｉｇｈａｎｄ…     

Microeconomic theory of chemical production processes: application to aqueous VOC air stripping operations

A novel microeconomic formalism for chemical processes is applied to air stripping of harmful volatile organic compounds (VOCs) from aqueous streams in a conventional packed tower. A simplified conceptual process model is combined with techno-economic aggregation rules to obtain an engineering production function, which relates process inputs (capital, material, labor, and energy) to output (stripped water flow rate). Process relationships determine column length and diameter required to achieve a specified VOC percent recovery from an aqueous stream of given composition and flow rate. Total capital is determined using a defined capital unit (1 capital unit=10 foot of 6-inch schedule 40 carbon steel welded pipe=$122, Jan. 1990) to put all installed capital equipment on the same basis and multiplying by 3.37 to account for the necessary plant infrastructure. Process labor is obtained from an empirical correlation, which relates workerhours to mass throughput. Simulations were made for four systems comprised from each of two representative random packings (i.e. 25-mm plastic Pall rings and 25-mm ceramic Raschig rings) and two model VOCs (i.e. 1,2-dichloroethane and trichloroethylene). Several examples are given, and process, technical and economic analyses of the results are presented. Two-dimensional (capital-energy) optimization was effective in determining the least cost combination of inputs for a plant to produce a specified output of stripped water. Furthermore, conventional economic models (e.g. Cobb-Douglas model) and associated methods (e.g. linear programming) were shown to be ineffective for air stripping plant design and optimization. Moreover, increasing returns to scale with economies of scale (declining long-run average cost) are prevalent.