玉米芯生物炭对河岸带土壤中乙草胺和阿特拉津的吸附性能

为改善农药对河岸带土壤污染状况,进而防控农业面源污染,以玉米芯为原料制备生物质炭,利用模拟实验研究其对河岸带土壤中乙草胺和阿特拉津的吸附性能影响,并探讨了其吸附机理。结果表明:河岸带土壤中添加生物炭可使乙草胺和阿特拉津的吸附容量显著增强,其吸附热力学过程与Freundlich和Langmuir模型拟合均有较好的相关性。与对照土壤相比,添加质量分数为1.0%生物炭的土壤对乙草胺的最大吸附量从13.28μg·g~(-1)升高到769.23μg·g~(-1);添加质量分数为0.3%生物炭的土壤对阿特拉津的最大吸附量从70.92μg·g~(-1)升高到333.33μg·g~(-1)。伪二级动力学速率方程对河岸带土壤吸附乙草胺和阿特拉津的过程拟合效果较好,优于一级动力学速率模型的拟合结果,吸附量以及吸附速率均与土壤中生物炭投加量成正比。玉米芯生物炭可作为河岸带土壤的修复剂,降低乙草胺和阿特拉津的迁移性。     

生物炭对双酚A和17α-乙炔基雌二醇在土壤中吸附的影响

研究了添加生物炭对土壤吸附双酚A(BPA)和17α-乙炔基雌二醇(EE2)的影响。结果表明:BPA和EE2在添加生物炭前后的土壤中的等温吸附线都能被Freundlich模型很好地拟合,所有等温吸附线都呈现出非线性(非线性参数n在0.40~0.79之间),且添加生物炭之后吸附参数KF显著增大。根据等温吸附线,在污染物的平衡浓度为0.01 mg·L-1时,添加4%生物炭后,BPA和EE2的土水分配系数(Kd)分别提高了2.6和3.0倍,此时生物炭对土壤吸附BPA和EE2的贡献度分别达到72.5%和88.5%。进一步研究发现,添加生物炭使土-水吸附系统的p H及溶解性有机质浓度(DOC)升高,这对污染物在土壤中的吸附分别表现为一定的抑制和促进作用。添加生物炭对土壤吸附EE2的促进效果优于BPA,这主要是由于EE2比BPA具有更强的疏水性。     

多环芳烃在淮河、黄河和卫河沉积物上的吸附及解吸行为研究

以淮河沉积物上多环芳烃的吸附研究为主线,以黄河、卫河沉积物为比对,研究菲和芘在3种河流沉积物上的吸附和解吸行为,重点考察吸附剂有机质组分、环境温度、吸附时间和共存物等因素对吸附的影响,找出可以用来预测这3条河流沉积物对多环芳烃吸附作用的模式。结果表明,菲和芘在3种河流沉积物上的吸附均呈非线性,可用Freundlich方程拟合,属放热反应、物理吸附。同一吸附质的有机碳归一化分配系数(Koc)数值相近,说明吸附剂有机质组分对吸附起主导作用;吸附能力随着吸附时间延长而增加,并与吸附质疏水性成正比;多环芳烃共存,有竞争吸附现象;辛醇/水分配系数可用来预测3种河流沉积物对多环芳烃的吸附作用;解吸存在滞后现象,吸附质疏水性强、吸附剂有机质含量高的体系,解吸滞后现象更加明显。     

小麦秸秆生物碳质吸附剂对硝基苯的吸附性能

在炭化温度为300℃下,用小麦秸秆制备生物碳质吸附剂,研究生物碳质吸附剂对硝基苯废水的吸附性能.考察了pH值、温度、吸附时间和吸附剂投加量对吸附效果的影响,分析了吸附剂在水中对硝基苯的吸附机理.结果表明,在pH值为7,温度为25℃,吸附时间为8h,吸附剂投加量为3 g/L条件下,生物碳质吸附剂对硝基苯的去除率达到90％.等温吸附曲线符合Freundlich方程,最大吸附量约为92.37 mg/g.定量描述了分配作用与表面吸附对生物碳质总的吸附作用的贡献,炭化后的小麦秸秆非极性增强,使硝基苯与其的极性更为匹配,引起分配作用增大.     

新制备生物炭的特性表征及其对石油烃污染土壤的吸附效果

生物炭作为一种绿色环保的功能材料因其在污水处理和污染土壤修复方面具有显著效果而受到极大关注.采用红外光谱、元素分析仪及微孔分析对不同温度(200、300、400、500和600℃)条件下制备的木屑和麦秆生物炭进行特性表征,并采用制备的生物炭净化石油污染土壤,分别考察了污染物性质、生物质原料和热解温度对其净化效果的影响.结果表明,随着热解温度的增高,生物炭芳香化程度增加,极性降低,微孔结构逐渐发育,表面积增大.加入生物炭33 d后,污染土壤中总石油烃及其组分烷烃的浓度比对照略有降低,而PAHs浓度下降显著.随着热解温度升高,2种生物炭对PAHs的吸附强度均逐渐增大,芳香度增高、表面积增大是强吸附的主要原因.2种生物炭在400℃及以下温度制备时对PAHs的吸附强度为:木屑生物炭＞麦秆生物炭;而400℃以上温度制备的生物炭吸附强度则相反,即麦秆生物炭＞木屑生物炭,说明生物炭原料对其吸附强度也具有显著影响.     

生物炭对土壤吸附邻苯二甲酸二乙酯的影响

选择花生壳为原材料,采用限氧升温法在450、700℃温度下分别热解2、4、6 h制备6种生物炭,在对其表面性质和元素组成进行分析的基础上,重点考察生物炭对土壤吸附邻苯二甲酸二乙酯(diethyl phthalate,DEP)的影响。结果表明:生物炭的比表面积和总孔体积随着热解温度的升高而增加,热解时间的延长也会提高比表面积和总孔体积,而4 h是较为适宜的热解时间;生物炭中元素组成主要受热解温度的影响,热解时间的作用很小,热解温度的升高使生物炭的芳香性增强,极性降低;添加生物炭能显著提高土壤对DEP的吸附能力;Langmuir模型和Freundlich模型均能较好地拟合添加生物炭土壤对DEP的吸附特征;在不同的平衡浓度条件下,生物炭对土壤吸附DEP的贡献率介于82.07%~99.49%之间,表明生物炭对土壤中DEP的吸附发挥着主导作用。相关分析发现,吸附参数ΔKoc与生物炭的比表面积和总孔体积具有显著相关性,提高比表面积和改善孔隙结构可以增强生物炭对DEP的吸附能力。     

热解条件对茶叶渣生物炭特性及镉污染土壤钝化效果的影响

以泡饮过的废弃茶叶为实验原料,通过不同热解温度(300、400、500和600℃)和热解时间(1 h和2 h)制备生物炭,探讨不同热解条件对茶叶渣生物炭(TSBC)的特性及其对镉(Cd)污染土壤钝化效果的影响。结果表明:热解温度的升高可明显增加TSBC的p H和比表面积,降低生物炭的产率、电导率和表面官能团的数量,使TSBC具有弱碱性、较大比表面积和较强的稳定性,对改良酸性土壤和吸附重金属存在一定潜力;而热解时间对其特性没有明显差异,与对照组相比,添加TSBC明显增加了Cd污染土壤的p H、有机碳(SOC)和可溶性有机碳(DOC)含量,但随着制备温度的升高,Cd污染土壤中SOC和DOC增加幅度逐渐降低。添加TSBC显著降低Cd污染土壤中可交换态镉的比例,当热解温度为500~600℃时降幅最显著,其下降比例与对照相比最高可达25.56%;残渣态镉比对照增加了0.88~1.18倍。因此,TSBC对镉污染土壤有较好的钝化效果,这为重金属污染土壤的修复和生活废弃物的资源化利用提供了理论依据。     

椰纤维生物炭添加对海南花岗岩砖红壤吸附Pb(Ⅱ)的影响

海南花岗岩砖红壤与300、500和700℃3种不同裂解温度下的椰纤维生物炭(分别记为YA300、YA500和YA700)混合培养30 d,进行批量等温吸附和解吸实验,研究不同裂解温度椰纤维生物炭添加对土壤吸附Pb(Ⅱ)性能的影响和机理,为生物炭对重金属污染土壤修复的研究提供理论依据。采用Langmuir和Freundlich吸附模型分析处理土壤对Pb(Ⅱ)的吸附差异,用吸附和解吸量推算方法研究处理土壤对Pb(Ⅱ)的静电吸附和非静电吸附差异。结果表明:经过30d的培养,椰纤维生物炭的添加显著提高了土壤的p H值和阳离子交换量(CEC值),提升幅度为YA700、YA500、YA300;生物炭的添加也提高了处理土壤对Pb(Ⅱ)的吸附能力,同时也提高了土壤对Pb(Ⅱ)的非静电吸附,提升幅度也为YA700、YA500、YA300;Langmuir模型可以更好地拟合处理添加YA300、YA500土壤和对照土壤对Pb(Ⅱ)的等温吸附。基础土壤对Pb(Ⅱ)的最大吸附量为3.53 mg·g-1,添加YA300、YA500和YA700培养后土壤对Pb(Ⅱ)的最大吸附量分别增加为4.49、4.92和6.03 mg·g-1。由于基础土壤的p H值和CEC值较低,椰纤维生物炭添加培养主要提高了处理土壤的p H值、CEC值以及土壤的负表面电荷,增强了土壤对Pb(Ⅱ)的吸附能力和非静电吸附百分比,从而降低Pb(Ⅱ)在土壤中的活性。     

鸡粪制备的生物碳对水中磷的吸附去除研究

以鸡粪为原料热解制备的生物碳作为吸附剂,考察了水中磷在生物碳上的吸附动力学,以及吸附效果的主要影响因素,并对磷的去除机制做了初步探讨.结果表明:以鸡粪为原料制备的生物碳具有较高的灰分含量和较高的比表面积,这有利于其对磷的吸附；拟一级动力学模型能更好描述水中磷在生物碳表面的吸附行为,水中磷是通过吸附到生物碳表面的胶体和MgO颗粒上而得以去除的；磷在生物碳上的吸附等温线能较好用Freundlich、Langmuir-Freundlich模型来拟合,表明生物碳对磷的吸附是由非均质过程控制的；生物碳对磷的吸附作用受溶液pH的影响,这是由于pH影响溶液中磷的存在形式,而各种离子在生物碳表面的竞争吸附会影响磷的吸附效果；利用鸡粪热解产生的生物碳吸附去除水中磷是可行的,不仅成本低廉并且能够达到以废治废的目的.     

腐殖酸对生物炭吸附水环境中雌激素的影响

以玉米秸秆为原料,通过500℃限氧裂解制备生物炭(记为500BC),并采用批量吸附实验对比500BC及腐殖酸负载后生物炭(记为500BC-HA)对于水环境中两种雌激素(双酚A(BPA)和17α-乙炔雌二醇(EE2))的吸附性能及作用机制。结果表明,腐殖酸分子可阻塞部分500BC孔隙,使500BC的孔径、孔容及比表面积下降,负载腐殖酸后,500BC的比表面积由8.43m~2/g减小至4.40m~2/g,孔径从26.1nm减小至3.2nm,孔容由0.018cm~3/g下降至0.001cm~3/g;与500BC相比,500BC-HA对BPA、EE2的吸附能力均明显降低,一方面是因为腐殖酸分子占据了500BC表面的吸附点位并堵塞部分孔隙,使其吸附能力降低,另一方面腐殖酸负载后引入更多的含氧官能团,使500BC表面疏水性降低,与雌激素间的疏水作用减弱。腐殖酸负载质量浓度为0～10mg/L时,增加负载质量浓度对500BC吸附性能影响明显,当负载质量浓度大于10mg/L时,腐殖酸在500BC表面达到饱和,继续增加负载浓度对500BC的吸附性能不再产生影响。     

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.     

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.     

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。     

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.     

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.     

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.