接种微生物与人粪便同步连续投加对好氧堆肥效果的影响

利用新型梨形筒式好氧堆肥反应器，在通风量为3．0L／min，搅拌频率为5min／h的条件下，就不接种微生物、接种土著菌种、枯草芽孢杆菌与酵母菌时人粪便连续投加好氧堆肥效果进行了对比。堆制20d即2个运行周期中各堆体的温度、含水率、COD、总氮、pH值与GI等的变化表明，接种微生物可以显著提高堆体的升温速率与堆体平均温度、COD降解率、Ct（P〈0．01），堆肥可迅速达到完全腐熟。接种土著菌种效果最为明显（P〈0．01），其后相继为枯草芽孢杆菌与酵母菌。接种土著菌种可使堆体温度在50℃以上维持18d，第8天COD降解率达到61．17％、总氮损失率为25．75％，第6天时GI达到108．22％。     

复合微生物菌剂对污泥堆肥的作用效果研究

为了研究复合微生物菌剂对污泥堆肥的作用效果,以消化污泥、锯末和回流堆肥为原料,接种不同剂量(0、0.2%、0.5%)的复合微生物菌剂进行室外露天堆肥,分析了温度、含水率、pH值、全碳(TC)、全氮(TN)、种子发芽指数(germination index,GI)的动态变化,结果表明:各堆体温度保持在50℃以上的时间均超过7 d,满足堆肥卫生标准;接种复合微生物菌剂的堆体升温速率和温度最高值均大于未接种堆体,接种复合微生物菌剂有利于增加堆体水分散失量,加快堆体有机质降解速度,降低堆体氮的损失量,提高GI值;其中微生物菌剂接种量为0.5%的堆体,接种处理对水分散失、氮损失的控制和GI值的增加效果较明显.     

固定化混合菌修复油污染地表水的研究

从辽河油田受石油污染的河床底泥中筛选出一株芽孢杆菌(Bacillus sp.)和一株黄杆菌(Flavobacterium sp.)，采用二次交联化学方法对2株细菌单独及混合固定，分别进行了不同接种量的固定化细菌对油的降解，以及固定化混合菌对环境的耐受性和在自然地表水中对油的降解进行研究，结果表明，在相同时间内固定化混合菌对油的降解效果明显优于固定化单株菌，而且都优于游离菌。固定化混合菌pH在6～10、温度在20～40℃范围内能保持较好的活性。在120 h时，固定化混合菌对自然地表水中油的降解率达94.5%,对地表水中COD的去除率达89.6%。扫描电子显微镜分析显示，固定化载体的微观结构适合细菌的生长，固定化混合菌在载体内部形成高密度的菌群。以上的研究为固定化微生物应用于油污染地表水的生物修复提供了一定的理论基础。     

不同菌种组合对发酵残余物好氧堆肥进程及氮素变化的影响

适宜菌剂组合对于初始电导率(Electronic conductivity,EC)较高的发酵残余物二次干化腐熟效果具有重要影响。通过在发酵残余物(猪场沼渣、城市生活污泥)好氧发酵过程中添加不同菌种组合,研究堆肥腐熟指标变化,特别是不同形态氮素指标变化,以期更好提升发酵残余物的干化和腐熟程度。结果表明:F3菌剂组合处理高温期达16 d,最高温度为69.5℃,最早进入腐熟阶段,全氮损失比例最少,为8.72%;对照组在高温期(14 d、69.3℃)及全氮损失比例(9.21%)指标上仅低于F3处理组,表明自然堆体存在耐盐菌种;在促进堆肥腐熟效果方面,霉菌起着关键的作用,堆肥后期酵母菌的存在促进堆体腐熟度的提升;菌种比例和种类的合理设置对于堆体腐熟度提高的重要性要高于活菌添加量;在堆肥保氮过程中,真菌(霉菌和酵母菌)起着重要作用。F3处理(即芽孢杆菌∶霉菌∶酵母菌=1∶2∶2),是实现发酵残余物快速高效堆肥的理想菌剂配方,其他复配菌种组合保氮效果改良侧重点各不相同。     

生物表面活性剂在城市污泥静态强制通风好氧堆肥中的作用

采用静态强制通风好氧堆肥模式对城市剩余污泥进行堆肥降解,并研究了生物表面活性剂鼠李糖脂对堆肥过程的作用。结果表明,堆肥过程中,添加了质量分数为0.015%鼠李糖脂溶液堆制处理和空白对照堆制处理的堆温变化都明显呈现出中温期0～5 d、高温期6～12 d和降温期13～28 d 3个阶段。实验组比空白组的堆体升温快、高温期持续时间长、堆体的含水率高。鼠李糖脂的添加,使实验组的微生物数量高于空白组。添加鼠李糖脂的堆体和空白堆体的种子发芽指数(GI)在堆肥结束时分别为53.70%和50.80%,说明鼠李糖脂促进了堆肥的腐熟,但由于相对浓缩效应,堆肥产品的重金属含量略高于空白堆体。生物表面活性剂的介入促进了堆肥中木质纤维素的初步降解。研究表明,添加鼠李糖脂能够改善堆肥处理的微环境,促进有机质降解和堆肥的腐熟。     

好氧堆肥反应器对人粪便堆肥中温降解的中试研究

控制温度为（35±2）℃，以新鲜锯末为空白载体，在控制含水率为55%~60%和强制通风的好氧条件下，进行为期15 d的实验，进行了人粪便好氧堆肥的中试研究，重点分析了在堆肥过程中有机物的降解、氮素的迁移转化规律及生物量的变化。结果表明，粪便中有机物含量在前2天稍微上升，然后迅速下降，最终去除率为71.82%；随着NH₃-N释放量的增加，堆料中N_tot含量从第4天开始减少，最终损失 22.61%，其中N_org损失占74.35%，NH₃-N占23.52%；所损失的氮素有91.66%以氨氮的形式释放。粪便中的有机物和氮的含量能在8~10 d后达到稳定，且堆体无臭味；粪便中溶解性有机物为微生物的生长提供营养物质，因此生物量变化的过程与有机物降解的有着紧密的联系；病原菌在堆肥过程中得到有效去除，表明该反应器堆肥的无害化。     

微生物对煤矿固体废弃物的脱硫效应

煤矸石是煤矿特有的一种固体废弃物，应用本实验室筛选出的氧化亚铁硫杆菌Thiobacillus ferrooxidans和嗜酸氧化硫硫杆菌Thiobacillus thiooxidans对宁夏大武口高硫煤矸石进行微生物脱硫技术及应用条件的研究，如不同煤矸石粒径、不同接种浓度和不同煤矸石浓度。2种脱硫细菌对煤矸石的脱硫效果显著，小粒径煤矸石的微生物脱硫效果更好。考虑脱硫成本及脱硫效率，Thiobacillus ferrooxidans菌最佳的接种浓度为25%，在Thiobacillus Thiobacillus thiooxidans菌悬液中，能脱出最大量硫酸根的煤矸石最佳比例是10%。2种菌混合较单菌株脱硫效果更好，以Thiobacillus ferrooxidans∶Thiobacillus thiooxidans=2∶3的比例混合后对煤矸石的脱硫效果最佳，该结果为煤矿废弃物煤矸石的污染防治提供技术依据。     

接种外源微生物菌剂对香蕉茎秆堆肥的影响

为了研究接种外源微生物菌剂对香蕉茎秆堆肥的影响,本实验采用高温好氧堆肥技术,设计了对照（不接菌）、接种白腐菌及棱盖多孔菌3个处理,探讨了不同处理堆肥过程中堆体温度、水分、pH值、电导率、有机碳、C/N、发芽指数及堆肥质量的变化情况。结果表明,接种微生物菌剂处理的温度均高于对照,且高温期持续时间相对较长,以接种白腐菌处理的高温持续时间最长;接种外源微生物菌剂对堆肥含水率、pH、EC、全碳、C/N变化影响不大;与对照相比,接种白腐菌可增加全氮及全钾的含量,有利于提高堆肥产品质量;接种白腐菌处理在36 d（GI〉50%）就达到腐熟,比对照提前8 d腐熟,明显缩短堆肥腐熟时间;而接种棱盖多孔菌处理比对照推迟10 d腐熟,共需54 d不利于香蕉茎秆堆肥的进行。     

利用污泥熟肥作为高含水率污泥堆肥调理剂

采用静态强制通风好氧堆肥的方法,以木屑作为对比,考察了利用污泥熟肥作为调理剂对污泥堆肥过程的影响。结果表明,与以木屑作为调理剂的污泥堆体(对照组)相比,以污泥熟肥作为调理剂的污泥堆体(实验组)升温快,高温阶段(>50℃)持续时间长达10 d,满足粪便无害化卫生标准的要求,而对照组仅持续了2 d;实验组腐熟的堆肥含水率从60%降到39%,下降了21%,pH维持在7.5～8.5范围内,微生物活性较强,而对照组含水率仅下降15%,pH始终低于7.5;实验组种子发芽指数(GI)在第14天就回升到80%以上,基本上去除了植物毒性,而对照组GI在第22天才回升到50%。总体而言,污泥熟肥能显著改善堆肥中微生物的微环境,促进有机物的降解,缩短堆肥腐熟时间,是一种优质的调理剂。     

造纸废水灌溉对黄河三角洲退化湿地可培养土壤微生物的影响

利用造纸废水恢复重度退化湿地，分析了土壤微生物数量、土壤呼吸强度及微生物量碳的变化情况。结果表明，灌溉后，8月份，细菌和真菌数量最多，放线菌5月份数量最多；细菌、真菌、放线菌各灌水深度上层大于中层，各灌水深度、细菌、真菌、放线菌上层数量均大于对照；土壤呼吸主要发生在表层（0~20 cm）；8月份，微生物量碳达到最大值690.3 mg/kg，且上中下层依次递减。相关分析表明，15 cm灌水量，土壤呼吸强度与有机碳呈极显著正相关（r=0.996，P=0.0036），灌水量为0、5、10和20 cm，土壤微生物量碳与有机碳呈极显著正相关(r=0.999，0.999，0.999；P<0.001)，15 cm灌水量，微生物量碳与速效磷呈极显著正相关（r=0.972，P=0.028）；5 cm灌水量，微生物总数与有机碳呈显著线性正相关（r=0.953，P=0.047），对照和15 cm灌水量，微生物总数与速效磷呈显著正相关（r=0.976，P=0.024；r=0.968；P=0.032）。灌溉处理后的造纸废水，可增加重度退化湿地土壤微生物的活性，改善土壤质量。     

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     

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.     

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.     

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.     

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。     

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.     

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.     

Visualisation of the complexity of EUSES

The interdependencies of parameters applied in the models of EUSES are visualised in a directed connectivity graph. The parameters (inputs, defaults, state variables, outputs) are represented by boxes (nodes) and their relations by lines (edges). The visualisation, on the one hand, clarifies the complexity of the models in EUSES and, on the other hand, creates an overview and transparency. The parameters’ relations to each other can be recognised faster, and the models can be better understood. The complexity was quantified by the number (variety), kind (substance parameter, physico-chemical parameter, concentration, other parameters), and depth (dimension) of the parameter and the number of relations (connectivity). The variety of EUSES (without the modelsSimple Treat andSimple Box whose interior structure is not documented and without the effect and risk characterisation) amounts to 466, the connectivity to 961, and the maximal dimension is 21.