电极-SBBR处理含铜有机污水

采用电极一SBBR系统去除Cu^2＋，考察了电流强度，IA竞争离子（阴离子SO4^2-、NO3^-、CL^-和阳离子Zn^2＋、Ph^2＋）、初始含Cu^2＋量及溶液pH值对除铜效除果的影响。结果表明，当电流强度为40mA时Cu^2＋去除率最高为98％。投加阴（SO4^2-、NO3^-、Cl^-）、阳（Zn^2＋、Pb^2＋）离子均会引起出水Cu^2＋浓度的增加，且Cl^-和Ph^2＋含量分别为45mg／L和30mg／L时对Cu^2＋去除的影响更为显著。进水Cu^2＋浓度为30mg／L时，Cu^2＋去除率最高为98．48％，当进水Cu^2＋≥70mg／L时，出水Cu^2＋浓度不能达标。酸性（pH4．0～4．5）与碱性（pH9．0～10．0）条件均不利于Cu^2＋的去除，且酸性条件的负面影响更显著．当pH为4．5～7．5时．Cu^2＋去除率最高为97．78％。     

改良型A2／O-MBR工艺的反硝化除磷性能研究

重点考察了-种改良型膜生物反应器（A2／O—MBR）的脱氮除磷性能。该工艺主要特点在于对膜池硝化回流液进行了固液分离，并将上清液和浓缩污泥分别回流至缺氧池和厌氧池，这种改进提高了系统对氮、磷的同步去除效率。实验结果表明，在水力停留时间（HRT）为12h，污泥龄（SRT）为30d，混合液回流比为200％的运行条件下，进水COD、NH4＋-N、TN和TP平均浓度分别为（225±38）、（24．8±3．9）、（26．7±2．9）和（2．90±0．53）mg／L时，增加膜池硝化回流液固液分离装置前后，系统对COD和NH4＋-N的去除都维持在较高水平，而系统对TN和TP的去除效果显著提高，出水TN和TP平均浓度分别由（14．9±3．3）mg／L和（1．95±0．72）mg／L下降到（9．4±1．9）mg／L和（0．91±0．38）mg／L，表明增加膜池硝化回流液固液分离装置显著改善了A2／O-MBR系统的脱氮除磷效果。反硝化除磷活性实验结果进一步表明，改进后系统中反硝化除磷活性占总除磷活性的比例由51．5％上升至61．7％，说明增加膜池硝化回流液固液分离装置强化了系统的反硝化除磷性能。     

金属铁去除水中Cr~（6＋）的影响因素研究

研究Fe/Cr6＋比值和不同浓度的NO3-、Cl-和SO42-对金属铁去除Cr6＋效果的影响。结果表明,金属铁对水中Cr6＋有很好的还原去除效果;当金属铁的使用量为Cr6＋量的1/2 000时,铁对Cr6＋的去除效果较差且易失去活性,而当金属铁的使用量为Cr6＋量的8 000倍时,铁对Cr6＋的去除效果较好且其活性的持续性较强;3种阴离子（NO3-、Cl-和SO42-）均能提高金属铁对重金属Cr6＋去除率,但在反应初期,3种阴离子对金属铁去除水中Cr6＋影响的差异性不显著,随着反应时间的增加,SO24-对金属铁去除水中Cr6＋的促进作用逐渐强于Cl-和NO3-,3种阴离子对金属铁去除Cr6＋效率促进作用的大小顺序为SO24-〉Cl-〉NO3-。     

利用13X沸石分子筛净化含NH+4-N废水的实验研究

研究了13X沸石分子筛在静态和动态条件下对中低浓度含NH4^＋-N废水的吸附性能，包括影响吸附的主要因素、沸石对NH4^＋-N的吸附效果和沸石的再生等。静态实验结果表明，pH值为6．5～7．5，吸附时间35rain，吸附温度20～30℃的条件下，沸石对50mL NH4^＋-N初始浓度（C0）为80mg／L的废水吸附效果最佳，吸附过程符合Langmuir型吸附等温式，饱和吸附量为8．61mg／g。动态条件下，随水力停留时间增加，沸石对NH4^＋-N的吸附量上升，最大饱和吸附量可达24．20mg／g，吸附过程符合Thomas吸附模型。直接焙烧法对吸附后的沸石进行再生活化处理效果良好。实验证明，利用13X沸石净化中低浓度含NH4^＋-N废水具有良好的工业化应用前景。     

人工湿地基质对NH4＋-N吸附性能

为研究建筑废物红砖和工业废物煤渣用作人工湿地脱氮基质的可行性，分别通过静态吸附实验和动态NHf—N去除效果实验进行考察。结果表明，红砖和煤渣对NH4＋-N最大静态吸附量分别为0．2533mg／g和0．0533mg／g，其吸附等温曲线均符合Freundlich型吸附方程，吸附常数分别为0．0419和0．0091；红砖煤渣组合对污水中NH4＋-N平均动态脱除率达到41．18％，高于红砖的37．63％和煤渣的30．92％。     

水解酸化-A2O污泥减量工艺的运行性能研究

生物处理单元采用水解酸化、多级串联接触曝气、连续流的除磷脱氮A2／O工艺，并辅以外排厌氧富磷污水侧流除磷，开发了一个新型的具有强化除磷脱氮功能的污泥减量HA—A／A—MCO工艺。用该工艺处理校园生活污水发现，在SRT60d、进水COD316～407mg／L、NH4＋-N30～40mg／L、TN35～53mg／L、TP8—12mg／L的条件下，出水COD≤18mg／L、NH4＋-N≤2．1mg／L、TN≤10．3mg／L、TP≤0．44mg／L。研究还发现，水解酸化池处理产生的VFA能有效促进生物除磷脱氮，导致厌氧释磷量达57mg／L，进入化学除磷池的侧流液量仅相当于进水量的13％；系统最主要的脱氮形式是SND和缺氧反硝化，SND脱氮占脱氮总量的50％，缺氧反硝化占26％；HA-A／A—MCO系统有效实现了生物相分离，并利用生物捕食作用获得较低的污泥产率，0．1gMLSS／gCOD。     

MnOx／Al-SBA-15催化剂低温NH3选择性催化还原NO的原位红外研究

用原位红外分别进行了MnOx／Al-SBA-15催化剂上NH3和NO＋O2的吸附态和瞬态实验以及NH3＋NO＋02反应的稳态实验。结果表明，催化剂上存在着L酸位和B酸位，NH3吸附在催化剂上形成配位态的NH3和NH4＋，配位态的NH3能脱氢形成-NH2活性中间态。NO＋O2在催化剂上吸附形成硝酸盐类、硝基类和亚硝酸盐类。将NO＋O2通入预吸附NH3的催化剂中时，表面的配位态的NH3、NH4＋和-NH2都会减少直至消失，SCR反应显著。而将NH3通人预吸附NO＋O2的催化剂中时，只有硝基类和亚硝酸盐类减少，硝酸盐类基本不发生变化，SCR反应微弱。NH3＋NO＋O2稳态反应中，催化剂表面稳定存在着NH4＋和硝酸盐类，SCR反应显著。     

电化学法去除水中的硝酸根

以钛基氧化物涂层材料（Ti／SnO2-Sb2O5-IrO2）为阳极，碳纳米管修饰的石墨（GE—CNT）为阴极构建电化学系统进行硝酸根（NO3-）去除研究，考察了阴极材料、阴极电位和pH值对电化学法去除水中NO[的影响，同时检测了铵离子（NH4＋）和亚硝酸根（NO2-）的生成量。结果表明，利用碳纳米管修饰的石墨阴极可获得较好的硝态氮去除效果；随着阴极电位负移，NO3-去除率随之升高；酸性条件下NO3-去除率最高，NH；生成量也更多。对于由NO3-转化产生的NH4＋，在氯离子存在条件下再次进行电化学处理120min，其去除率可达97．1％。     

改性膨润土对水中磷和藻类的同步去除

为快速去除富营养化水体中的磷和藻类，制备了絮凝剂-镧复合改性膨润土(聚合氯化铝铁-镧复合改性膨润土(PAFC-La)、聚合硫酸铝-镧复合改性膨润土(PAS-La)、聚合硫酸铁-镧复合改性膨润土(PFS-La)、聚合氯化铝-镧复合改性膨润土(PAC-La)),对材料进行表征，通过吸附动力学和等温吸附模型比较4种复合改性膨润土的除磷性能，并探究投药量和pH对复合改性膨润土除磷除藻的影响。结果表明，4种材料吸附磷的过程均能由准二级动力学模型和Langmuir等温吸附模型描述。其中，PAC-La的磷吸附容量最大(44.677 mg/g);投药量为300 mg/L时，总磷(TP)去除率最高的是PAC-La(94.1%),叶绿素a(Chla)去除率最高的是PFS-La(78.2%);在pH为5～10时，PAC-La除磷除藻效果受pH影响最小。实验结果表明，采用絮凝剂-镧复合改性膨润土能够同步去除富营养化水体中的磷和藻类，尤其是采用PAC-La性能最优。     

共存物质对钢渣除磷的影响

研究了pH、共存离子（Cl^-、NO3^-、SO4^2-、F^-、HCO3^-）和腐植酸对钢渣吸附除磷的影响。结合吸附饱和钢渣上的磷形态分析了产生影响的原因，采用SEM-EDS（扫描电子显微镜-X射线能谱分析）对吸附磷酸盐前后钢渣表面的微观形态特征进行观察。结果表明：钢渣对磷酸盐具有很好的去除效果，吸附饱和钢渣中的磷主要以Ca—P形式存在。钢渣吸附磷酸盐最适初始pH为3～5，高pH抑制Ca—P的生成，对吸附不利。NHf的存在提高了Ca—P含量，从而促进钢渣对磷酸盐的吸附。共存阴离子Cl^-、NO3^-、SO4^2-对钢渣吸附磷酸盐没有影响，但是F^-和HCO3^-明显抑制Ca—P的生成，从而减少了钢渣对磷酸盐的吸附。腐植酸的存在显著抑制了Ca—P和O-P的生成，使钢渣对磷酸盐的吸附量大大减小。     

鼓泡反应器中液相络合催化同时脱硫脱硝的研究

在鼓泡反应器中考察了[Co(en)3]2+同时吸收去除SO2和NO的影响因素,实验结果表明,pH值和脱硫剂种类是影响乙二胺合钴同时脱除NO和SO2的最重要影响因素,烟气中的氧促进乙二胺合钴吸收NO和SO2,烟气中的SO2,CO2和NO2对乙二胺合钴吸收NO具有抑制作用。在实验条件温度为20℃,pH为13.0,[Co(en)3]2+浓度为0.025 mol/L,加入1 g NH3.H2O的脱硝率更好,连续吸收60 min,脱硝率均保持在93.5%,加入NaOH和NH3.H2O的脱硫效果最好。乙二胺合钴络合同时脱除NO和SO2完全可以在一个装置中完成。     

硫酸铝渣去除水中磷研究

分别以蒸馏水和太湖水为例,研究了硫酸铝渣去除水中磷的能力,并分析了其对水体Al3+、SO24-以及pH的影响.结果表明:(1)除太湖水pH为9.0、10.0两种条件外,随着磷平衡浓度的增加,硫酸铝渣除磷量趋于某一定值,其规律符合Langmuir吸附等温式；太湖水pH为9.0、10.0两种条件下,硫酸铝渣除磷量符合Fre...     

Effects of changes in sulfate,ammonia, and nitric acid on particulate nitrate concentrations in the southeastern United States

A thermodynamic equilibrium model, Simulating Composition of Atmospheric Particles at Equilibrium (SCAPE2), was used to investigate the response of fine particulate NO3(-) to changes in concentrations of HNO3, NH3, and SO4(2-) in the southeastern United States. The data consisted of daily, 24-hr time resolution measurements from the Aerosol Research Inhalation Epidemiology Study (ARIES) Jefferson Street (Atlanta) site and five other sites of the Southeastern Aerosol Research and Characterization Project (SEARCH). Reductions of total NH3 (gas-phase NH3 plus particulate NH4(+)), total NO3(-) (HNO3 plus particulate NO3(-)), SO4(2-), or combined total NO3(-) (HNO3 plus particulate NO3(-)) with SO4(2-) were used to estimate the effects of changing emission levels. The conversion of SO2 to SO4(2-) and NO2 to HNO3 involves additional nonlinear reactions not incorporated into the model. For all sites, fine particulate NO3(-) concentrations decreased in response to reductions of either NH3 or total NO3(-), but the particulate NO3(-) decreases were greater for the NH3 reductions than for the total NO3(-) reductions. Particulate NO3(-) concentrations increased in response to reductions of SO4(2-). For the combined reduction (total NO3(-) plus SO4(2-)), the resulting particulate NO3(-) concentrations were on average no different than the base-case NO3(-) levels. Measurements of fine particulate NO3(-) and HNO3 support the modeling conclusions and indicate that particulate NO3(-) formation is limited by the availability of NH3 at most times at all SEARCH sites.     

Inorganic PM2.5 at a U.S. agricultural site

In this study, we present approximately two years (January 1999-December 2000) of atmospheric NH3, NH4+, HCl, Cl-, HNO3, NO3-, SO2, and SO4= concentrations measured by the annular denuder/filter pack method at an agricultural site in eastern North Carolina. This site is influenced by high NH3 emissions from animal production and fertilizer use in the surrounding area and neighboring counties. The two-year mean NH3 concentration is 5.6 (+/-5.13) microg m(-3). The mean concentration of total inorganic PM2.5, which includes SO4=, NO3-, NH4+, and Cl-, is 8.0 (+/-5.84) microg m(-3). SO4=, NO3-, NH4+, and Cl- represent, respectively, 53, 24, 22, and 1% of measured inorganic PM2.5. NH3 contributes 72% of total NH3 + NH4+, on an average. Equilibrium modeling of the gas+aerosol NH3/H2SO4/HNO3 system shows that inorganic PM2.5 is more sensitive to reductions in gas + aerosol concentrations of sulfate and nitrate relative to NH3.     

Acidification of a Solonetzic soil by nitrogenous fertilizers

Annual applications of (NH4)2SO4, NH4NO3 and urea on a Solonetzic soil at 112 kg N/ha for 10 consecutive years reduced pH levels from 5.6 for the check to 4.4, 4.9 and 5.3, respectively for (NH4)2SO4, NH4NO3 and urea. (NH4)2SO4 generated twice as much exchange acidity as NH4NO3 and four times as much as urea. Net extractable cations leached from the Ap horizon closely approximated the amount of exchange acidity generated by (NH4)2SO4 and NH4NO3 fertilizers. The levels of soil extractable Al and Mn were greatly enhanced by (NH4)2SO4 as were plant contents. Similar acidifying effects to that produced by the (NH4)2SO4 occurred when NH4NO3 was applied at 300 kg N/ha annually for 12 consecutive years in another field experiment on the same soil. Liming samples of the field (NH4)2SO4 acidified soils in the greenhouse, significantly increased yields and lowered the Al and Mn contents of the plants to normal levels.     

Characterization of major chemical components of fine particulate matter in North Carolina

This paper presents measurements of daily sampling of fine particulate matter (PM2.5) and its major chemical components at three urban and one rural locations in North Carolina during 2002. At both urban and rural sites, the major insoluble component of PM2.5 is organic matter, and the major soluble components are sulfate (SO4(2-)), ammonium (NH4(+)), and nitrate (NO3(-)). NH4(+) is neutralized mainly by SO4(2-) rather than by NO3(-), except in winter when SO4(2-) concentration is relatively low, whereas NO3(-) concentration is high. The equivalent ratio of NH4(+) to the sum of SO4(2-) and NO3(-) is < 1, suggesting that SO4(2-) and NO3(-) are not completely neutralized by NH4(+). At both rural and urban sites, SO4(2-) concentration displays a maximum in summer and a minimum in winter, whereas NO3(-) displays an opposite seasonal trend. Mass ratio of NO3(-) to SO4(2-) is consistently < 1 at all sites, suggesting that stationary source emissions may play an important role in PM2.5 formation in those areas. Organic carbon and elemental carbon are well correlated at three urban sites although they are poorly correlated at the agriculture site. Other than the daily samples, hourly samples were measured at one urban site. PM2.5 mass concentrations display a peak in early morning, and a second peak in late afternoon. Back trajectory analysis shows that air masses with lower PM2.5 mass content mainly originate from the marine environment or from a continental environment but with a strong subsidence from the upper troposphere. Air masses with high PM2.5 mass concentrations are largely from continental sources. Our study of fine particulate matter and its chemical composition in North Carolina provides crucial information that may be used to determine the efficacy of the new National Ambient Air Quality Standard (NAAQS) for PM fine. Moreover, the gas-to-particle conversion processes provide improved prediction of long-range transport of pollutants and air quality.     

Arsenic(V) removal with a Ce(IV)-doped iron oxide adsorbent

The removal of arsenic(V) by a new Ce-Fe adsorbent was evaluated under various conditions. Under an initial As(V) of 1.0 mg l(-1), the adsorption capacity of the Ce-Fe absorbent was constant around a value of 16 mgg(-1) over a wide pH range (3-7), while a maximum adsorption capacity of 8.3 mgg(-1) was obtained over a narrow pH range around 5.5 for activated alumina, a conventional adsorbent. Kinetics of adsorption obeys a pseudo-first-order rate equation with the rate constant K(ad) as 1.84 x 10(-3) min(-1). The pattern of adsorption of As(V) by the adsorbent fitted well both the Langmuir and Freundlich models. A Langmuir Q(0) of 70.4 mgg(-1) was obtained at an initial pH of 5.0 and temperature of 20 degrees C, significantly higher than those of other adsorbents reported. Phosphate seriously inhibited the removal of As(V) while fluoride did not compete with As(V) even at an F/As molar ratio as high as 30, suggesting that the adsorption sites for As(V) and fluoride were different. Salinity, hardness, and other inorganic anions such as Cl(-), NO(3)(-), and SO(4)(2-) had no apparent effect on As(V) adsorption. Fourier transform infrared spectra of Ce-Fe adsorbent before and after As(V) adsorption demonstrated that M-OH groups plays an important role for As(V) ions removal in the adsorption mechanisms of Ce-Fe adsorbent.     

海水微生物菌群去除铵氮和亚硝酸氮研究

研究了筛选的自养和异养微生物菌群的脱氮效果后发现 ,异养微生物无论是生长还是对NH+ 4 N及NO-2 N的去除都明显好于自养微生物。通过研究 ,培养出了具备很强脱氮能力包含自养和异养菌的混合微生物 ,在细胞干重浓度为0 .4 8g/L的情况下 ,在实验 3h和 5h后 ,可将初始浓度 10 6mg/L的NH+ 4 N和初始浓度 4 9.9mg/L的NO-2 N全部去除。     

改性钢渣吸附氨氮和磷的特性研究

利用钢渣与氢氧化铝以4∶3质量配比混合,在700℃下进行2 h煅烧,得到改性钢渣。通过批次吸附实验,研究了改性钢渣在不同初始pH值、振荡时间和温度下对水溶液中氨氮和磷酸根的吸附情况,进而分析了改性钢渣对氨氮和磷酸根的吸附等温线、热力学和动力学特性。结果表明,改性钢渣脱氮除磷能力比原钢渣显著增强,且最适pH值为4～8。改性沸石对氨氮和磷酸盐的吸附均符合Langmuir等温吸附方程,氨氮(以N计)最大吸附量在10、20和30℃下分别为1.67、2.59和3.24 mg/g,磷酸根(以P计)的最大吸附量在10、20和30℃下分别为1.02、1.19和1.37 mg/g。热力学参数ΔG0、ΔH0和ΔS0表明,该吸附是一个自发、吸热、熵增型反应过程,且磷的吸附是化学吸附为主,氨氮的吸附是以离子交换吸附和物理吸附为主。改性钢渣对磷和氨氮的吸附动力学符合伪二级方程(R2>0.999)。     

The use of ambient measurements to identify which precursor species limit aerosol nitrate formation

A thermodynamic equilibrium model was used to investigate the response of aerosol NO3 to changes in concentrations of HNO3, NH3, and H2SO4. Over a range of temperatures and relative humidities (RHs), two parameters provided sufficient information for indicating the qualitative response of aerosol NO3. The first was the excess of aerosol NH4+ plus gas-phase NH3 over the sum of HNO3, particulate NO3, and particulate SO4(2-) concentrations. The second was the ratio of particulate to total NO3 concentrations. Computation of these quantities from ambient measurements provides a means to rapidly analyze large numbers of samples and identify cases in which inorganic aerosol NO3 formation is limited by the availability of NH3. Example calculations are presented using data from three field studies. The predictions of the indicator variables and the equilibrium model are compared.