粉砂介质包气带中甲苯蒸气挥发的迁移转化

挥发性有机物通过包气带向上迁移到地表或室内引发的蒸气入侵(vapor intrusion,VI)问题越发受到关注。以甲苯作为研究对象,采用土柱实验,对粉砂介质包气带中甲苯蒸气发生的扩散、生物降解的规律进行研究。结果表明,粉砂介质中,甲苯蒸气扩散穿透70 cm土柱时间为24 h,甲苯蒸气在土柱内扩散10 d时,土柱达到短暂的稳态平衡;12~30 d时,处于动态平衡;30~60 d时,土柱内甲苯蒸气浓度下降速率发生变化,土柱内O_2体积分数下降了8%,CO_2体积分数增加了6%;60 d时,甲苯蒸气基本被降解。说明覆盖一定厚度的粉砂对甲苯蒸气的迁移有比较好的阻滞和生物降解作用。     

不同水分条件下活性污泥对土壤中DOM产生及DDT降解的影响

采用盆钵实验,通过控制淹水、田间最大持水量和60%相对含水量3种水分条件系统研究施用活性污泥(AS)对不同质地土壤中DOM的产生消长规律及DDT降解的影响,旨在为农药污染土壤修复及农产品清洁生产提供理论依据。结果表明:1)不同水分条件下AS均能提高土壤中DOM的含量,且随添加比例增加而增加;2)不同水分条件下AS均能促进土壤中p,p'-DDT降解,淹水条件下添加1%~3%的AS使粘土、壤土和砂土中p,p'-DDT的降解率分别提高4.0%~45.0%、2.7%~48.9%和2.2%~35.4%;最大持水量条件下粘土、壤土和砂土中p,p'-DDT的降解率分别提高2.9%~40.9%、1.9%~46.9%和2.1%~34.3%;60%相对含水量条件下粘土、壤土和砂土中p,p'-DDT的降解率分别提高3.0%~40.9%、2.1%~45.0%和1.7%~31.6%;3)不同水分条件下,不同质地土壤中添加AS后DOC含量与p,p'-DDT含量呈显著正相关。上述结果表明不同水分条件下AS对p,p'-DDT降解的促进效果表现为淹水条件最大持水量60%相对含水量,p,p'-DDT在不同质地土壤中的降解速度表现为壤土粘土砂土。     

嗜热栖热菌降解氟喹诺酮类抗生素

氟喹诺酮类抗生素在各种环境基质中积累造成的生态和耐药基因污染等问题已引起广泛的关注。为了能够有效去除环境中氟喹诺酮类抗生素污染并且探究其生物代谢途径,利用嗜热菌Thermus sp. C419在高温(70℃)条件下降解2种典型的氟喹诺酮类抗生素(诺氟沙星和恩诺沙星),分析了菌株C419对这2种药物在单一和混合添加时的降解特性;通过UPLC-MS/MS检测了其相关的降解产物,并推测了可能的代谢途径;利用平板扩散法对生物降解后的氟喹诺酮类药物进行抑菌活性测定。结果表明:氟喹诺酮类化合物可被菌株C419有效降解,降解率为60%～80%;该生物降解过程符合一级动力学模型,培养基中氟喹诺酮类化合物浓度越高,降解率越高,降解半衰期越短;菌株C419对诺氟沙星的生物降解有3条可能的降解途径和7种降解产物,对恩诺沙星的生物降解有4条可能的降解途径和6种降解产物。此外,与2种药物的母体化合物相比,生物降解后药物对不同细菌的抗菌活性均有一定程度的降低,这说明嗜热菌株C419在热环境中去除氟喹诺酮类污染物方面可能会具有良好的实用性和应用前景。     

连续活性污泥法降解壬基酚聚氧乙烯醚废水的研究

采用连续活性污泥法对壬基酚聚氧乙烯醚NP-10(简称NP-10)废水的生物降解性能进行了研究,考察了水力停留时间(HRT)对其生物降解的影响。结果表明:(1)在生物降解的稳定期,HRT为3、6h的初级生物降解度平均分别为96.5%、96.2%,最终生物降解度平均分别为84.8%、87.3%。这表明,NP-10较易初级生物降解,大部分NP-10可以最终生物降解;延长HRT对其初级生物降解基本没有影响,对其最终生物降解影响不大。(2)采用高效液相色谱法检测了苯环的降解情况。10～20d,HRT为3、6h的苯环降解度平均分别为58.7%、75.4%,说明部分苯环可被降解,苯环降解度随HRT的延长而增加。(3)在稳定期,对不同HRT的空白曝气罐与NP-10曝气罐中的微生物进行鉴定和计数后发现,空白曝气罐与NP-10曝气罐中的微生物在种类和数量上都存在一定的差异;不同HRT的NP-10曝气罐内的微生物情况基本一致。     

TiO_2对几种农药在土壤中光降解的催化作用

以太阳光为光源,研究了TiO2添加量、土壤厚度对毒死蜱、苯线磷、克百威、多菌灵在土壤中光催化降解的影响,并分析了毒死蜱、苯线磷初始浓度对其光催化降解的影响。结果表明,这4种农药的光降解均符合准一级动力学方程,随着TiO2添加量从0mg/kg增加到200mg/kg,光催化降解一级动力学常数逐渐增加。这4种农药在不同厚度含有TiO2的土壤中的光催化降解率不同;在土壤厚度较大的情况下,相应的半衰期也较长;在土壤中添加毒死蜱、苯线磷浓度相对较低的情况下,其对应的光催化降解较快。     

4株聚丙烯酰胺降解菌的深度驯化及联合降解作用

从含聚污泥中分离出4株聚丙烯酰胺降解菌,分别命名为PM1、PM2、PM3和PM4,经16S r DNA鉴定,4种菌分别属于肠杆菌(Enterobacteriaceae bacterium),阴沟肠杆菌(Enterobacter cloacae),巨大芽孢杆菌(Bacillus megaterium)和霍米奇肠杆菌(Enterobacter hormaechei)。为了提高菌种对高浓度、高分子量含聚污水的适应能力及降解聚丙烯酰胺的效率,将其进行深度驯化并混合培养。结果表明:经过驯化,菌种的OD值明显高于驯化之前,4种降解菌对400 mg/L溶液中聚丙烯酰胺的降解率分别由驯化前的29.8%、30.9%、40.1%和33.4%提高到36%、40.1%、54.7%和42.7%;并且混合菌PM2PM3在投加体积分数为4%时对聚丙烯酰胺降解率最高能达到67%,具有一定的协同作用。红外图谱结果显示,生物降解后聚丙烯酰胺分子结构发生变化,分子链上的酰胺基被氧化为羧基。     

酸性媒介黄GG生物降解性能的试验研究

通过试验研究酸性媒介黄GG染料在厌氧、好氧条件下的生物降解机理、降解能力及共代谢降解效果.试验结果表明,厌氧菌能够通过葡萄糖共代谢作用很快降解酸性媒介黄GG;而好氧条件下经驯化活性污泥不能降解酸性媒介黄GG,经过较长时间驯化活性污泥能降解酸性媒介黄GG,但降解效果很差.葡萄糖浓度的升高对提高酸性媒介黄GG厌氧生物降解率有利,当葡萄糖浓度为2000 mg/L时,40mg/L酸性媒介黄GG的12和60 h厌氧生物降解率分别达到81.5%和93.5%.酸性媒介黄GG浓度对厌氧菌的生物降解能力也有影响.当葡萄糖浓度为2000 mg/L,酸性媒介黄GG(浓度为20～100 mg/L)的厌氧降解率最好,降解效率达到了94%,说明厌氧菌对酸性媒介黄GG的降解能力较好.     

慢速可生物降解有机物的转化特性及利用

通过对西安市城市污水处理厂碳源赋存特性和生物降解性分析,探明了西安市城市污水厂碳源的分布特性。西安市污水厂原水中颗粒态COD占总COD的65%左右,以慢速可生物降解有机物为主,是污水厂进水碳源的主要组成部分。分析评价了慢速可生物降解有机物的转化特性与利用潜力,结果表明,在好氧和厌氧2种条件下慢速可生物降解有机物会发生水解发酵作用,在8 h内转化率分别达到58%和65%。其中第1小时为慢速可生物降解有机物的限速阶段,降解缓慢。从第2~4小时降解转化速率显著提高,此后速率逐渐平缓。慢速可生物降解有机物水解产物主要有挥发性脂肪酸(VFAs)、多糖和蛋白类等易于直接被微生物利用的物质。与此同时,也会产生一些腐殖质类的难降解有机物,并在处理过程中会引发其结构改变,趋于生物可利用。     

植物-微生物联合修复石油污染土壤的实验研究

筛选高效石油降解菌并考察菌株的石油降解能力,通过植物-微生物联合修复石油污染土壤室内实验,在修复过程中测定了土壤中细菌和固氮菌,碱解氮、速效磷和速效钾的含量变化,同时采用傅立叶变换离子回旋共振质谱(ESI FT-ICR MS)考察了植物-微生物联合修复效果。结果表明,菌株3#、4#的生长适应性较强,其混合菌的降解效果最好,将其混合菌液与植物进行植物-微生物联合修复不同浓度的石油污染土壤,经过150 d的温室降解,最高降解率达到73.47%。ESI FT-ICR MS分析结果表明,与空白组相比,植物组的O1、O2和N1类等化合物相对丰度都发生了显著变化,石油污染物得到一定程度的生物降解。     

不同共代谢基质下四氯乙烯厌氧生物降解研究

分别用葡萄糖、乳酸盐和醋酸盐作为驯化好的厌氧污泥的共代谢基质 ,对四氯乙烯 ( PCE)的降解进行研究。结果表明 ,PCE是通过还原脱氯发生生物降解的。实验的回归结果表明 ,反应均符合一级动力学方程 ;反应速率常数的大小依次为 k乳酸盐 >k葡萄糖 >k醋酸盐 ;以乳酸盐作为共代谢基质时 ,PCE的降解速率较快 ,在实验条件下乳酸盐是最合适的共代谢基质     

次氯酸钠发生器的研制

介绍了电解法生产次氯酸钠的原理 ,并在原有生产工艺的基础上进行了重新设计和对设备的重新选择、改造 ,得出了各个工艺参数的最佳值 ,生产出高品质的次氯酸钠     

Estimation of uncertainty of sampling for analysis of pesticide residues

Abstract

A computer model was used to take random samples from primary sample populations obtained from field trials to simulate the uncertainty of sampling for residue analysis of plant commodities and soil. The results indicate about 40%, 30% and 20% relative uncertainty when random samples of size 5, 10 and 25 are taken respectively, from a single lot. Therefore the sample size should be the same for establishing and enforcing legal limits.     

Evaluation of the presence of drugs of abuse in tap waters

A total of seventy samples of drinking water were tested for non-controlled and illicit drugs. Of these, 43 were from Spanish cities, 15 from seven other European countries, three from Japan and nine from seven different Latin American countries. The most frequently detected compounds were caffeine, nicotine, cotinine, cocaine and its metabolite benzoylecgonine, methadone and its metabolite EDDP. The mean concentrations of non-controlled drugs were: for caffeine 50 and 19 ng L⁻¹, in Spanish and worldwide drinking water respectively and for nicotine 13 and 19 ng L⁻¹. Illicit drugs were sparsely present and usually at ultratrace level (<1 ng L⁻¹). For example, cocaine has mean values of 0.4 (Spain) and 0.3 ng L⁻¹ (worldwide), whereas for benzoylecgonine, these mean values were 0.4 and 1.8 ng L⁻¹, respectively. Higher concentrations of benzoylecgonine were found in Latin American samples (up to 15 ng L⁻¹). No opiates were identified in any sample but the presence of methadone and EDDP was frequently detected. Total mean values for EDDP were 0.4 ng L⁻¹ (Spain) and 0.3 ng L⁻¹ (worldwide). Very few samples tested positive for amphetamines, in line with the reactivity of chlorine with these compounds. No cannabinoids, LSD, ketamine, fentanyl and PCP were detected.     

不同泥源对厌氧氨氧化反应器启动的影响

采用2套上流式生物膜反应器,分别接种少量厌氧氨氧化污泥和大量硝化污泥,考察其对厌氧氨氧化反应器启动的影响。污泥接种入反应器后,测得接种厌氧氨氧化污泥的反应器(R1)内MLSS为0.22 g/L,另一个反应器(R2)MLSS为2.7 g/L。与直接接种厌氧氨氧化污泥相比,R1经过72 d的运行才显现出厌氧氨氧化特性。经过114 d的培养,前者氮去除速率由0.23 kg/(m3.d)提升到5.29 kg/(m3.d),总氮去除率大于89%;R2的氮去除速率由0.01 kg/(m3.d)提升到1.1 kg/(m3.d),总氮去除率大于84.6%。说明普通污泥启动需要一个较长的筛选过程,直接接种少量的厌氧氨氧化污泥比接种普通的污泥能够更快启动厌氧氨氧化反应器。     

An application of the theory of kinematics of mixing to the study of tropospheric dispersion

The most common technique used for numerical simulations of tracer mixing is that of the numerical solution of the advection–diffusion equation with the unresolved fluxes parameterized using the similarity theory. Despite correct predictions of the overall directions of transport, models based on a numerical solution of the advection–diffusion equation lack sufficient accuracy to correctly reproduce the coupling of mixing with small scale processes which are sensitive to the microstructure of the tracer distribution. The objective of this paper is to revisit the basic formalism employed in numerical models used to investigate atmospheric tracers. The main mathematical method proposed here is the theory of kinematics of mixing which could be applied effectively for simulations of atmospheric transport processes. At the beginning of the paper, we introduce simple mathematical transformations in order to demonstrate how complex topological structures are created by mixing processes. These idealistic flow systems are essential to explain transport properties of much more complex three-dimensional geophysical flows. An example of the application of the kinematics of mixing to the analysis of tracer transport on a planetary scale is presented in the following sections. The complex filamentary structures simulated in the numerical experiment are evaluated using some commonly applied statistical measures in order to compare the results with the data published in the literature. The results of the experiment are also analysed with the help of simple conceptual models of fluid filaments. The microstructure of the tracer distribution introduced in the paper is essential to increase our understanding of atmospheric transport and to develop more realistic parameterizations of small-scale mixing. The presented results could also be used to improve calculations of the coupling between microphysical processes and tracer mixing.     

Mechanisms of biodegradation of dibenzoate plasticizers

Biodegradation mechanisms were elucidated for three dibenzoate plasticizers: diethylene glycol dibenzoate (D(EG)DB), dipropylene glycol dibenzoate (D(PG)DB), both of which are commercially available, and 1,6-hexanediol dibenzoate, a potential green plasticizer. Degradation studies were done using Rhodococcus rhodochrous in the presence of pure alkanes as a co-substrate. As expected, the first degradation step for all of these systems was the hydrolysis of one ester bond with the release of benzoic acid and a monoester. Subsequent biodegradation of the monobenzoates of diethylene glycol (D(EG)MB) and dipropylene glycol (D(PG)MB) was very slow, leading to significant accumulation of these monoesters. In contrast, 1,6-hexanediol monobenzoate was quickly degraded and characterization of the metabolites indicated that the biodegradation proceeded by way of the oxidation of the alcohol group to generate 6-(benzoyloxy) hexanoic acid followed by β-oxidation steps. This pathway was blocked for D(EG)MB and D(PG)MB by the presence of an ether function.The use of a pure hydrocarbon as a co-substrate resulted in the formation of another class of metabolites; namely the esters of the alcohols formed by the oxidation of the alkanes and the benzoic acid released by hydrolysis of the original diesters. These metabolites were biodegraded without the accumulation of any intermediates.     

混凝试验搅拌器的研制

影响混凝效果的因素众多,混凝沉淀烧杯试验是进行水的混合、絮凝、沉淀工艺研究、设计和生产指导的最有效方法之一,阐述了智能型混凝试验搅拌器的设计原理和技术性能.     

产油微藻培养与回收的关键技术研究进展

寻找廉价而高效的替代原料是实现生物柴油产业化的关键所在.微藻以含油量高、生长周期短、环境适应能力强、生物产量高等优点,有望成为一种极具潜力的生物柴油生产原料.然而,目前尚存在微藻培养低效成本高和微藻回收效率低两大难题.综述了微藻培养与回收过程中的关键技术,并对存在的两大难题及其改进技术进行了详细的探讨.最后,总结并展望了微藻培养、回收技术未来的发展趋势.     

生物质快速热裂解主要参数对生物油产率的影响

以松木木屑为原料,在自制的小型流化床上,开展了生物质热裂解温度、生物质粒径和进料速率对生物油产率的影响实验研究.结果表明,在热裂解温度分别为450、475、500、525和550℃条件下,当热裂解温度为500℃时,生物油产率最高,平均产率达到53.33%（质量百分比）.反应温度越高,炭产量越低,不可冷凝气体产量越高,气体发热值越高;粒径＜1 mm的生物质其粒径对生物油产率影响不大;生物质进料速率增加时,生物油产率增加.本研究为生物能的利用提供了新的途径.     

造纸废水混凝处理中SFT助凝替代性研究

中小造纸厂废水处理常用PAC作混凝剂 ,PAM作助凝剂。由于PAM成本很高 ,影响了处理设备的投运率。用超细滑石粉 (SFT)替代PAM助凝 ,与混凝剂PAC配合 ,其混凝处理效果基本相当 ,但是处理成本降低 0 .10元 /m3 。由于SFT属环境无害材料 ,不会给排泥带来二次污染