对水质检测结果的质量控制与保证研究

针对水质检测结果的质量控制与保证探讨这一问题,给出了水质检测的机构,主要介绍了需要对水质检测人员的选择、对水质检测设备的选择和对水质检测材料的选择,同时给出了水质检测方法,主要包括对水样本的确定方法、对水样的检测项目、检测质量的审核,在检测项目中,主要介绍了分析方式的选择、水样本二次检测及检测数据比对、对水样本测试得到异常值复检和对水样本校准曲线控制,这样得到的测试数据,才具有正确性与真实性,才能保证人类对水的质量控制。     

耐氨固氮菌对水稻的增产效果及对土壤肥力变化的影响

耐氨固氮菌是通过基因工程选育出来的新型菌株，水稻接种后，因根系活性提高、吸收功能增强、体内营养状况得到改善而增产．盆栽和田间试验结果表明．水稻接种耐氨固氮菌后增产３．１％—７．１％，氮肥利用率提高１．４％—１１．２％；与对照区比较，土壤肥力并无下降的趋势，是一种投资小、简便易行的增产措施．     

小流域森林生态系统土壤发生与元素地球化学特性

本文研究了广东五华县牛角塘综合治理试验区几种典型森林生态系统土壤的物质迁移、肥力特性及元素迁移与富集传性，结果表明，生态类型的差异不仅会影响到土壤的肥力状况，同时由于水土流失等因素的影响，还会造成土壤机械组成、元素迁移富集特点以及其它发生学特性的差异，林地、半林地及光山地之间在这些方面也存在着明显的差异性．     

黄棕壤镉污染的电动修复及肥力的提升

近些年来,有关施加电场以去除土壤中污染物的报道较多,但是关于电动力学对土壤肥力的影响方面的报道很少。文章研究了电动力学(1V·cm-1)对土壤肥力的影响。修复前后测量的指标有土壤有机质(SOM)、pH、电导率(EC)、氧化还原电位(ORP)、有效氮、速效磷、速效钾。镉质量分数约为100mg·kg-1的模拟污染土壤经电动力学处理60h后,镉的平均去除效率为71%。土壤中的有效氮、速效磷和速效钾分别平均增加38.49%、47.55%和26.81%,同时TOC也增加了7.96%。总之,电动力学修复后,土壤的肥力有了明显的提升。研究结果表明,电动力学在有效去除土壤中镉的同时还能提升土壤的肥力,是一种可行的土壤修复技术。     

欧洲红豆杉细胞培养的研究

从欧洲红豆杉（Ｔａｘｕｓｂａｃｃａｔａ）的嫩茎及什叶诱导出愈伤组织，并对之进行了愈伤组织培养及细胞悬浮培养研究；利用ＨＰＬＣ方法测定了培养物合成紫杉醇的能力．探索了提高培养细胞生长率及紫杉醇含量的一些措施．结果表明，欧洲红豆杉愈伤组织及悬浮培养细胞的生长速率已分别达到０．２７ｇ·Ｌ－１·ｄ－１和０．３５ｇ·Ｌ－１·ｄ－１，紫杉醇含量分别为０．００３１％和０．０１７％。     

市场经济与土肥科技

土肥的基础地位是不随社会性质或社会经济类型的变化而变化的，它既具重要性，又具长久性．市场经济是仍然需要土肥科技的．土肥科技的教学、科研和推广的力度必须加大，局面必须改观，且宜快不宜迟．土肥科技工作者一定要将培肥地力作为中心工作．根据广东的实际，增施有机肥是培肥地力的主要措施，因而抓秸秆还田和发展冬绿肥是我们工作的重点．     

原废水培养基分离活性污泥中的苯酚降解细菌

用未经处理的含酚焦化工业废水为基础配制培养基，采用平板涂布法，在10^-5稀释度下得到100个单菌落分离物．它们均能在以苯酚(500-800mg L^-1)为唯一碳源的无机盐培养基上生长，其16S rDNA基因的ARDBA多态性分析将这些分离物划分成4个分类操作单元(OTUs)．各单元代表株的16S rRNA基因序列分析和检索结果表明，97个分离物与Alcaligenes faecalis同源性达99％，2个分离物分别与Arthrobacter nicotianae和Klebsiella sp.99％同源．另一个分离物与Ochrobactrum sp．96％同源．苯酚经化酶大亚基基因(LmPHs)PCR扩增表明，除类似Arthrobacter nicotianae的菌株外，其它3个分类操作单元的降酚菌都能利用多组分苯酚经化酶代谢途径进行酚代谢．图2表2参11     

Filtration and transport of Bacillus subtilis spores and the F-RNA phage MS2 in a coarse alluvial gravel aquifer: implications in the estimation of setback distances

Filtration of Bacillus subtilis spores and the F-RNA phage MS2 (MS2) on a field scale in a coarse alluvial gravel aquifer was evaluated from the authors' previously published data. An advection-dispersion model that is coupled with first-order attachment kinetics was used in this study to interpret microbial concentration vs. time breakthrough curves (BTC) at sampling wells. Based on attachment rates (katt) that were determined by applying the model to the breakthrough data, filter factors (f) were calculated and compared with f values estimated from the slopes of log (cmax/co) vs. distance plots. These two independent approaches resulted in nearly identical filter factors, suggesting that both approaches are useful in determining reductions in microbial concentrations over transport distance. Applying the graphic approach to analyse spatial data, we have also estimated the f values for different aquifers using information provided by some other published field studies. The results show that values of f, in units of log (cmax/co) m(-1), are consistently in the order of 10(-2) for clean coarse gravel aquifers, 10(-3) for contaminated coarse gravel aquifers, and generally 10(-1) for sandy fine gravel aquifers and river and coastal sand aquifers. For each aquifer category, the f values for bacteriophages and bacteria are in the same order-of-magnitude. The f values estimated in this study indicate that for every one-log reduction in microbial concentration in groundwater, it requires a few tens of meters of travel in clean coarse gravel aquifers, but a few hundreds of meters in contaminated coarse gravel aquifers. In contrast, a one-log reduction generally only requires a few meters of travel in sandy fine gravel aquifers and sand aquifers. Considering the highest concentration in human effluent is in the order of 10(4) pfu/l for enteroviruses and 10(6) cfu/100 ml for faecal coliform bacteria, a 7-log reduction in microbial concentration would comply with the drinking water standards for the downgradient wells under natural gradient conditions. Based on the results of this study, a 7-log reduction would require 125-280 m travel in clean coarse gravel aquifers, 1.7-3.9 km travel in contaminated coarse gravel aquifers, 33-61 m travel in clean sandy fine gravel aquifers, 33-129 m travel in contaminated sandy fine gravel aquifers, and 37-44 m travel in contaminated river and coastal sand aquifers. These recommended setback distances are for a worst-case scenario, assuming direct discharge of raw effluent into the saturated zone of an aquifer. Filtration theory was applied to calculate collision efficiency (alpha) from model-derived attachment rates (katt), and the results are compared with those reported in the literature. The calculated alpha values vary by two orders-of-magnitude, depending on whether collision efficiency is estimated from the effective particle size (d10) or the mean particle size (d50). Collision efficiency values for MS-2 are similar to those previously reported in the literature (e.g. ) [DeBorde, D.C., Woessner, W.W., Kiley, QT., Ball, P., 1999. Rapid transport of viruses in a floodplain aquifer. Water Res. 33 (10), 2229-2238]. However, the collision efficiency values calculated for Bacillus subtilis spores were unrealistic, suggesting that filtration theory is not appropriate for theoretically estimating filtration capacity for poorly sorted coarse gravel aquifer media. This is not surprising, as filtration theory was developed for uniform sand filters and does not consider particle size distribution. Thus, we do not recommend the use of filtration theory to estimate the filter factor or setback distances. Either of the methods applied in this work (BTC or concentration vs. distance analyses), which takes into account aquifer heterogeneities and site-specific conditions, appear to be most useful in determining filter factors and setback distances.     

Characterization of permanent fouling on the surfaces of UV lamps used for wastewater disinfection.

A significant problem with UV disinfection of wastewater is the accumulation of fouling materials at sleeve-water interfaces. It has been shown that automated chemical and/or mechanical cleaning can remove most fouling materials satisfactorily. However, permanent foulants, which cannot be removed completely by typical cleaning operations, always remain on the quartz sleeves. These permanent foulants reduce UV transmittance, in turn reducing disinfecting effectiveness. This research investigated the origins, formation, and composition of permanent fouling. Four instrumental analyses were used: atomic force microscope (AFM), X-ray fluorescence (XRF), scanning electron microscope combined with energy dispersive X-ray microanalysis (SEM/EDX), and sleeve UV transmittance (SUVT). It appeared that permanent foulants were trapped initially by microscale holes and peaks on fresh sleeve surfaces. Based on the topography and roughness measurements from the AFM, after long-term regular chemical and mechanical cleaning, the wipers of cleaning systems damage sleeve surfaces, creating scratches or holes with larger surface areas. Foulants are trapped more easily, and are attached tightly to the surfaces of these scratches or to each other. The results from XRF and SEM/EDX showed that the main fouling components were aluminum, iron, magnesium, calcium, and phosphorus. These could not be related to wastewater quality. For the specific cases studied, chemical plus mechanical cleaning is more effective in removing foulants and avoiding the accumulation of permanent foulants than mechanical cleaning alone; in most cases, SUVT was higher than 90% after chemical plus mechanical cleaning, whereas mechanical cleaning alone achieved only approximately 30% SUVT after long-term usage.     

CuO负载在TiO_2和CeO_2-TiO_2上对NO CO反应的催化作用

用NO CO微反流动法、TPR、XRD、BET和NO TPD等技术研究了CuO在TiO2 和CeO2 TiO2 上对NO CO的催化还原作用 .实验表明 ,不同负载量的CuO在TiO2 上 ,其NO CO的反应活性以Cu12 Ti为最佳 ,在反应温度为 4 0 0℃时 ,NO的转化率达到 10 0 % ;且CuO负载在CeO2 TiO2 上其活性随CeO2 含量的增加而提高 ,Cu12 Ce10 Ti在 30 0℃时就能使NO达到 10 0 %转化 .XRD和TPR结果显示 ,该体系催化活性的高低 ,与CuO在TiO2 和CeO2 TiO2 上高度分散的Cu物种及形成细颗粒的晶相CuO物种有非常密切的关系 ;NO TPD结果显示 ,催化剂还原活性的高低和NO在催化剂表面的脱出与分解难易程度有关 .