期刊文献+
共找到747篇文章
< 1 2 38 >
每页显示 20 50 100
Recycle of Wastewater from Lead-Zinc Sulfide Ore Flo-tation Process by Ozone/BAC Technology 被引量:3
1
作者 Xingyu Liu Bowei Chen +3 位作者 Wenjuan Li Yongsheng Song Jiankang Wen Dianzuo Wang 《Journal of Environmental Protection》 2013年第1期5-9,共5页
Lead-zinc sulphide ore contains lead sulphide (galena), and zinc sulphide (sphalerite). In the first flotation stage, galena is rendered hydrophobic with an organic collector such as xanthate, while sphalerite is kept... Lead-zinc sulphide ore contains lead sulphide (galena), and zinc sulphide (sphalerite). In the first flotation stage, galena is rendered hydrophobic with an organic collector such as xanthate, while sphalerite is kept from floating by depressants, and in the second flotation stage, activator was used to activated zinc flotation. Since the organic regent used are different in the two flotation stage, wastewater from the second zinc flotation stage can’t be directly recycled to the first lead flotation stage. Wastewater from flotation process for concentrating lead-zinc sulphide ore often containing organic compounds such as diethyldithiocarbamate(DDTC), xanthate, terpenic oil(2# oil) and thionocarbamate esters (Z-200), are environmentally hazardous. Their removal from contaminated water and the reuse of the water is one of the main challenges facing lead-zinc sulphide ore processing plants. In this study, synthetic wastewater containing DDTC, xanthate, 2# oil and Z-200 at concentrations ranging from 21 to 42 mg/L was fed into an Ozone/Biological activated carbon (BAC) reactor. Analyses of the effluent indicated a chemical oxygen demand (COD) removal over 86.21% and Total organic carbon (TOC) removal over 90.00% were achieved under Hydraulic retention time (HRT) of 4h and O3 feeding concentration of 33.3mg/L. The effluent was further recycled to the lab scale lead concentrating process and no significant difference was found in compare with fresh water. Furthermore, lead-zinc sulphide mineral concentrating process was carried out at lab scale. The produced wastewater was treated by Ozone/BAC reactor at O3 feeding concentration of 16.7mg/L and HRT of 4h. The effluent analysis showed that TOC removal was 74.58%. This effluent was recycled to the lab scale lead-zinc sulphide mineral concentrating process and the recovery of lead was not affected. The results showed that by using Ozone/BAC technology, the lead-zinc sulphide mineral processing wastewater could be recycled. 展开更多
关键词 Lead-zinc SULPHIDE ore ozone/bac FLOTATION WASTEWATER RECYCLE
暂未订购
Mechanism of Formation of the Ozone Valley over the Tibetan Plateau in Summer-Transport and Chemical Process of Ozone 被引量:16
2
作者 刘煜 李维亮 +1 位作者 周秀骥 何金海 《Advances in Atmospheric Sciences》 SCIE CAS CSCD 2003年第1期103-109,共7页
With the 3D chemical transport model OSLO CTM2, the valley of total column ozone over the Tibetan Plateau in summer is reproduced. The results show that when the ozone valley occurs and develops, the transport process... With the 3D chemical transport model OSLO CTM2, the valley of total column ozone over the Tibetan Plateau in summer is reproduced. The results show that when the ozone valley occurs and develops, the transport process plays the main part in the ozone reduction, but the chemical process partly compensates for the transport process. In the dynamic transport process of ozone, the horizontal transport process plays the main part in the ozone reduction in May, but brings about the ozone increase in June and July. The vertical advective process gradually takes the main role in the ozone reduction in June and July. The effect of convective activities rises gradually so that this effect cannot be overlooked in July, as its magnitude is comparable to that of the net changes. The effect of the gaseous chemical process brings about ozone increases which are more than the net changes sometimes, so the chemical effect is also important. 展开更多
关键词 Tibetan Plateau ozone valley dynamic transport process chemical process
在线阅读 下载PDF
Degradation of 2,4-dichlorophenoxyacetic acid in water by ozonehydrogen peroxide process 被引量:16
3
作者 YU Ying-hui MA Jun HOU Yan-jun 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2006年第6期1043-1049,共7页
This study reports an investigation into the degradation of 2,4-dichlorophenoxyacetic acid in bubble contactor column by O2/H2O2 process, which is widely used as a principal advanced oxidation process. The degradation... This study reports an investigation into the degradation of 2,4-dichlorophenoxyacetic acid in bubble contactor column by O2/H2O2 process, which is widely used as a principal advanced oxidation process. The degradation of 2,4-dichlorophenoxyacetic acid was studied under different H202/O3 molar ratio and pH value. Meanwhile, TOC removal was investigated both in distilled water and tap water. The influences of ozone transfer and consumed hydrogen peroxide were also discussed. The degradation products and oxidation intermediates were identified by GC-MS and LC-MS. A possible reaction mechanism was thus proposed. 展开更多
关键词 2 4-dichlorophenoxyacetic acid ozonE hydrogen peroxide advanced oxidation process
在线阅读 下载PDF
Effect of ozone on the performance of a hybrid ceramic membrane-biological activated carbon process 被引量:12
4
作者 Jianning Guo Jiangyong Hu +2 位作者 Yi Tao Jia Zhu Xihui Zhang 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2014年第4期783-791,共9页
Two hybrid processes including ozonation-ceramic membrane-biological activated carbon (BAC) (Process A) and ceramic membrane-BAC (Process B) were compared to treat polluted raw water. The performance of hybrid p... Two hybrid processes including ozonation-ceramic membrane-biological activated carbon (BAC) (Process A) and ceramic membrane-BAC (Process B) were compared to treat polluted raw water. The performance of hybrid processes was evaluated with the removal efficiencies of turbidity, ammonia and organic matter. The results indicated that more than 99% of particle count was removed by both hybrid processes and ozonation had no significant effect on its removal. BAC filtration greatly improved the removal of ammonia. Increasing the dissolved oxygen to 30.0 mg/L could lead to a removal of ammonia with concentrations as high as 7.80 mg/L and 8.69 mg/L for Processes A and B, respectively. The average removal efficiencies of total organic carbon and ultraviolet absorbance at 254 nm (UV254, a parameter indicating organic matter with aromatic structure) were 49% and 52% for Process A, 51% and 48% for Process B, respectively. Some organic matter was oxidized by ozone and this resulted in reduced membrane fouling and increased membrane flux by 25%-30%. However, pre-ozonation altered the components of the raw water and affected the microorganisms in the BAC, which may impact the removals of organic matter and nitrite negatively. 展开更多
关键词 biological activated carbon ceramic membrane hybrid process ozone
原文传递
Formation processes and source contributions of ground-level ozone in urban and suburban Beijing using the WRF-CMAQ modelling system 被引量:4
5
作者 Shuxian Zhang Zhongzhi Zhang +5 位作者 Yang Li Xiaohui Du Linglu Qu Wei Tang Jun Xu Fan Meng 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2023年第5期753-766,共14页
Beijing faces the challenge of high levels of ozone(O_(3))pollution.In this study,the Weather Research and Forecasting model and Community Multiscale Air Qualitymodel(CMAQ)were used to simulate atmospheric O_(3) conce... Beijing faces the challenge of high levels of ozone(O_(3))pollution.In this study,the Weather Research and Forecasting model and Community Multiscale Air Qualitymodel(CMAQ)were used to simulate atmospheric O_(3) concentrations in Beijing.To investigate the formation mechanisms and source contributions of O_(3) pollution in different regions of Beijing,process analysis and the integrated source apportionmentmethodwithin the CMAQwere applied to O_(3) concentrations in the summer of 2018.The process analysis results showed that vertical diffusion was the major contributor to O_(3) concentrations at all receptor sites in Beijing,at>65.94μg/(m^(3)·hr).Gas-phase chemical reactions consumed a significant amount of O_(3) in urban and inner suburban areas(>−5.57μg/(m^(3)·hr)),while near-surface chemical reactions made positive contributions in outer suburban areas(>4.72μg/(m^(3)·hr)).The O_(3) formation chemical reactions indicated that NO titration,which removes O_(3) at night-time,mainly occurred in urban areas.The weaker chemical reactions occurring near the surface in outer suburbs suggested that suburban-area O_(3) was produced in the upper atmospheric layers and was transported vertically to the lower layers.The O_(3) source apportionment results showed that boundary contributions were the dominant contributor to O_(3) pollution in Beijing(>40%).The contribution of non-local emissions to O_(3) levels was significantly greater in the outer suburbs than in urban and inner suburban areas due to topography.This study increases the understanding of the complex processes of O_(3) formation in different areas of Beijing and informs the implementation of O_(3) control plans. 展开更多
关键词 ozonE Source apportionment process analysis Air quality model
原文传递
Heterogeneous catalytic ozonation by amorphous boron for degradation of atrazine in water 被引量:1
6
作者 Zirong Song Jie Li +3 位作者 Hongxin Xu Yu Li Yaxiong Zeng Baohong Guan 《Chinese Chemical Letters》 SCIE CAS CSCD 2023年第5期408-413,共6页
As one of the most promising and practical advanced oxidation processes(AOPs),the catalytic ozonation is triggered by the active components of catalyst,which are usually derived from metals or metal oxides.To avoid th... As one of the most promising and practical advanced oxidation processes(AOPs),the catalytic ozonation is triggered by the active components of catalyst,which are usually derived from metals or metal oxides.To avoid the metal pollution from catalyst,here the amorphous boron(A-boron)is used as a metalfree catalyst for catalytic ozonation to produce free radicals for effective degradation of atrazine(ATZ),the world-widely used herbicide and also a widespread pollutant in environment.A-boron exhibits an outstanding performance for catalytic ozonation to remove ATZ from water.As A-boron is introduced into ozonation,the degradation efficiency in 10 min is promoted to 97.1%,much higher than that of 15.1%under ozonation.The mechanism is that the B-B bonds and internal suboxide B in A-boron serve as the main active sites to donate electrons to accelerate ozone decomposition to produce reactive oxygen species(ROS),including·O_(2)^(-)and^(1)O_(2),and further enhance ATZ degradation via ROS reactions.Moreover,the A-boron is still highly active with a degradation efficiency of ATZ over 95%in 10 min even after four successive cycles.This work shows A-boron could be an alternative for the active components of metal or metal oxide in catalytic ozonation. 展开更多
关键词 Amorphous boron Catalytic ozonation Reactive oxygen species ATRAZINE Advanced oxidation processes
原文传递
Photocatalytic ozonation-based degradation of phenol by ZnO—TiO_(2)nanocomposites in spinning disk reactor 被引量:1
7
作者 Xueqing Ren Jiahao Niu +5 位作者 Yan Li Lei Li Chao Zhang Qiang Guo Qiaoling Zhang Weizhou Jiao 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2024年第8期74-84,共11页
Spinning disk reactor(SDR)has emerged as a novel process intensification photocatalytic reactor,and it has higher mass transfer efficiency and photon utilization for the degradation of toxic organic pollutants by adva... Spinning disk reactor(SDR)has emerged as a novel process intensification photocatalytic reactor,and it has higher mass transfer efficiency and photon utilization for the degradation of toxic organic pollutants by advanced oxidation processes(AOPs).In this study,ZnO—TiO_(2)nanocomposites were prepared by solgel method,and coated on the disk of SDR by impregnation-pull-drying-calcination method.The performance of catalyst was characterized by X-ray diffraction,scanning electron microscope,X-ray photoelectron spectroscopy,photoluminescence and ultraviolet—visible diffuse reflectance spectroscopy.Photocatalytic ozonation in SDR was used to remove phenol,and various factors on degradation effect were studied in detail.The results showed that the rate of degradation and mineralization reached 100%and 83.4%under UV light irradiation after 50 min,compared with photocatalysis and ozonation,the removal rate increased by 69.3%and 34.7%,and mineralization rate increased by 56.7%and 62.9%,which indicated that the coupling of photocatalysis and ozonation had a synergistic effect.The radical capture experiments demonstrated that the active species such as photogenerated holes(h^(+)),hydroxyl radicals(·OH),superoxide radical(·O_(2)-)were responsible for phenol degradation,and·OH played a leading role in the degradation process,while h+and·O_(2)^(-)played a non-leading role. 展开更多
关键词 Spinning disk reactor Photocatalytic ozonation ZnO-TiO_(2)nanocomposites Advanced oxidation processes
在线阅读 下载PDF
Degradation of Selected Indoor Air Pollutants:Comparison Study of Photocatalytic,Ozone-Assisted Photocatalytic and Amine Adsorption Processes 被引量:3
8
作者 赵文昌 程金平 +1 位作者 陈颖 王文华 《Journal of Shanghai Jiaotong university(Science)》 EI 2012年第1期13-19,共7页
Indoor air pollutants impact human health,comfort and productivity.The method of photocatalysis has been applied mainly in flow reactors and little information is available on indoor air pollutant removal in airtight ... Indoor air pollutants impact human health,comfort and productivity.The method of photocatalysis has been applied mainly in flow reactors and little information is available on indoor air pollutant removal in airtight reactors.In the paper,experiments were carried out to remove formaldehyde(HCHO),ammonia(NH_3) and volatile organic compounds(VOCs)in the airtight and ventilated chambers.Results demonstrated that 90.4%of HCHO,92.3%of NH_3 and 57.9%of VOCs were removed in the amine adsorption process,while 67.5% (hereinbefore,these are the mass fraction)of HCHO,60.0%of NH_3,and 61.2%of VOCs were removed in the photocatalytic process.However,ozone-assisted photocatalytic process showed great potential to degrade indoor air pollutants in the ventilated chamber.Factors and mechanisms of the photocatalytic degradation of HCHO, NH_3 and VOCs were also discussed. 展开更多
关键词 TiO2 photocatalysis ozone-assisted photocatalysis amine adsorption process indoor air pollutants
原文传递
Controlling of crustacean zooplankton reproduction in biological activated carbon (BAC) filters by strengthen operation and management of conventional process
9
作者 刘丽君 张金松 +1 位作者 李小伟 赫俊国 《Journal of Harbin Institute of Technology(New Series)》 EI CAS 2010年第5期661-666,共6页
To counter the mass reproduction and penetration of crustacean zooplankton in Biological Activated Carbon(BAC)filters which may result in the presence of organisms in potable water and water pollution,this paper analy... To counter the mass reproduction and penetration of crustacean zooplankton in Biological Activated Carbon(BAC)filters which may result in the presence of organisms in potable water and water pollution,this paper analyzed the factors affecting organisms' reproduction in BAC filters.A comparative study was performed on the density and composition of crustacean zooplankton of the concerned water treatment units of two advanced water plants(Plant A and B)which with the same raw water and the same treatment technique in southern China.The results obtained show that the crustaceans' density and composition was very different between the sand filtered water of Plant A and Plant B.which Harpacticoida bred sharply in the sediment tanks and penetrated sand filter into BAC filters was the primary reason of crustaceans reproduce in BAC filters of Plant A.For prevention of the organisms reproduction in BAC,some strengthen measures was taken including pre-chlorination,cleaning coagulation tanks and sediment tanks completely,increasing sludge disposal frequency to stop organisms enter BAC filters,and the finished water quality was improved and enhanced. 展开更多
关键词 CRUSTACEAN zooplankton reproduction bac filter CONVENTIONAL treatment process STRENGTHEN operation and management tap water quality
在线阅读 下载PDF
北方低浊微污染原水O_(3)-BAC深度处理效能及机制
10
作者 权晨妍 郭媛 +3 位作者 张昭赫 李家科 刘珊珊 时文歆 《中国给水排水》 北大核心 2025年第23期55-63,共9页
为了探究臭氧-生物活性炭(O_(3)-BAC)深度处理工艺对北方低浊微污染原水的净化效能及其作用机制,选取我国北方某座同步运行常规工艺与O_(3)-BAC深度处理工艺的给水厂作为研究对象,考察了两种工艺在冬季低温、长期低浊和有机微污染的同... 为了探究臭氧-生物活性炭(O_(3)-BAC)深度处理工艺对北方低浊微污染原水的净化效能及其作用机制,选取我国北方某座同步运行常规工艺与O_(3)-BAC深度处理工艺的给水厂作为研究对象,考察了两种工艺在冬季低温、长期低浊和有机微污染的同一水源条件下的净水效果和污染物削减规律,同时分析了细菌群落结构及其变化特征与生物风险。结果表明,O_(3)-BAC深度处理工艺适用于处理我国北方低浊微污染原水,但实际运行效果易受季节更替的影响;在O_(3)-BAC与常规工艺协同作用下,可构建多级屏障以强化对污染物的去除,其中炭滤和砂滤填料上所附着的生物膜在降解有机微污染物中发挥了重要作用,例如Saprospiracea和Blastocatella菌属。 展开更多
关键词 饮用水处理 臭氧-生物活性炭 低浊原水 功能细菌 生物风险
原文传递
Bardenpho工艺用于某污水处理厂提标改造
11
作者 郭强 刘新安 +4 位作者 王社平 高荣宁 孟令八 杨永维 李权 《中国给水排水》 北大核心 2026年第4期126-131,共6页
西安市某污水处理厂总处理规模为40万m^(3)/d,污水处理采用预处理+A/A/O生化反应池+纤维转盘滤池+接触消毒工艺。该污水处理厂毗邻奥体中心等场馆,周边环境敏感,因此本次提标改造工程将出水标准由《城镇污水处理厂污染物排放标准》(GB 1... 西安市某污水处理厂总处理规模为40万m^(3)/d,污水处理采用预处理+A/A/O生化反应池+纤维转盘滤池+接触消毒工艺。该污水处理厂毗邻奥体中心等场馆,周边环境敏感,因此本次提标改造工程将出水标准由《城镇污水处理厂污染物排放标准》(GB 18918—2002)的一级A标准提高至《地表水环境质量标准》(GB 3838—2002)的准Ⅳ类标准,同时进行加盖除臭。将原A/A/O工艺改造为五段Bardenpho工艺,重新划分功能分区;深度处理采用高效沉淀池+V型滤池+臭氧接触池。提标改造工程建成运行以来,出水水质稳定达标,通过加盖除臭、优化景观设计等措施消除了“邻避”效应。 展开更多
关键词 污水处理厂 提标改造 准Ⅳ类标准 Bardenpho工艺 臭氧氧化
原文传递
高级氧化法处理电子工业TMAH废水研究进展
12
作者 张立成 张宇婷 +2 位作者 刘澈 张志磊 冯锴 《现代化工》 北大核心 2026年第4期58-63,共6页
对多种方法处理电子工业TMAH废水进行了综述,包括Fenton法、光催化技术、臭氧氧化法、UV/H_(2)O_(2)工艺以及过硫酸盐活化工艺等。结合活性自由基特征反应机制,TMAH的降解路径被阐明为以逐步去甲基化为主并最终生成NH_(4)^(+)和NO_(3)^... 对多种方法处理电子工业TMAH废水进行了综述,包括Fenton法、光催化技术、臭氧氧化法、UV/H_(2)O_(2)工艺以及过硫酸盐活化工艺等。结合活性自由基特征反应机制,TMAH的降解路径被阐明为以逐步去甲基化为主并最终生成NH_(4)^(+)和NO_(3)^(-)。 展开更多
关键词 四甲基氢氧化铵 高级氧化法 羟基自由基 硫酸根自由基 臭氧氧化
原文传递
O_3/BAC工艺应用于城市污水深度处理 被引量:15
13
作者 蒋以元 杨敏 +3 位作者 张昱 邓荣森 周军 広辻淳二 《中国给水排水》 CAS CSCD 北大核心 2004年第7期92-95,共4页
 为使再生水适合不同用途,对经过混凝沉淀和砂滤处理的再生水进行了臭氧—生物活性炭的深度处理。在臭氧消耗量和反应时间分别为5mg/L和10min,BAC空床停留时间(EBCT)为10min的条件下,臭氧—生物活性炭工艺对CODMn、DOC、UV254和色度平...  为使再生水适合不同用途,对经过混凝沉淀和砂滤处理的再生水进行了臭氧—生物活性炭的深度处理。在臭氧消耗量和反应时间分别为5mg/L和10min,BAC空床停留时间(EBCT)为10min的条件下,臭氧—生物活性炭工艺对CODMn、DOC、UV254和色度平均去除率为32.4%、29.2%、48.6%和80.1%,出水CODMn、DOC、UV254和色度的平均值分别为3.3mg/L、4.0mg/L、0.05cm-1和2.0倍;臭氧生物活性炭工艺出水SDI<4,从而满足了反渗透系统的进水要求。 展开更多
关键词 城市污水 深度处理 再生回用 臭氧氧化 bac SDI
在线阅读 下载PDF
O_3/BAC对氯化消毒副产物的控制作用 被引量:17
14
作者 张金松 张红亮 +4 位作者 董文艺 汪义强 金立建 马军 范洁 《中国给水排水》 CAS CSCD 北大核心 2004年第2期16-20,共5页
采用臭氧化—生物活性炭 (O3/BAC)深度处理工艺去除水中消毒副产物前质的试验结果表明 ,该工艺能够有效去除水中消毒副产物前质 ,可控制氯化消毒副产物的生成 ,其中主臭氧化对三卤甲烷前质和卤乙酸前质均具有很好的去除效果 ,生物活性... 采用臭氧化—生物活性炭 (O3/BAC)深度处理工艺去除水中消毒副产物前质的试验结果表明 ,该工艺能够有效去除水中消毒副产物前质 ,可控制氯化消毒副产物的生成 ,其中主臭氧化对三卤甲烷前质和卤乙酸前质均具有很好的去除效果 ,生物活性炭对卤乙酸前质表现出较好的去除效果 ,但对三卤甲烷前质的去除效果有限 ;藻类、有机物等在滤层的累积使得砂滤池在同一工作周期中的不同阶段对水中三卤甲烷前质的去除效果有所不同 ,因而需要合理设置砂滤池的反冲洗周期。臭氧化—生物活性炭工艺充分发挥了臭氧化和生物活性炭两种技术的优点 ,并相互促进和补充 。 展开更多
关键词 臭氧化 生物活性炭 氯化消毒副产物 三卤甲烷前质 卤乙酸前质
在线阅读 下载PDF
预臭氧-BAC工艺处理微污染原水参数优化与有机物去除特性 被引量:5
15
作者 石晶晶 朱光灿 +1 位作者 戴小冬 吕锡武 《净水技术》 CAS 2014年第5期11-16,共6页
采用中试装置研究了预臭氧-生物活性炭工艺对长江南京段微污染原水有机物的去除特性,考察了臭氧投加量和臭氧接触时间对预臭氧氧化、砂滤及生物活性炭单元中DOC、BDOC、CODMn、UV254和微量有机污染物去除的影响。结果表明当臭氧投加量为... 采用中试装置研究了预臭氧-生物活性炭工艺对长江南京段微污染原水有机物的去除特性,考察了臭氧投加量和臭氧接触时间对预臭氧氧化、砂滤及生物活性炭单元中DOC、BDOC、CODMn、UV254和微量有机污染物去除的影响。结果表明当臭氧投加量为3 mg/L、臭氧接触时间为10 min时,预臭氧氧化单元中DOC、CODMn和UV254的去除率分别达到19%、31%和78%,BDOC增长了33%;砂滤单元四种指标的去除率分别为25%、52%、42%和44%,而生物活性炭滤柱对四种污染物指标的去除率分别为46%、83%、52%和20%,高于常规处理工艺。整个工艺对三种微量有机物(1,2,4-三氯苯、DMP和DEHP)的去除率也分别达到了60%、68.6%和68.8%。与未投加臭氧相比,臭氧的投加有效促进了砂滤和生物活性炭对有机污染物的去除。采用预臭氧-生物活性炭工艺处理微污染长江原水,有效提高了有机污染物的去除效果,可保障出水水质安全。 展开更多
关键词 预臭氧生物活性炭 臭氧投加量 臭氧接触时间 深度处理 微量有机污染物
在线阅读 下载PDF
应用Illumina MiSeq高通量测序技术解析O_3-BAC饮用水处理过程细菌多样性变化 被引量:10
16
作者 葛英亮 于水利 +2 位作者 时文歆 杨帆 漆晴 《食品科学》 EI CAS CSCD 北大核心 2016年第16期223-228,共6页
采用Illumina MiSeq高通量测序技术,对臭氧-生物活性炭水处理工艺过程各单元出水中细菌多样性及丰度进行研究,测序获得196 809条16S r DNA基因序列,归类为38个门,522个属。各样品中细菌多样性分析结果表明:在各处理单元出水中细菌群落... 采用Illumina MiSeq高通量测序技术,对臭氧-生物活性炭水处理工艺过程各单元出水中细菌多样性及丰度进行研究,测序获得196 809条16S r DNA基因序列,归类为38个门,522个属。各样品中细菌多样性分析结果表明:在各处理单元出水中细菌群落具有高度多样性,预臭氧和臭氧氧化处理对水体中细菌多样性及丰度的影响最大,可杀灭一部分属的细菌,可合理控制臭氧浓度杀灭部分耐氯菌;絮凝沉淀和沙滤单元处理对水体中细菌多样性具有恢复效果,使水体中细菌种属进一步增多;在生物活性炭滤池处理后,细菌多样性增加,丰度分布更为均匀,对后期消毒工艺提出了更高的要求。 展开更多
关键词 MI Seq高通量测序 臭氧-生物活性炭 饮用水处理 细菌多样性食品
在线阅读 下载PDF
上向流O_3-BAC工艺处理微污染湖泊水研究 被引量:5
17
作者 张晓健 廖晓斌 +6 位作者 丁根宝 张智翔 董仁杰 谢曙光 汪隽 王成坤 陈超 《给水排水》 CSCD 北大核心 2014年第S1期1-6,304,共6页
以我国华东地区某湖泊水为原水,进行中试规模的上向流臭氧生物活性炭(O3—BAC)工艺研究,考察该工艺去除水中有机物的能力,以及工艺出水的生物稳定性和化学安全性。研究结果表明:该工艺能有效去除有机物、氨氮和消毒副产物前体物,同时能... 以我国华东地区某湖泊水为原水,进行中试规模的上向流臭氧生物活性炭(O3—BAC)工艺研究,考察该工艺去除水中有机物的能力,以及工艺出水的生物稳定性和化学安全性。研究结果表明:该工艺能有效去除有机物、氨氮和消毒副产物前体物,同时能提高出水的生物稳定性。该工艺出水CODMn、UV254和DOC的平均值分别为2.31mg/L、0.034cm-1和1.76mg/L,平均去除率为53.4%、67.3%和65.1%;三卤甲烷,卤乙酸和亚硝胺类副产物生成潜能的平均去除率分别为50.3%,59%和96.6%;AOC平均去除率为54.5%;工艺出水BDOC仅为0.56mg/L;且出水未检出BrO3-。因此,O3—BAC工艺适合处理该湖泊水且出水水质安全。 展开更多
关键词 臭氧活性炭 有机物 消毒副产物 生物稳定性 饮用水
在线阅读 下载PDF
O_3—BAC工艺处理微污染地表水的试验研究 被引量:2
18
作者 战楠 廖日红 +4 位作者 刘操 马宁 申颖洁 刘树才 黄赟芳 《给水排水》 CSCD 北大核心 2010年第S1期97-101,共5页
采用预臭氧—曝气生物活性炭滤池(O_3—BAC)工艺处理低碳源的北运河通州段原水,探讨了该系统的主要工艺参数与各项污染物去除效果的相关性。研究结果表明,臭氧的投加对提高COD_(Cr)和NH_3—N的去除效果均有促进作用,且在投加量3 mg/L、... 采用预臭氧—曝气生物活性炭滤池(O_3—BAC)工艺处理低碳源的北运河通州段原水,探讨了该系统的主要工艺参数与各项污染物去除效果的相关性。研究结果表明,臭氧的投加对提高COD_(Cr)和NH_3—N的去除效果均有促进作用,且在投加量3 mg/L、接触时间30 min时臭氧利用效率最高;在此投加量和接触时间、回流比1:1时,COD_(Cr)和NH_3—N的去除率分别可达42%和94.3%,均高于回流比为0.5:1时,而TN去除率为13.4%,有所降低,投加外碳源和降低好氧单元气水比可使之升高;系统对UV_(254)去除率达到38.8%,其中臭氧接触单元去除率为18.66%,由臭氧氧化特性推断,原水中大分子有机物以芳香族化合物为主。 展开更多
关键词 臭氧 曝气生物活性炭滤池 反硝化滤池 回流比
在线阅读 下载PDF
O_3-BAC深度处理工艺对有机物及三氯乙醛生成潜能的去除 被引量:9
19
作者 蔡广强 卢小艳 +5 位作者 张金松 刘丽君 黄河洵 尤作亮 刘嘉祺 曲颖 《给水排水》 CSCD 北大核心 2017年第12期35-40,共6页
以我国南方某O_3-BAC深度处理工艺水厂为研究对象,对工艺过程中有机物及三氯乙醛生成潜能(CHFP)进行每月一次为期1年的监测,同时对温度较高的夏季水样予以极性分离,以明晰O_3-BAC深度处理工艺对有机物及CHFP的去除能力与工艺过程中有机... 以我国南方某O_3-BAC深度处理工艺水厂为研究对象,对工艺过程中有机物及三氯乙醛生成潜能(CHFP)进行每月一次为期1年的监测,同时对温度较高的夏季水样予以极性分离,以明晰O_3-BAC深度处理工艺对有机物及CHFP的去除能力与工艺过程中有机物的极性变化等。结果表明,O_3-BAC深度处理工艺原水TOC、UV_(254)、CHFP均呈现一定的季节性变化趋势,高温季节(4~9月)相对较高,范围分别为1.03~2.13mg/L、0.024 1~0.053 5cm^(-1)、17.49~41.40μg/L;O_3-BAC深度处理工艺对TOC、UV_(254)、CHFP去除率范围分别为31.54%~58.83%、46.59%~79.53%、46.20%~75.24%,混凝沉淀和BAC单元在去除有机物和CHFP中起主要作用。此外,臭氧化作用增加了亲水性有机物含量使CHFP升高,同时亦强化了BAC单元对CHFP的去除作用。 展开更多
关键词 O3-bac深度处理工艺 有机物 消毒副产物 三氯乙醛生成潜能 去除能力
在线阅读 下载PDF
O_3/BAC工艺中炭滤池pH值调节技术的研究 被引量:3
20
作者 李芳 陆少鸣 林县平 《中国给水排水》 CAS CSCD 北大核心 2013年第17期44-46,50,共4页
针对采用O3/BAC工艺的某自来水厂中炭滤池出水pH值大幅度降低的现象,根据炭滤池pH值变化的关键因素对其调节技术进行了研究,开发出了活性炭滤料原位酸碱改性技术,并从净水效果和经济性两方面对砂滤池前投加烧碱或石灰进行了对比研究。... 针对采用O3/BAC工艺的某自来水厂中炭滤池出水pH值大幅度降低的现象,根据炭滤池pH值变化的关键因素对其调节技术进行了研究,开发出了活性炭滤料原位酸碱改性技术,并从净水效果和经济性两方面对砂滤池前投加烧碱或石灰进行了对比研究。结果表明:先对活性炭进行烧碱浸泡改性,使其pH值平衡点提高至所需值,再在砂滤池前投加石灰调节待滤水pH值至该平衡点左右,经过炭滤池酸碱缓冲后出水pH值维持在该平衡点处,达到了调节pH值的效果,出水COD Mn、NH3-N、浊度等指标均能达标,且水质硬度从90.7 mg/L增加到了178.4 mg/L,对防止给水管网腐蚀有利。 展开更多
关键词 O3 bac工艺 PH值 活性炭 改性
原文传递
上一页 1 2 38 下一页 到第
使用帮助 返回顶部