离子色谱法测定无组织废气中溴化氢浓度

探讨无组织废气中溴化氢的测定方法。采样方法参照环境空气中氯化氢的采样方法,用淋洗液做吸收液,用大型气泡吸收管作收集器,点位设置按照《大气污染物综合排放标准(》GB16297-1996)附录C给出的无组织排放监控点设置方法进行;分析方法使用离子色谱法测定,分离度较高,相对标准偏差为1.7%～1.9%,加标回收率为93.8%～97.6%,溴离子的检测限为0.02μg/ml,当采样体积为60 L时,无组织废气中溴化氢的检出限为0.003 mg/m3。     

液氯泄露环境风险评价

文章以如东易昌化工有限公司为例,按照《建设项目环境风险评价导则》的要求,在对液氯的理化性质及危险性识别的基础上,分别进行了风险识别、伴生/次生危险性分析、源项分析等工作,确定了此次风险评价采用的相关标准,采用导则推荐的多烟团模式进行了事故发生后液氯泄露的环境风险预测和评价,得出了不利气象条件下的事故风险影响范围,求得了最大风险值,并从氯气瓶库及供氯站设置、生产过程等方面提出了相关的风险管理措施。     

新疆部分城市可吸入颗粒物的浓度及粒径分布

采用TH-β10大气颗粒物浓度监测仪,从2011年4-5月在乌鲁木齐、奎屯、阿克苏、库尔勒、喀什、和田市环境监测站采集大气可吸入颗粒物PM2.5、PM5和PM10样品,分析了不同采样点大气颗粒物的质量浓度变化范围及与TSP的相应比值。结果表明,不论是PM2.5、PM5还是PM10,阿克苏市可吸入颗粒物的质量浓度变化幅度较大,其次是库尔勒市,其余采样点在采样期间的浓度变化幅度不大,并且库尔勒、喀什、奎屯、阿克苏四个城市PM5/TSP和PM2.5/TSP的比例大,除喀什、阿克苏的PM10/TSP的比例接近于1之外,其余可吸入颗粒物的浓度均小于TSP;采用显微镜观测成像技术结合血球计数板方法,利用粒径分布函数分析对六个城市的PM10和5个城市的PM2.5颗粒物在不同粒径的分布进行了分析。结果表明,对于PM10而言,阿克苏在dp<0.5的粒径范围内分布函数高达79%、喀什在dp=0.5~0.6μm之间为44%、和田则在dp=1.2~2.2μm出现20%的最大粒径分布函数。就PM2.5而言,库尔勒在dp<0.5、dp=0.5~0.6、0.6~1.2μm区间内的分布函数均为最大值,其值分为79%、50%、50%,可以说明在采样期间,库尔勒市区的颗粒物在粒径小于1.2μm出现的几率更大些,即颗粒物以积聚模态为主。     

我国建设内陆核电站对环境的影响

未来十年我国内陆核电将处在快速增长的阶段,本文以内陆核电站发电原理为基础,考察污染产生种类及成因,探讨我国内陆核电站在正常运营情况下可能对环境产生的影响,并思考发展方向。     

小回流比条件下污泥浓度分区试验研究

用次毫米过滤（sub-milliFiltration,SMF）组件将生物处理系统内的污泥分为高浓度区和低浓度区,使高浓度区保持大量污泥,强化对有机物的去除,使低浓度区污泥浓度满足膜分离的要求.主要验证了小回流比（R为0.5、1.0、1.5、2.0）条件下污泥浓度分区的效果,考察了采用SMF组件后,系统对COD的去除效果,并将各小回流比条件下A、B两区污泥浓度的理论值和实测值做比较.结果表明,在小回流比条件下可实现污泥浓度分区,低浓度区的MLSS在9 g.L-1以下,高浓度区的MLSS在20 g.L-1以上;系统的COD平均去除率超过90%;A、B两区MLVSS的理论值与实测值具有相关性.     

胶州湾及邻近海域表层海水中一氧化氮浓度分布及其影响因素探讨

2011年2～3月利用化学发光法对胶州湾及邻近海域表层海水中一氧化氮(NO)浓度进行了监测.结合水文、化学和生物等要素的同步观测资料,对该海域NO浓度分布及其影响因素进行了探讨.结果表明,胶州湾内表层海水中NO浓度为0.080～0.493 nmol.L-1,平均值为(0.292±0.146)nmol.L-1,胶州湾外NO浓度为未检出～0.435 nmol.L-1,平均值为(0.160±0.130)nmol.L-1.总体来说,胶州湾表层海水中NO浓度呈现出自湾内向湾外递降的分布趋势,陆地径流和人为活动可能对NO浓度的分布造成一定程度的影响.胶州湾及邻近海域表层海水中NO浓度比开阔大洋高1个数量级.周日变化研究表明,NO浓度具有一定的变化特征,最大值出现在15:00,这可能主要受光照的影响.影响NO浓度分布的因素比较复杂,可能主要受亚硝酸盐、光强和pH等因素的影响.结果表明,2011年春季胶州湾及邻近海域表层海水是大气NO的源,通量约为1.09×10-15 mol.(cm2.s)-1.     

Sludge concentration dynamic distribution and its impact on the performance of UNITANK

UNITANK is a biological wastewater treatment process that combines the advantages of traditional activated sludge process and sequencing batch reactor, which is divided into Tank A, B and C. In this study, the sludge distribution and its impact on performance of UNITANK were carried out in Liede Wastewater Plant （WWTP） of Guangzhou, China. Results showed that there was a strong affiliation between Tank A and B of the system in sludge concentration distribution. The initial sludge concentration in Tank A could present the sludge distribution of the whole system. The sludge distribution was mainly influenced by hydraulic condition. Unsteady sludge distribution had an impact on variations of substrates in reactors, especially in decisive reactor, and this could lead to failure of system. Settler could partially remove substrates such as COD and NO3-N, but there was adventure of sludge deterioration. The rational initial sludge concentration in Tank A should be 4000-6000 mg/L MLSS.     

Oxidation inhibition of sulfite in dual alkali FGD system

A laboratory-scale well-mixed thermostatic reactor with continuously blasting air was used to investigate the oxidation inhibition of sulfite in dual alkali flue gas desulfurization （FGD） system. The effects of operating parameters such as pH value and catalyst concentration on the oxidation were studied. Sodium thiosulfate was used in the system, and was found that it significantly inhabited the sulfite oxidation. In the absence of catalyst, sodium thiosulfate at 12.67 mmol/L had an inhibition efficiency of approximately 98%. While in the presence of catalyst, sodium thiosulfate at 26.72 mmol/L had an inhibition efficiency less than 85.0%. The oxidation reaction order of sulfite in the sodium thiosulfate was determined to be -1.90 and 4）.55 in the absence and presence of the catalyst, respectively. Apparent activation energy of oxidation inhibition was calculated to be 53.9 kJ/mol. Pilot tests showed that the consumption rate of thiosulfate agreed well with the laboratory-scale experimental results.     

Degradation of metabolites accumulated of benzo[a]pyrene by coupling Penicillium Chrysogenum with KMnO4

Several main metabolites of benzo[a]pyrene （BaP） formed by Penicillium chrysogenum, Benzo[a]pyrene-1,6-quinone （BP 1,6- quinone）, trans-7,8-dihydroxy-7,8-dihydrobenzo[a]pyrene （BP 7,8-diol）, 3-hydroxybenzo[a]pyrene （3-OHBP）, were identified by high-performance liquid chromatography （HPLC）. The three metabolites were liable to be accumulated and were hardly further metabolized because of their toxicity to microorganisms. However, their further degradation was essential for the complete degradation of BaP. To enhance their degradation, two methods, degradation by coupling Penicillium chrysogenum with KMnO4 and degradation only by Penicillium chrysogenum, were compared; Meanwhile, the parameters of degradation in the superior method were optimized. The results showed that （1） the method of coupling Penicillium chrysogenum with KMnO4 was better and was the first method to be used in the degradation of BaP and its metabolites; （2） the metabolite, BP 1,6-quinone was the most liable to be accumulated in pure cultures; （3） the effect of degradation was the best when the concentration of KMnO4 in the cultures was 0.01% （w/v）, concentration of the three compounds was 5 mg/L and pH was 6.2. Based on the experimental results, a novel concept with regard to the bioremediation of BaP-contaminated environment was discussed, considering the influence on environmental toxicity of the accumulated metabolites.     

次氯酸钠氧化消除水中BPA的影响因素和动力学

采用常用消毒剂次氯酸钠对内分泌干扰物双酚A（BPA）的氧化消除及动力学规律进行研究,考察了加氯量、BPA初始浓度、pH值、Br^-浓度和温度各因素对降解效果的影响.结果表明,次氯酸钠对BPA的氧化降解过程符合拟一级反应动力学;pH值对该降解反应影响较大,当pH为8～9时,BPA与 HOCl的反应速率达到最大为0 .544 3　min^-1;溶液中存在Br^-会加快BPA的降解,并且其整体反应不符合拟一级动力学规律,随着Br^-浓度的增加,BPA降解得越快;温度对该降解反应的影响较大并且符合Van't Hoff规则,提高反应温度,有利于氯对BPA的降解.