供水管网水质评价方法的探讨及其应用

利用了模糊数学评价模型和综合指数评价模型分别对南方某市部分给水管网水质进行评价。评价结果分析表明,模糊数学评价法具有评价准确性好、操作简单的特点;综合指数法具有评价结果直观、精确度较高的优点。从评价结果上看,综合指数法较模糊数学评价法更为合理。     

餐厨垃圾国家政策及地方法规研究和思考

文章介绍了餐厨垃圾的产生和危害,以及目前国家及地方在餐厨垃圾处理方面颁布和制定的指导性文件、政策性法规、及行业标准。通过总结苏州、宁波、西宁、乌鲁木齐等城市在治理餐厨垃圾过程中的经验,结合这些地区在餐厨垃圾处理方面的地方法规、收集运输系统、无害化处理体系的建立过程,通过分析思考,提出了适用于一般城市的关于餐厨垃圾收集、运输、处理过程系统性的工作框架。指出了餐厨垃圾处理目前面临的主要问题,并对未来如何推进和完善餐厨垃圾处理工作提出了合理化建议,对政府未来的决策具有一定程度的参考意义。     

密云水库流域2000-2005年植被覆盖度变化监测

植被是生态系统最重要的组成部分,而植被覆盖度是衡量地表植被状况的一个最重要的指标,是生态系统健康评价的前提和必要的基础。文章利用2000和2005年2个时相的Landsat 7 ETM+遥感影像为数据源,以BP神经网络法为植被覆盖度估算模型,计算了密云水库流域内不同时期的植被覆盖度,生成了该流域2个时相内的植被覆盖度图,以此分析密云水库流域植被覆盖度的时空变化。结果表明,从2000-2005年,密云水库流域内除无植被覆盖类型外(即水域部分),其余土地利用类型的植被覆盖度都呈增加趋势,其中以沙质地和耕地最为明显,分别增长了29.5%和27.3%,并且密云水库流域的平均植被覆盖度不高,尤其西部地区植被覆盖度较差,水土流失和土地沙化情况比较严重。     

新型专性厌氧菌利用葡萄糖进行发酵产氢的实验研究

采用批式发酵法对厌氧产氢菌株Bacteria.P利用葡萄糖发酵,在底物浓度、初始pH值、接种比例等不同培养条件下的产氢能力进行了研究。结果表明:专性厌氧菌P是一种高效产氢的菌株,在葡萄糖质量浓度为10 g/L、初始pH为6.0、接种比例为1∶20时,发酵气体总产量和细胞干重达到最大值,分别为485 mL和0.836 g/L。     

日本高校环境人才培养体制建设特征分析

本文对日本高校的环境人才培养目标,相关课程体系改革及教学方法创新和人才培养规模等环境人才培养体制建设的现状进行分析研究后,认为在为中国逐步实现由人力资源大国向人才强国转变过程中,日本高校环境人才培养体制建设的经验和做法值得我们学习和研究。     

沙湖湿地的生态环境健康评价的研究

通过对生态系统健康评价体系的研究,以沙湖为例进行论证,最终得出沙湖生态系统健康度为0.32,属于不健康,制约沙湖不健康的疾病因子在于：湿地的补水水质差,导致湿地水质污染加重,富营养化现象严重,并且由于人为因素,导致物种多样性逐年下降,以上因素最终导致了沙湖湿地生态系统抗干扰能力下降,湖区湿地健康水平较低,根据对沙湖湿地功能的分析,最终设计出了沙湖湿地生态系统健康恢复技术方案。     

条形荷载下三明治形加筋土挡墙的变形特性分析∗

为了研究条形荷载作用下三明治形混合填土方式对加筋土挡墙变形特性的影响,采用 FLAC3D建立了数值计算模型,分析了三明治形加筋土挡墙的黏土弹性模量 E1、砂土弹性模量 E2、砂土厚度 d、筋材长度 L 以及荷载距面板距离 D 对挡墙变形特性的影响。结果表明：相对于加筋黏土挡墙,三明治形加筋土挡墙变形大幅减小,减少其墙顶沉降约 32%,减少面板位移约 44%;其土压力分布规律为墙后水平土压力大体上随填土深度的增加而增大;适当增大黏土弹性模量有利于减小挡墙顶面差异沉降;砂土存在一个最优弹性模量,使得面板水平位移最小;三明治形加筋土挡墙存在一个最优砂土厚度,使得三明治加筋土挡墙工作性能最佳;当 L/H≥0.7 时,继续增加筋材长度或当 D/H≥0.3 时,继续增大荷载距面板距离对挡墙影响相对较小。     

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.     

Unregulated emissions from diesel engine with particulate filter using Fe-based fuel borne catalyst

The alteration and formation of toxic compounds and potential changes in the toxicity of emissions when using after-treatment technologies have gained wide attention. Volatile organic compound（VOC）, carbonyl compound and particle-phase polycyclic aromatic hydrocarbon（PAH） emissions were tested at European Steady State Cycle（ESC） to study unregulated emissions from a diesel engine with a fuel-borne catalyst and diesel particulate filter（FBC–DPF）. An Fe-based fuel-borne catalyst was used for this study. According to the results, brake specific emissions of total VOCs without and with DPF were 4.7 and4.9 mg/kWh, respectively, showing a 4.3% increase. Benzene and n-undecane emissions increased and toluene emission decreased, while other individual VOC emissions basically had no change. When retrofitted with the FBC–DPF, total carbonyl compound emission decreased 15.7%, from 25.8 to 21.8 mg/kWh. The two highest carbonyls, formaldehyde and acetaldehyde, were reduced from 20.0 and 3.7 to 16.5 and 3.3 mg/kWh respectively. The specific reactivity（SR） with DPF was reduced from 6.68 to 6.64 mg/kWh. Total particle-phase PAH emissions decreased 66.4% with DPF compared to that without DPF. However, the Benzo[a]pyrene equivalent（BaPeq） with DPF had increased from 0.016 to 0.030 mg/kWh.Fluoranthene and Pyrene had the greatest decrease, 91.1% and 88.4% respectively. The increase of two- and three-ring PAHs with DPF indicates that the fuel-borne catalyst caused some gas-phase PAHs to adsorb on particles. The results of this study expand the knowledge of the effects of using a particulate filter and a Fe-based fuel-borne catalyst on diesel engine unregulated emissions.     

Fouling distribution in forward osmosis membrane process

Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis （FO） membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic （alginate） fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process.