废气处理工艺条件对二噁英类污染物排放浓度的影响

通过对医疗废物焚烧炉不同处理工艺条件下二噁英排放浓度的比较,揭示了降低二噁英排放的关键因素。控制合适的一燃室炉膛及二燃室炉膛温度,烟气在二燃室内停留时间不低于2 s,保证焚烧炉的含氧量在6%～10%之间,从而达到控制二噁英类前驱物的多相催化合成;减少由于积灰导致受热面积降低,延长烟气的降温时段,从而导致二噁英类污染物的二次合成;采用透气性好、过滤效率高、反吹及清灰后不改变孔隙的布袋及有效的活性碳脱除二噁英。     

火焰原子吸收分光光度法与石墨炉原子吸收分光光度法测定环境空气中铅的对比研究

分别采用火焰原子吸收分光光度法和石墨炉原子吸收分光光度法测定标准样品和环境空气中的铅,并进行了对比分析。结果表明,两种方法都具有较高的准确度和精密度,无显著性差异。     

云南省火电行业SO2产排污系数核算研究

本地化的排放因子研究对污染物的准确核算具有重要意义.因此,本文根据2009年云南省火电行业的生产现状及SO2排放情况,采用实测法与物料衡算法相结合的方法,核算出云南省火电行业的SO2产排污系数,同时给出特定工艺及规模下的SO2产排污系数;并将所得系数与《第一次全国污染源普查工业污染源产排污系数手册》(以下简称《手册》)、环境统计的相关系数进行比较.结果表明,云南省火电行业的SO2产污系数为19.64kg·t-1(以每t原料中的SO2计,下同),排污系数为2.98～7.45kg·t-1.与《手册》比较得知:本研究中煤粉炉工艺≥600MW机组的产污系数较小;51～300MW机组及≤50MW机组的产污系数与《手册》的相符;本研究中煤粉炉工艺≥600MW机组和51～300MW机组的排污系数低值均比《手册》中的大;《手册》中循环流化床锅炉工艺机组的产排污系数在本研究的产排污系数区间内.与环境统计系数比较,两者产污系数基本相符,环境统计排污系数在本研究的排污系数区间内.     

A review of removal technology for antimony in aqueous solution

Antimony (Sb) and its compounds, toxic metalloid, have been classified as high-priority pollutants. Increasing Sb released into the water environment by natural processes and anthropogenic activities, which exposure threatens to human health and ecosystems. Therefore, it is of unquestionable importance to remove Sb from polluted water. Keeping in view the extreme importance of this issue, we summarize the source, chemistry, speciation, distribution, toxicity, and polluted situation of Sb about aqueous solution. Then, we provide the recent and common technology to remove Sb, which are based on adsorption, coagulation/flocculation, electrochemical technology, membrane technology, ion exchange, etc. In this review, we focus in detail on the adsorption method, researchers at present have been investigating to discover more advanced, cost-effective, eco-friendly, reusable adsorbents. However, to date the Sb-containing wastewater treatment technologies are not sufficiently developed and most of research have been tested only in controlled lab conditions. Few reports are available that include field studies and applications. We critically analyzed the salient features and removal mechanisms, evaluating benefits and limitations of these technologies, hoping to provide more references for further research. Finally, we considered the Fe- or Mn-based technologies was the most promising technique to remove Sb for field application.     

Formation process and mechanism of humic acid-kaolin complex determined by carbamazepine sorption experiments and various characterization methods

To explore the formation process and mechanism of organic matter and organic-mineral complex under humification and mineralization conditions, a series of samples including humic acid, kaolin, and humic acid-kaolin complex were prepared using a subcritical water treatment method(SWT) under specific temperature, pressure and reaction time conditions. HA was used as a surrogate for natural organic matter because it has a similar abundant pore structure,variety of carbon types, and chemical components. These samples were used in carbamazepine(CBZ) sorption experiments and characterized by a variety of techniques. The polymerization of humic acid under the conditions of increased temperature and pressure resulted in an increase in specific surface area and molecular quantity. In addition, the degree of aromaticity rose from59.52% to 70.90%. These changes were consistent with the transformation from ‘soft carbon' to‘hard carbon' that occurs in nature. The results of sorption experiments confirmed the interaction between humic acid and kaolin from the difference between the predicted and actual Qevalues. The conceptual model of humic acid-kaolin complex could be deduced and described as follows. Firstly, the aromatic components of humic acid preferentially combine with kaolin through the intercalation effect, which protects them from the treatment effects.Next, the free carboxyl groups and small aliphatic components of humic acid interact on the surface of kaolin, and these soft species transform into dense carbon through cyclization and polymerization. As a result, humic acid-kaolin complex with a mineral core and dense outer carbonaceous patches were formed.     

水体突发污染事件的在线生物监测技术研究进展

水体突发性污染事件的污染方式具有多样性,污染物种类具有复杂性。水体突发污染事件的特征决定在线生物监测的难度。结合受试生物种类和生物生理生态指标的不同,综合分析了已经报道的水体污染在线生物监测技术。根据统计分析结果,已经报道的水体突发性污染在线生物监测技术主要分为:基于生物行为变化的在线生物监测技术、基于生物生理变化的在线生物监测技术和基于综合生物指标的在线生物监测技术3类。在不同生物种类和生理生态指标分析基础上,对不同在线生物监测技术的基本原理和优缺点进行分析,也对不同在线生物监测技术存在的缺点提出解决的主要方案,为水体突发污染事件监测分析提供支持,以满足水体突发污染事件的在线监测和应急管理需求。     

微生物絮凝剂的发酵培养和诱变研究

对粪产碱杆菌B-20进行发酵培养,观察菌株生长与絮凝剂积累、絮凝性、糖类物质消耗和氧浓度之间的关系,发现菌株的生长与絮凝剂的积累呈正相关,并且发酵培养过程中pH保持在7.2～7.9.通过热诱变获得能够稳定传代的B-2022突变菌株,比较了在不同pH、CaCl2添加量、菌液添加量以及不同温度条件下,其与原菌株B-20的发酵混合液的絮凝率差异,发现热诱变菌株B-2022具有更好的絮凝性能,尤其对pH的适应性较强,最优的絮凝条件为pH=9.0、100 mL高岭土悬浮液中1%(质量分数)CaCl2和发酵混合液添加量都为4 mL.进一步将热诱变菌株B-2022紫外诱变45 s,得到紫外诱变菌株B-2022c,其最佳絮凝率可达94.3%,比原菌株B-20和热诱变菌株B-2022的最佳絮凝率分别提高了2.4%和1.7%.通过化学法、紫外分光光度法和红外分光光度法测得絮凝剂的主要化学成分为糖类物质.     

典型产业集聚区地下水优先控制污染物筛选

为明确地下水污染高风险区环境管控目标,快速识别优先控制污染物,于2022年以典型产业集聚区为研究对象,利用污染源产排污状况和地下水基础环境状况调查结果,将污染评价和环境风险相结合,优选污染源超标率、地下水环境污染等级、生物毒性参数和环境迁移转化参数作为筛选因子,利用层次分析法和综合分析法,计算各污染指标综合得分,建立筛选地下水优先控制污染物的方法体系。筛选结果显示,该产业集聚区的优先控制污染物相关指标包括：硝酸盐、耗氧量、石油类、总硬度、亚硝酸盐、镍、锌、硫酸盐、甲苯、氨氮等。筛选结果与园区主导行业产排污特征和地下水质量现状相符,具有一定的可靠性,可为科学、精准管控高风险区地下水质量提供依据。     

基于风险的Football组合法在筛选农用地优先控制酞酸酯类污染物的应用

为探索建立农用地优先管控酞酸酯类有毒有害化学物质的筛选方法,基于Football组合法开展了相关研究。结果表明,邻苯二甲酸二丁酯(DBP)、邻苯二甲酸二(2-乙基己基)酯(DEHP)、邻苯二甲酸二异丁酯(DIBP)、邻苯二甲酸丁基苄基酯(BBP)和邻苯二甲酸二乙酯(DEP)等5种酞酸酯类内源污染物潜在风险较高,将筛选结果与国内外管控化学物质名单进行比较分析,表明Football组合法可用于筛选农用地优先控制酞酸酯类有毒有害物质。     

上海郊区表层土壤中DDT残留特征

为掌握上海市北部郊区农田表层土壤有机氯农药残留状况,在上海市宝山区的农田分布区域布设采样点,采集表层土壤样品,用美国EPA方法分析了土壤中DDT及其4种衍生物的残留量.结果表明,上海市宝山区农田土壤中平均DDT总残留量为0.057 mg·kg-1,DDT的4种衍生物p,p'-DDE,p,p'-DDD,p,p'-DDT,o,p'-DDT的平均残留量分别为0.032、0.007、0.018、0.000 mg·kg-1.该研究中大部分区域土壤DDT总残留量低于国家土壤环境质量二级标准限值,没有形成土壤DDT污染;但在DDT残留量最高的地块,土壤DDT总残留量达0.694 mg·kg-1,超过了国家土壤环境质量二级标准限值,形成了一定范围的土壤DDT污染.在所有采样点中,有4个点位的p,p′-DDT/p,p′-DDE比值大于1,且其DDT总残留量也较高,说明这几块区域村在禁用期间又被新施加了DDT的可能.该研究可为有针对性地开展区域土壤环境保护和污染防治提供重要参考依据.