自来水二氧化氯消毒控制三氯甲烷研究

对自来水二氧化氯消毒控制三氯甲烷形成进行了试验研究 ,二氧化氯预消毒替代预氯化消毒可以降低水中的三氯甲烷 ,预消毒处理后形成三氯甲烷的反应受温度和反应时间的影响。使用二氧化氯与氯配制的混合消毒剂消毒时 ,随二氧化氯含量增加 ,水中的三氯甲烷将明显减少。     

自来水二氧化氯消毒控制三氯甲烷研究

对自来水二氧化氯消毒控制三氯甲烷形成进行了试验研究，二氧化氯预消毒替代预氯化消毒可以降低水中的三氯甲烷，预消毒处理后形成三氯甲烷的反应受温度和反应时间的影响。使用二氧化氯与氯配制的混合消毒剂消毒时，随二氧化氯含量增加，水中的三氯甲烷将明显减少。     

二氧化氯和氯复合消毒剂对城市污水的消毒效果

试验研究了二氧化氯和氯复合消毒剂用于经城市污水处理厂处理后的城市污水消毒的效能 ,结果表明 ,二氧化氯和氯复合消毒剂的使用减低了生成的亚氯酸根离子的浓度 ,增加了残余的二氧化氯的浓度 ,粪大肠菌灭活效果良好。     

自由氯、一氯胺和二氧化氯对饮用水中粪肠球菌的消毒动力学研究

以粪肠球菌为研究对象,研究了自由氯、一氯胺和二氧化氯在不同pH值和温度下的消毒效果,并将灭活速率常数表示为pH和温度的函数,对Chick—Watson模型进行了修正。结果表明,随着pH的上升,自由氯和一氯胺的灭活率减小,二氧化氯的灭活率则增大。温度对一氯胺的影响较小,对自由氯和二氧化氯的影响较显著。修正后含有pH和温度两参数的消毒动力学模型可以很好地模拟消毒过程,增强了模型的通用性。     

二氧化氯和氯复合消毒剂对城市污水的消毒效果

试验研究了二氧化氯和氯复合消毒剂用于经城市污水处理厂处理后的城市污水消毒的效能，结果表明，二氧化氯和氯复合消毒剂的使用减低了生成的亚氯酸根离子的浓度，增加了残余的二氧化氯的浓度，粪大肠菌灭活效果良好。     

反渗透海水淡化水的消毒

反渗透海水淡化是解决水资源危机的一项重要技术。反渗透海水淡化水在饮用水生产过程中需进行消毒以解决微生物污染问题。采用次氯酸钙、二氧化氯和紫外线3种消毒方法,考察了反渗透海水淡化水和自来水的消毒效果,比较了对主要水质指标如pH、硬度和碱度的影响及余氯和余ClO_2的衰减性。结果表明,二氧化氯消毒速率最快,次氯酸钙消毒对水质的影响最大,而紫外线的消毒效果最为稳定。可为反渗透海水淡化水的进一步利用提供依据。     

反渗透海水淡化水的消毒稳定性

采用次氯酸钙、二氧化氯和紫外线3种消毒方法对反渗透海水淡化水进行消毒,综合p H、总溶解性固体(TDS)、余氯、大肠杆菌数等指标研究了消毒剂量和水质随贮水时间的变化。结果表明,消毒剂最佳剂量分别为次氯酸钙5mg·L~(-1),二氧化氯1 mg·L~(-1),紫外线5 m J·cm-2。经次氯酸钙消毒后淡化水的p H和TDS逐渐升高,7 d后基本稳定;而二氧化氯消毒后淡化水的p H略有降低,6 d后基本不变,TDS变化则相反。紫外线消毒后p H和TDS几乎不变,但大肠杆菌容易复活,第7天检出浓度为18 CFU·L~(-1)。     

二氧化氯在饮用水消毒中的应用前景

本文通过二氧化氯(ClO_2)对有机卤代物形成的影响、消毒效果、对健康的影响,以及去除水中污染物的能力和ClO_2发生技术等方面的综合评述,认为二氧化氯在饮用水消毒中的应用前景是乐观的。     

饮用水消毒工艺对病毒的灭活

饮用水中的病毒会引发人体健康风险,故消毒是饮用水生物安全的重要屏障。为了比较不同消毒工艺对病毒的灭活效果,在总结水介质中常见病毒的种类及特性的基础上,围绕当前饮用水处理中广泛应用的消毒工艺(氯、氯胺、臭氧、二氧化氯、紫外线),梳理了各种消毒工艺的原理、影响因素、消毒效果及实际应用中的问题。鉴于消毒工艺进水水质对病毒灭活效果影响较大,且饮用水常规、深度处理工艺均可直接、间接强化对病毒的去除效果,故提出"常规处理+深度处理+消毒"协同高效运行的饮用水多级屏障处理工艺,以有效控制病毒等致病微生物引发的饮用水水质风险。     

在血液透析中心氯和二氧化氯副产物的去除

二氧化氯,因为是一种不形成卤仿的强氧化剂,所以正在成为受欢迎的替代氯的生活给水消毒剂。然而,当二氧化氯用于血液透析治疗中水的消毒时,必须注意,保证充分地除掉那些能够影响病人的全部氧比剂。本例研究探讨了各透析中心为去除二氧化氯、氯及其残留氧化剂所典型使用的水处理工艺的效果。初步数据表明,亚氯酸盐离子和游离氯已被有效去除,但因为二氧化氯和氯酸盐离子在门诊给水或处理间,最后产生的水中根本不能被鉴别,所以测不出它们的去除情况。     

二氧化氯杀灭小球藻

实验研究了二氧化氯投加量、小球藻的初始浓度、pH、有机物和氨氮含量对ClO2杀灭来自于水库水的小球藻的影响,考察了ClO2氧化与混凝工艺结合时去除小球藻的效果并对工艺条件进行优化。结果表明,ClO2在投加量1.1 mg/L下,接触10 min,小球藻的杀灭率为71.93%。小球藻的杀灭率随着ClO2投加量的增大和藻初始浓度的升高而提高,随水中有机物含量的增加而显著降低,氨氮含量对小球藻杀灭的效果影响很小。在酸性条件和碱性条件下,小球藻的杀灭率均随pH升高而急剧下降,而在中性至弱碱性区间内,藻的杀灭率随pH升高而缓慢下降。对于某以小球藻为优势藻的供水水库源水,ClO2氧化与混凝工艺结合,藻的去除率高达98.47%。除藻的最佳工艺条件为：二氧化氯投加量为0.5 mg/L,聚合氯化铝为5 mg/L,二氧化氯与混凝剂同时投加。     

二氧化氯催化氧化处理难降解废水技术的研究

研究了二氧化氯化学氧化体系和二氧化氯催化氧化体系。实验结果表明 :单用二氧化氯化学氧化处理COD为 35 0 0mg/L的酸性大红染料配制废水时 ,最佳反应pH值为 6— 8,氧化剂经济用量为 10 0 0mgClO2 /L废水 ,反应时间为 6 0min ,COD去除率可达 5 0 %左右 ,氧化指数 (COD削减量∶ClO2 投加量 ) =2 .3。当二氧化氯与自制催化剂所组成的催化氧化体系用于对酸性大红染料配制废水的处理时 ,最佳反应pH值为 2左右 ,氧化剂经济用量为 80 0mgClO2 /L废水 ,反应时间为4 5— 6 0min ,COD去除率可达 80 %以上 ,氧化指数 =3.5 ,去除每kgCOD氧化剂费用为 3.7元人民币 ,并且废水的可生化性有很大的提高 ,效果明显优于二氧化氯化学氧化。经济技术评估表明 ,二氧化氯催化氧化法是一种新型高效的处理难降解废水的技术 ,有着广阔的应用前景     

Reduction of perchlorate and nitrate by salt tolerant bacteria

Spent regenerant brine from ion-exchange technology for the removal of perchlorate and nitrate produces a high salt waste stream, which requires remediation before disposal. Bioremediation is an attractive treatment option. In this study, we enriched for salt tolerant bacteria from sediments from Cargill salt evaporation facility (California, USA), the Salton Sea (California, USA), and a high density hydrocarbon oxidizing bacterial cocktail. The bacterial cocktail enrichment culture reduced ClO4- from 500 to 260 mg 1 in 4 weeks. Salt tolerant bacterial isolates from the enrichment cultures and two denitrifying salt tolerant bacteria, Haloferax denitrificans and Parococcus halodenitricans, substantially reduced perchlorate. The highest rate of perchlorate removal was recorded with the isolate, Citrobacter sp.: 32% reduction in 1 week. This bacterium substantially reduced perchlorate in 0-5% NaCl solutions and maximally at 30 degrees C and at an initial pH 7.5. In simulated brines containing 7.5% total solids, the Citrobacter sp. significantly reduced both perchlorate and nitrate with 34.9 and 15.6% reduction, respectively, in 1 week. Coculture of a potent perchlorate reducing, non-salt tolerant (non-saline) bacterium, perclace and the Citrobacter sp. proved most effective for perchlorate removal in the brine (46.4% in 1 week). This study demonstrates that both anions can be reduced in treatment of brines from ion exchange systems.     

高浓度钻井废水的混凝-催化氧化处理

以华北油田某深井的高浓度钻井废水(COD高达14 460.0 mg/L)为研究对象,提出了酸化-混凝-催化氧化-吸附的组合处理工艺。重点研制了钻井废水催化氧化处理催化剂(镍基催化剂),通过实验确定了最佳工艺参数条件。着重考察了催化氧化处理的工艺条件,在pH值为4,次氯酸钙投加量为4.4 g/L,催化剂投加量为1.6 g/L的条件下COD降至403.5 mg/L,进一步吸附处理后COD降至139.9 mg/L、色度为30倍、石油类含量为3.8 mg/L、pH为8.0和SS浓度为52mg/L,最终出水水质达到《污水综合排放标准》(GB 8978-1996)二级标准,处理成本为84.8元/m3。     

The formation and control of disinfection by-products using chlorine dioxide

In this study, chlorine dioxide (ClO2) was used as an alternative disinfectant with vanillic acid, p-hydroxybenzoic acid, and humic acid as the organic precursors in a natural aquatic environment. The primary disinfection by-products (DBPs) formed were trihalomethanes (THMs) and haloacetic acids (HAAs). Under neutral conditions (pH = 7) for vanillic acid, more total haloacetic acids (THAAs) than total trihalomethanes (TTHMs) were found, with a substantial increase during the later stages of the reaction. In the case of p-hydroxybenzoic acid, the amount of THAAs produced was minimal. Raising the concentration of ClO2 was not favorable for the control of THAAs in low concentrations of vanillic acid. ClO2 could reduce the total amount of TTHMs and THAAs for higher concentration of vanillic acid. It was found that the humic acid treatment dosage was not significant. Under alkaline conditions (pH = 9), the control of TTHMs and THAAs for the treatment of vanillic acid was better and more economical, however, an appreciable amount of inorganic by-products were observed. Under the same alkaline condition, the control of THAA for the treatment of p-hydroxybenzoic acid was not beneficial and for the treatment of humic acid was not significant.     

聚合硫酸铁/高锰酸钾/二氧化氯组合工艺用于聚氯乙烯废水回收的工程化研究

采用聚合硫酸铁复配高锰酸钾混凝结合二氧化氯氧化的组合工艺成功解决了某厂聚氯乙烯生产废水回收工艺CODMn不达标问题。工程运行结果表明,当原水CODMn=30～48 mg/L,浊度=25～46 NTU时,在CFe=16.8 mg/L,CKMnO4=45 mg/L,CClO2=20 mg/L的条件下,出水CODMn<10 mg/L,浊度<0.5 NTU,达到工业循环补给水的水质要求。     

在线酸度计监测系统研制

分析了温度对连续在线监测锅炉水的pH及其他离子浓度监测的影响，提出了相应的解决办法，并具体介绍了在线酸度计监测系统的硬件、软件组成及处理电路的设计。该系统为锅炉的安全生产与自动控制提供了条件。     

Microbial perchlorate reduction with elemental sulfur and other inorganic electron donors

ClO(4)(-) has recently been recognized as a widespread contaminant of surface and ground water. This research investigated chemolithotrophic perchlorate reduction by bacteria in soils and sludges utilizing inorganic electron-donating substrates such as hydrogen, elemental iron, and elemental sulfur. The bioassays were performed in anaerobic serum bottles with various inocula from anaerobic or aerobic environments. All the tested sludge inocula were capable of reducing perchlorate with H2 as electron donor. Aerobic activated sludge was evaluated further and it supported perchlorate reduction with Fe(0) and S(0) additions under anaerobic conditions. Heat-killed sludge did not convert ClO(4)(-), confirming the reactions were biologically catalyzed. ClO(4)(-) (3mM) was almost completely removed by the first sampling time on d 8 with H2 (> or = 0.37mMd(-1)), after 22d with S(0) (0.18mM d(-1)) and 84% removed after 37d with Fe(0) additions (0.085mMd(-1)). Perchlorate-reduction occurred at a much faster rate (1.12mMd(-1)), when using an enrichment culture developed from the activated sludge with S(0) as an electron donor. The enrichment culture also utilized S(2-) and S(2)O(3)(2-) as electron-donating substrates to support ClO(4)(-) reduction. The mixed cultures also catalyzed the disproportionation of S(0) to S(2-) and SO(4)(2-). Evidence is presented demonstrating that S(0) was directly utilized by microorganisms to support perchlorate-reduction. In all the experiments, ClO(4)(-) was stoichiometrically converted to chloride. The study demonstrates that microorganisms present in wastewater sludges can readily use a variety of inorganic compounds to support perchlorate reduction.     

改性松针对水体中铅(II)的吸附

探讨了改性松针(GXLsp)作为吸附剂对水体中铅离子的吸附性能,考察了吸附时间、溶液pH值、吸附剂用量、盐离子浓度、Pb(II)初始浓度及温度对改性松针吸附Pb(II)的影响。利用Langmuir和Freundlich等温线模型对实验数据进行非线性拟合分析,结果表明,Freundlich等温线模型能很好地描述松针对Pb(II)的吸附过程。热力学参数表明吸附是一个自发的吸热过程。改性松针对铅的吸附行为符合拟二级动力学方程,表明吸附过程是以化学吸附为主。在293K时松针对Pb(II)的饱和吸附量为318.3 mg/g,因此,GXLsp可作为一种高效低值生物质吸附剂以去除水体中重金属Pb(II)的污染。