PW—W膜分离式活性污泥法处理中小规模高浓度有机废水

阐述ＰＷ－Ｗ膜分离式活性污泥法处理高浓度有机废水的原理、工艺流程及特点。处理系统集生化处理功能和固液分离于一体，对高浓度有机废水的处理取得了良好的效果，且剩余污泥量少，处理水质稳定，维护管理方便，运行费用低。     

我国环境信息技术应用回顾与展望

２１世纪人类将全面进入知识经济时代。专家预测 ,到２１世纪中叶主导知识经济社会的仍是信息。在此期间 ,信息系统是资金投入的重点 ,数据转化为信息、信息转化为知识、知识转化为智慧、智慧转化为科学决策 ,信息与知识管理、存储、传递和应用将对决策起着重要的指导作用。面对新世纪知识经济的挑战 ,必须从战略高度来认识并建设我国环境信息系统。１我国环境信息发展历程１ １我国环境信息基础设施建设“七五”期间 ,我国开始环境信息标准化和环境数据库的开发研究。经过十几年的努力 ,国家环境信息化进展较快 ,取得了一定成效。《国家环…     

生物接触氧化法处理煤矿生活污水的工艺探讨

根据煤矿生活污水的特点，结合几年来工作和学习的经验及体会，论述生物接触氧化法的工艺流程，讨论设计中遇到的问题，探讨设计参数，使用填料和选取方法，为今后的污水处理站设计提供参考。     

战略环境评价及其应用初探

概述了战略环境价的概念、产生原因、研究现状及其工作程序，结合川南矿肥工程项目对它进行了应用初探，提出了计划、规划层次ＳＥＡ的方法和指标，并对我国环评工作提出了建议。     

碳酸根对磷酸钙沉淀反应回收磷的影响简

以模拟的厌氧消化液为处理对象,通过小试实验,考察不同初始磷浓度C_P、Ca/P物质的量比、pH和温度下,碳酸根（CO₃^2-）对磷酸钙沉淀反应回收磷的影响;利用扫描电镜（SEM）、X射线衍射仪（XRD）和傅里叶变换红外光谱（FTIR）对沉淀产物进行表征。结果表明,高浓度的CO₃^2-对以磷酸钙沉淀反应去除和回收磷的效率影响较大;C_P相同时,CO₃^2-浓度（C_CO3^2-）越大,P的去除率越低,低C_P（20 mg/L）时尤为显著;当C_CO3^2-相同时,随着C_P的增大,反应速率加快,P的去除率逐渐升高,但升高幅度越来越小;增大Ca/P比和pH能提高P的去除率,降低CO₃^2-对磷酸钙沉淀反应的抑制作用,综合考虑实际效果,应选择Ca/P比为3.33,pH为9.0作为适宜的反应条件;升高温度对降低CO₃^2-对磷酸钙沉淀反应的抑制作用贡献不大。在C_P为60 mg/L,Ca/P比为1.67,pH为9.0,温度为20℃的条件下,当C _CO3^2-为0时,得到的沉淀产物主要为羟基磷灰石HAP;当C _CO3^2-为30 mmol/L时,得到的沉淀产物为磷酸钙和碳酸合磷灰石的混合物。     

基于白碳黑的水化硅酸钙制备及其磷回收特性简

以白碳黑、硅灰、硅藻土和硅胶筛选硅质原料,并与钙质原料电石渣制备了水化硅酸钙。借助XRF、BET、FTIR等表征手段,通过多次重复除磷实验,研究了硅质原料特性对水化硅酸钙回收磷性能的影响。结果表明,白碳黑具有极高的反应活性,因此可作为制备具有磷回收特性的水化硅酸钙的硅质原料。结合XRD等表征发现,白碳黑的有效利用率是影响水化硅酸钙回收磷性能的关键,该利用率取决于白碳黑与电石渣的摩尔配比以及水热反应温度。当电石渣与白碳黑的摩尔比为1.6：1,反应温度为170℃时,白碳黑具有最佳的利用效率。该条件制备的水化硅酸钙可作为晶种,在其表面结晶形成羟基磷灰石,从而达到磷回收的目的,磷回收后固体物质中的磷含量为19.05%。     

聚甲亚胺酰胺树脂对水中Cu~(2+)的吸附

制备了聚甲亚胺酰胺树脂,对其进行傅里叶变换红外光谱分析。采用批处理方法实验了pH、铜离子初始浓度、吸附时间、吸附剂用量对吸附量的影响,研究了等温吸附模型和吸附动力学模型。优化后的吸附条件为:在铜离子溶液体积50 mL、初始浓度为300 mg/L、pH为6.0时,吸附剂投放量50 mg、吸附时间60 min,此时吸附量达到269.1 mg/g,去除率达89.7%。25℃时在研究浓度范围内,铜离子吸附过程用Langmuir等温线模型和Freundlich等温线模型描述均可;与准一级动力学方程、Elovich方程及内扩散方程相比,准二级动力学方程能更好地描述其吸附动力学过程。     

Fate and transformation of naphthylaminesulfonic azo dye Reactive Black 5 during wastewater treatment process

Certain aromatic amines generated by the decolorization of some azo dyes are not removed substantially by conventional anaerobic–aerobic biotreatment. These aromatic amines are potentially toxic and often released in the wastewater of industrial plants. In this study, the fate and transformation of the naphthylaminesulfonic azo dye Reactive Black 5 (RB5) during different phases of a sequencing batch reactor were investigated. The major products of RB5 decolorization during the anaerobic phase include 2-[(4-aminophenyl)sulfonyl]ethyl hydrogen sulfate (APSEHS) and 1-2-7-triamino-8-hydroxy-3-6-naphthalinedisulfate (TAHNDS). During the aerobic phase, APSEHS was hydrolyzed and produced 4-aminobenzenesulfonic acid, which was further degraded via dearomatization. TAHNDS was transformed rapidly via auto-oxidation into TAHNDS_DP-1 and TAHNDS_DP-2, which were not further removed by the activated sludge during the entire 30-day aerobic phase. In contrast, different behaviors of TAHNDS were observed during the anoxic phase. The transformation of TAHNDS was initiated either by deamination or desulfonation reaction. TAHNDS was then converted into 3,5-diamino-4-hydroxynaphthalene-2-sulfonic acid, which was subsequently removed via ring cleavage reaction under aerobic condition. In conclusion, complete degradation of TAHNDS by activated sludge occurs only during anoxic/aerobic processes instead of the conventional anaerobic/aerobic processes.     

Outdoor fine and ultrafine particle measurements at six bus stops with smoking on two California arterial highways—Results of a pilot study

As indoor smoking bans have become widely adopted, some U.S. communities are considering restricting smoking outdoors, creating a need for measurements of air pollution near smokers outdoors. Personal exposure experiments were conducted with four to five participants at six sidewalk bus stops located 1.5–3.3 m from the curb of two heavily traveled California arterial highways with 3300–5100 vehicles per hour. At each bus stop, a smoker in the group smoked a cigarette. Gravimetrically calibrated continuous monitors were used to measure fine particle concentrations (aerodynamic diameter ≤2.5 µm; PM_2.5) in the breathing zones (within 0.2 m from the nose and mouth) of each participant. At each bus stop, ultrafine particles (UFP), wind speed, temperature, relative humidity, and traffic counts were also measured. For 13 cigarette experiments, the mean PM_2.5 personal exposure of the nonsmoker seated 0.5 m from the smoker during a 5-min cigarette ranged from 15 to 153 µg/m³. Of four persons seated on the bench, the smoker received the highest PM_2.5 breathing-zone exposure of 192 µg/m³. There was a strong proximity effect: nonsmokers at distances 0.5, 1.0, and 1.5 m from the smoker received mean PM_2.5 personal exposures of 59, 40, and 28 µg/m³, respectively, compared with a background level of 1.7 µg/m³. Like the PM_2.5 concentrations, UFP concentrations measured 0.5 m from the smoker increased abruptly when a cigarette started and decreased when the cigarette ended, averaging 44,500 particles/cm³ compared with the background level of 7200 particles/cm³. During nonsmoking periods, the UFP background concentrations showed occasional peaks due to traffic, whereas PM_2.5 background concentrations were extremely low. The results indicate that a single cigarette smoked outdoors at a bus stop can cause PM_2.5 and UFP concentrations near the smoker that are 16–35 and 6.2 times, respectively, higher than the background concentrations due to cars and trucks on an adjacent arterial highway.

Implications: Rules banning smoking indoors have been widely adopted in the United States and in many countries. Some communities are considering smoking bans that would apply to outdoor locations. Although many measurements are available of pollutant concentrations from secondhand smoke at indoor locations, few measurements are available of exposure to secondhand smoke outdoors. This study provides new data on exposure to fine and ultrafine particles from secondhand smoke near a smoker outdoors. The levels are compared with the exposure measured next to a highway. The findings are important for policies that might be developed for reducing exposure to secondhand smoke outdoors.     

活性污泥缺氧转化1-2-7-三氨基-8-羟基-3-6-萘二磺酸

1—2-7-三氨基-8-羟基-3—6-萘二磺酸（TAHNDS）作为偶氮染料的脱色产物很难被常规的厌氧-好氧染料废水处理工艺所去除。研究了未经驯化的活性污泥对TAHNDS的缺氧转化效果。结果表明,只有在特定的缺氧条件下（ORP在-50～-150mV之间）,TAHNDS才能被活性污泥所降解转化。当浓度在10—80mg／L范围内,TAHNDS可在72h内转化93％以上。加入100mg／L的硝酸盐和0．64mmol／L的氧化还原介体蒽醌-2-磺酸钠（AQS）可将40mg／L的TAHNDS的转化时间从84h缩短到36h。光谱及HPLC—MS分析表明,TAHNDS在缺氧条件下主要是通过脱氨基和脱磺酸作用生成已知可好氧生物降解的3,5-二氨基4-羟基萘-2-磺酸。因此,缺氧处理有望作为预处理工艺促进废水中TAHNDS的完全降解。