Aniline and 2,4,6-trinitrotoluene associate preferentially to low molecular weight fractions of dissolved soil organic matter

Aniline and 2,4,6-trinitrotoluene (TNT) were equilibrated with particulate (POM) and dissolved organic matter (DOM) from an organic soil at different compositions of adsorbed major cations (Na, Al) and pH (aniline: 3.7–5.1, TNT: 4.8–5.0). After separation of POM, concentrations of ¹⁴C-labelled aniline and TNT* (including TNT degradation products) were determined in DOM size fractions using size-exclusion chromatography (SEC) and UV-detection. Concentrations in the <3.5 kDa size fraction were 2.8–6.0 and 8.5–9.5 times higher for aniline and TNT*, respectively, as compared to the >40 kDa fraction. Thus, both aniline and TNT* were preferentially associated to the smallest DOM size fraction. The significant binding to DOM (similar extent as to POM) and the fact that the <3.5 kDa DOM fraction was less susceptible to flocculation by major metals suggests that the mobility of aniline and TNT is highly affected by the solubility of soil organic matter.     

好氧膜-生物反应器中微滤膜选择的实验研究

用扫描电镜表面观察和全自动压汞仪测定了2种亲水化改性PVDF微滤膜的平均孔径、孔隙率等基本性能参数。对2种膜的纯水通量,及其平板膜组件在好氧膜生物反应器内污染过程进行分析。结果显示,2种膜污染过程均呈现先缓慢后快速的"二阶段"趋势,第二阶段是膜污染的主导阶段。尽管平均孔径小、孔隙率高的膜本身阻力大、纯水通量低,但其污染速率较低,物理及化学清洗恢复率较高。膜孔径及孔隙率指标是影响其在MBR中运行的污染速率的主要因素,平均孔径小、孔隙率高的膜抗污染能力强。     

序批式反应器处理垃圾渗滤液的污泥颗粒化及污染物去除性能研究

应用序批式反应器(SBR)处理垃圾渗滤液,以絮状活性污泥为接种污泥,经过37 d的运行,反应器内出现小粒径颗粒污泥。第50 d,反应器中污泥完全颗粒化。稳定运行期间,反应器内污泥的平均粒径为0.7 mm;SVI5min一直维持在较低的水平(27~47 mL/g);MLSS基本稳定在3 700~4 500 mg/L;当COD和氨氮的平均进水浓度为2 150 mg/L和312 mg/L时,平均出水浓度分别为540 mg/L和35 mg/L,去除率分别为75%和89%。     

A new approach to natural capital sustainable development

The three-dimension (3D) ecological footprint makes the analysis of the relationships between the demand and supply of natural capital more credible by importing footprint depth and footprint size. This article used China’s regions as the object to analyze the high-level sustainability of the natural capital from the view of “ecology – efficiency – fairness” multidimensional framework. Research showed that China’s ecological footprint has risen while bio-capacity per capita has descended in recent 20 years. This paper also discusses the spatial distribution of China’s natural capital ecological sustainability, efficiency sustainability and fairness sustainability. Finally, it builds multi-criteria evaluation (MCE) models to get multidimensional sustainability framework taking ecological sustainability, efficiency sustainability, and fairness sustainability into consideration.     

滤料粒径对给水曝气生物滤池运行稳定性的影响

利用给水曝气生物滤池(UBAF)处理刘屋洲水源水,考察了不同陶粒粒径对氨氮、高锰酸盐指数的去除效果以及水头损失变化的影响。结果表明,陶粒3～5 mm的UBAF对氨氮、高锰酸盐指数的去除效果较高,但是其水头损失较大,且反冲洗前后水头损失变化偏大,不利于UBAF稳定运行。陶粒6～10 mm的UBAF运行状况良好,氨氮的去除率为73.8%,高锰酸盐指数的去除率为18.6%,滤池24 h过滤水头损失<0.4 m,反冲洗前后过滤水头损失变化量<5 cm。其出水氨氮和高锰酸盐指数均达到《生活饮用水卫生标准》(GB5749-2006),滤池的水头损失小,反冲洗前后也变化甚微。进一步的实验表明陶粒破碎会导致滤料粒径级配变化,使得水头损失增加。     

利用给水厂污泥预处理畜禽养殖废水

实验考察了直接回用未脱水的给水厂污泥(undewatered water treatment sludge,UWTS)做絮凝剂进行畜禽养殖废水预处理的可行性.单因素实验结果表明,随着投加量和pH的增加,出水悬浮物浓度(suspended solid,SS)、化学需氧量(chemical oxygen demand,COD)和总磷(total phosphorus,TP)的去除率不断增加;随着快速搅拌速度的提高,UWTS的絮凝效果呈现先增强后减弱的趋势;随着沉淀时间的延长,出水中SS、COD和TP的去除率起初逐渐增大,但15 min后去除率变化不明显.进一步的正交实验分析结果表明,UWTS回用做絮凝剂的最佳反应条件为投加量2 800 mg/L,快速搅拌速度300 r/min,沉淀时间15 min,此时对应的SS、COD和TP的去除率分别为74.8％、54.6％和60.5％.最佳反应条件下的粒径分析结果表明,UWTS的投加使得粒径范围在40 ～ 180 μm的颗粒物得到了去除.尽管与商品化絮凝剂相比,UWTS的絮凝效果略差,但是,利用其预处理畜禽养殖废水具有成本优势,因而具有应用潜力.     

压汞法测定火电厂SCR板式催化剂孔参数的研究

以压汞法测定多孔物质的孔结构及比表面积已广泛用于化学工业、催化剂、石油、陶瓷及水泥等各个领域,但国内外关于压汞法在火电厂烟气脱硝催化剂表征中的应用鲜有报道。借鉴孔结构测试的标准方法,对样品处理方法及一些试验条件进行了优化,确定了一种用压汞法表征脱硝催化剂孔参数（主要包括孔容、孔径及孔径分布）的方法。并将该方法用于某电厂运行不同时间的催化剂参数的表征,结果表明,压汞法测得的孔隙数据与催化剂活性存在相关性。此方法的应用将对电厂脱硝催化剂的表征和管理提供指导。     

三峡水库干流消落带沉积泥沙粒径特征及其物源意义

为揭示三峡水库干流消落带的泥沙沉积规律、分析沉积泥沙来源,本研究采用原位观测方法采集沉积泥沙样品,利用激光粒度仪测试泥沙粒径,分析沉积泥沙粒径在水平、垂直和高程3个维度上的变化特征,并与三峡水库入库泥沙的粒径特征相结合,阐述消落带沉积泥沙来源。结果表明:(1)三峡水库干流消落带沉积泥沙粒径在水平方向上存在比较强烈的空间变化,中值粒径沿河流流向方向呈逐渐下降趋势,并在忠县及其下游河段基本保持稳定;(2)泥沙粒径随高程的变化存在较大的空间差异,河流挟沙是消落带下部粗颗粒泥沙的主要来源,而消落带上方的土壤侵蚀强度越高,消落带顶部的沉积颗粒就越容易变粗;(3)在水库尾端,泥沙剖面存在较明显的旋迴分层现象,其中值粒径数值较大、变化幅度较宽,越往下游推进,中值粒径的数值越低、变化幅度越小,泥沙旋迴分层现象逐渐消失;(4)水库尾端的沉积泥沙以库区外来沙为主,越往下游推进,库区内产沙对粗颗粒泥沙的贡献逐渐升高,但库区内外来沙都能够为沉积泥沙提供丰富的细颗粒物源,因此,细沙的来源具有一定的复杂性和多样化特征。     

Rain‐washing of mimic®, RH‐5992, from balsam fir foliage following application of two formulations

Abstract

Two formulation concentrates of the insecticide, RH‐5992 [N'‐t‐butyl‐N'‐(3,5‐dimethylbenzoyl)‐N‐(4‐ethylbenzoyI) hydrazine], an aqueous flowable (2F) and an emulsion‐suspension (ES), were diluted with water to provide spray mixes containing dosage rates ranging from 35 to 150 g of the active ingredient (AI)/ha. The mixes were sprayed in a laboratory chamber, onto balsam fir branch tips collected from field trees and greenhouse‐grown seedlings. Droplet spectra and spray mass recovery were determined on artificial samplers. Simulated rainfall of two different intensities was applied at different rain‐free periods, and rain droplet sizes were determined. Foliar washoff of RH‐5992 was assessed after application of different amounts of rain, and the increase in soil residues was evaluated.

A direct relationship was indicated between the amount of rainfall and RH‐5992 washoff. The larger the rain droplet size, the greater the amount washed off. Longer rain‐free periods made the deposits more resistant to rain. Regardless of the amount of rainfall, rain droplet size and rain‐free period, foliar deposits of the 2F formulation were washed off to a greater extent than the ES formulation. The increase in soil residues due to foliar washoff was greater for the 2F than for the ES formulation. The deposits of the emulsion‐suspension were consistently more resistant to rain‐washing than those of the aqueous flowable formulation.     

“引江济太”河段重金属在水体、悬浮颗粒物及表层沉积物中的含量特征研究及标准化分析

研究了"引江济太"河段(长江—望虞河—贡湖段)孔隙水、上覆水、悬浮颗粒物及表层沉积物中重金属的含量特征,并采用标准化分析方法推测了"引江济太"调水对太湖重金属含量及分布的影响。结果表明,"引江济太"河段的上覆水和间隙水中的重金属污染较轻,6种重金属(Cd、Pb、Zn、Cu、Cr和As)平均值大多低于《地表水环境质量标准》(GB 3838—2002)Ⅰ类标准,且低于美国优先污染物国家推荐水质基准持续浓度。悬浮颗粒物及表层沉积物中主要的重金属污染元素是Cd,其中Cd平均值分别为2.20、1.78μg/g,为中国水系沉积物平均值的16、13倍,且达到加拿大淡水沉积物保护准则最初影响水平的3倍左右。标准化分析结果表明,"引江济太"调水工程对太湖重金属含量的变化有一定影响,"引江济太"河段沉积物中的重金属可能经过再悬浮过程进入水体,造成水体二次污染。