用折流式旋转填料床处理含氨废水

采用折流式旋转填料床处理含氮废水,考察了各因素对吹脱率、传质系数及气相压降的影响、实验结果表明：在pH为10左右、温度为20℃、废水中氨质量浓度为10366mg／L、气体流星为160m^3／h、液体流晕为60L／h、转述为800r／min的条件下,吹脱率为92％,传质系数为3．46kmol／（m^3·s）;折流式旋转填料床的气相压降显著低于其他旋转填料床,且湿床压降低于干床压降;获得了折流式旋转填料床的传质系数和气相压降的回归方程,可分别计算折流式旋转填料床的传质系数和气相压降,考察传质性能和流体力学性能。     

两种接触氧化填料处理洗涤剂废水的比较

以某日化企业在生产过程中产生的洗涤剂废水为处理对象,以接触氧化法为核心工艺,比较了悬挂式组合填料和移动床生物膜反应器(MBBR)悬浮填料对洗涤剂废水的处理效果。实验结果表明:悬挂式组合填料和MBBR悬浮填料的挂膜启动时间分别为13,25 d;当悬挂式组合填料反应器的DO为4.0 mg/L时,COD和LAS的去除率分别为84.33%和89.06%;当MBBR悬浮填料反应器的DO为3.0 mg/L时,COD和LAS的去除率分别为82.54%和90.31%;当MBBR悬浮填料反应器的COD容积负荷为0.5~1.3 kg/(m3·d)时,平均COD去除率为83.91%,继续增大COD容积负荷,COD去除率仍能保持在80%以上;MBBR悬浮填料在COD的高效降解及高浓度有机废水的处理方面优于悬挂式组合填料。     

用移动床生物膜反应器处理石化废水

采用悬浮填料移动床生物膜反应器处理石化废水,在水力停留时间大于6h、反应器填料投加率为50％的条件下,出水COD、NH3－N、SS、浊度等均达到国家排放标准,在水力停留时间大于8h时,能达到良好的硝化效果。     

改性填料对移动床生物膜反应器性能的影响

分别选取3种不同柱状悬浮填料,采用两级好氧移动床生物膜反应器处理低浓度化工废水。实验结果表明,在平均有机负荷为1.67 kg/(m~3·d)、废水pH为7.5～7.8、温度为32～33℃、HRT为8 h、第一级反应器DO为0.5～1.0 mg/L、第二级反应器DO为1.5～2.0 mg/L的条件下,A型悬浮填料(添加改性剂和微量元素、φ10 mm×10 mm)、B型悬浮填料(添加改性剂和微量元素、φ25 mm×10 mm)和C型悬浮填料(无添加剂、φ10 mm×10 mm)的COD平均去除率分别为82.2%、81.8%和70.6%。     

升流式厌氧污泥床处理抗生素制药废水

采用升流式厌氧污泥床(UASB)反应器处理抗生素制药废水。实验结果表明:进水COD为9 300mg/L、容积负荷为9.3kg/(m3.d)时,COD去除率仍在80%以上;在COD∶ρ(SO42-)=6、进水ρ(SO42-)为1 500mg/L以下时,COD去除率一直保持在80%以上,SO42-去除率始终在23%以下。SO24-的存在对产甲烷菌影响不大,UASB反应器运行稳定。UASB反应器产沼气的产气率达0.48m3/kg,沼气中甲烷体积分数为68%,二氧化碳体积分数为27%,产甲烷菌具有较高的活性。     

空气流体振荡提升曝气溶氧效率的效果及机制

开发了新型空气流体振荡器用于曝气系统，将进入曝气器的稳定流变为振荡流，以标准氧总传质系数为指标，考察了曝气盘类型、振荡器反馈通道长度、空气流量等因素对曝气溶氧效率的影响，并通过Fluent软件模拟振荡器内部流场，分析振荡原理。结果表明，流体在振荡器内产生稳定附壁现象，控制端对流体的压力作用使其流向产生周期性切换，从而产生流体振荡效果。在振荡器反馈通道长度10.5 cm、空气流量10.0 L/min的条件下，相对于稳定流，三元乙丙橡胶（EPDM）微孔曝气盘振荡流可使标准氧总传质系数提升114.6%。振荡流通过增大气泡密度和减少气泡兼并行为来减小气泡尺寸，振荡流的气泡平均尺寸相较于稳定流降低了42.6%。     

用硅橡胶平板复合膜分离苯酚时总传质系数的影响因素

用硅橡胶平板复合膜处理高浓度含酚废水,测定了体系的总传质系数（Kov）,分析了温度、盐离子强度、跨膜压差（△p）、膜厚度对Kov的影响。实验结果表明：Kov随温度的升高而呈线性增加,传质通量与温度的关系符合Arrhenius方程;当△p〈0．1MPa时,Kov与压力无关;当△p〉0．1MPa时,压差升高可提高传质系数,但会导致膜的致密化;离子强度改变了苯酚在相间的分配系数,进而影响传质过程;膜厚度降低能有效提高膜的Kov;在膜活性皮层厚度4μm、pH12．5～13．0、温度323．15K、废水流量1205mL／min、废水中苯酚质量浓度7．78g/L、无压差和离子强度的条件下,运行8h后,Kov为16．1×10^-7m／s。     

生物膜反应器脱氮性能及其硝化细菌的研究

采用模拟含氮废水对自行设计制作的A/O生物膜反应器进行脱氮性能研究。研究结果表明：在水温为20～23℃、水力停留时间为18h、进水总氮质量浓度为61～78m g/L、曝气量为25L/min、进水COD分别为110～165m g/L和205～272m g/L的条件下,废水的COD去除率均在90%以上,硝化率分别为98%和95%,总氮去除率分别为50%和78%。采用荧光原位杂交技术对反应器各区域中的硝化细菌进行了检测。结果表明,反应器中的硝化菌主要为亚硝化螺菌属和硝化螺菌属,有少量亚硝化单胞菌属和硝化杆菌属存在。亚硝化菌和硝化菌在好氧区数量相对较多,在缺氧区数量相对较少。     

微氧环境两级膨胀颗粒污泥床反应器处理焦化废水

研究了微氧条件下两级膨胀颗粒污泥床反应器对焦化废水的处理。实验结果表明:一、二级反应器的氧化还原电位在0~+15mV和+60~+80mV时系统对COD和NH3-N的去除率均为90%,系统出水COD和NH3-N质量浓度分别为100~150m g/L和20m g/L;在运行过程中未添加碱和碳源的条件下,两级反应器出水硝酸盐氮和亚硝酸盐氮的平均质量浓度分别为5m g/L和144m g/L,说明出水亚硝酸盐积累明显。颗粒污泥微氧条件下的累计产甲烷量比厌氧条件下增加了一倍多。     

转鼓铁碳微电解法预处理液晶废水

采用转鼓铁碳微电解法预处理液晶生产废水,优化了工艺参数,并进行了装置连续运行试验。结果表明:保持转鼓转速2 r/min,在废水pH=2.0、铁碳比(m(铸铁屑)∶m(活性炭))1∶1.5、填料装填率(填料体积与反应器有效容积之比)1∶10、HRT=3 h的优化工艺条件下,废水BOD5/COD由处理前的0.181提高到0.265;电解装置连续运行30 d,COD去除率稳定在40.1%~43.2%之间,且填料未出现板结现象。     

油田高含盐污水雾化蒸发的数值模拟

基于FLUENT软件,对油田高含盐污水的雾化蒸发过程进行了数值模拟,得到了逆流型雾化蒸发塔内的流场分布特性,对比分析了不同操作参数对蒸发效果的影响。结果表明:液滴蒸发速率沿塔体中心轴线自上而下呈加快趋势;进口空气流速与温度是影响液滴蒸发的关键操作参数,提高流速及温度均可加快液滴的蒸发速率;当进口空气流速达到0.4 m/s后,对蒸发速率的影响减弱;当进口空气温度达到313 K后,对蒸发速率的提高作用不大;喷雾锥角的变化对蒸发速率影响不明显;液滴越细化,蒸发速率越快。     

煤燃烧过程中金属元素迁移特性

利用ICP-AES光谱仪对原煤、飞灰和底灰中铝、钾、钙、镁、铁、锰、锌、铜、硒、铬、砷等11种元素的含量进行了分析;对上述元素在煤燃烧过程中的迁移挥发特性进行了讨论,结果是钙、锰、铁挥发性较小,主要沉积在底灰中,而锌、铜挥发性较大,其他元素属于中等挥发性。     

经济社会学视角下的我国环境污染转移问题分析

在阐述环境污染转移的概念及其主要表现形式的基础上。对我国环境污染转移的原因进行了深入分析，并提出了合理可行的解决对策。     

氧气对湿式电晕放电脱硫技术影响的研究

对O2在湿式电迁移烟气脱硫技术中的作用进行了研究，得到在放电电场中O2的存在有利于SO2的荷电迁移的结论。O2浓度的增加可使脱硫效率上升7％，使总脱硫效率接近100％，O2浓度的增加还会大幅度提高SO2电迁移量。     

Photosensitized Oxidation of Cyanide in Aqueous Solutions of Photoactive Modified Hydroxyethylcellulose

Novel water-soluble polymeric photosensitizers based on a natural polymer, naphthalene-modified hydroxyethylcellulose (HENC), were obtained and used for the photooxidation of cyanide. The reaction leads to the formation of cyanate. The process occurs via photoinduced electron transfer from CN⁻ to the naphthalene or naphthoquinone polymeric chromophores. The kinetics of the reaction depend on the degree of substitution of HENC, its concentration, and pH of the solution. The polymers can be easily removed after reaction as prolonged irradiation leads to their photodegradation.     

纳米二氧化钛可见光催化的研究进展

TiO2纳米材料是目前研究最为广泛的光催化纳米材料之一。但TiO2通常只在紫外光下具有光催化活性,严重影响了它的实际应用范围。光敏化作用以及配合物-金属电子转移等途径可将TiO2的光响应范围拓展到可见光区域,成为TiO2光催化领域的研究热点。综述了近年来光敏化作用和配合物-金属电子转移等方法在TiO2可见光催化领域的研究进展,旨在为今后进一步扩大TiO2的实际应用提出新的研究方向。     

Secondary materials transfer from Japan to China: destination analysis

China has been the largest importer of secondary materials for recycling from Japan during the past decade. In this study, we analyzed the transfer of major secondary materials (plastic, steel, copper, and aluminum scrap) from Japan to China. We identified specific destinations for secondary materials, and the characteristics of secondary materials transferred to China. The major destination for the transfer of secondary materials to China is Guangdong province and part of the Huadong area (Shanghai, Zhejiang, and Jiangsu). Most scrap metal imported into China is of low quality. The destinations of most high-quality nonferrous scrap, imported as processed goods on consignment or through the transit improvement trade, are the northeast border provinces, especially Xinjiang Uighur province. The coefficients of specialization for Chinese cities were different from those for the provinces. Guangdong shows an average recycling structure for China. The structure gradually changes from south to north.     

On equilibration of pore water in column leaching tests

Column leaching tests are closer to natural conditions than batch shaking tests and in the last years have become more popular for assessing the release potential of pollutants from a variety of solids such as contaminated soils, waste, recycling and construction materials. Uncertainties still exist regarding equilibration of the percolating water with the solids, that might potentially lead to underestimation of contaminant concentrations in the effluent. The intention of this paper is to show that equilibration of pore water in a finite bath is fundamentally different from release of a certain fraction of the pollutant from a sample and that equilibrium is reached much faster at low liquid-to-solid ratios typical for column experiments (<0.25) than in batch tests with much higher liquid-to-solid ratios (e.g. 2–10). Two mass transfer mechanisms are elucidated: First-order type release (film diffusion) and intraparticle diffusion. For the latter, mass transfer slows down with time and sooner or later non-equilibrium conditions are observed at the column outlet after percolation has been started. Time scales of equilibrium leaching can be estimated based on a comparison of column length with the length of the mass transfer zone, which is equivalent to a Damköhler number approach. Mass transfer and diffusion coefficients used in this study apply to mass transfer mechanisms limited by diffusion in water, which is typical for release of organic compounds but also for dissolution of soluble minerals such as calcite, gypsum or similar. As a conclusion based on these theoretical considerations column tests (a) equilibrate much faster than batch leaching tests and (b) the equilibrium concentrations are maintained in the column effluent even for slow intraparticle diffusion limited desorption for extended periods of time (>days). Since for equilibration the specific surface area is crucial, the harmonic mean of the grain size is relevant (small grain sizes result in high concentrations even after short pre-equilibration of a column). The absolute time scales calculated with linear sorption and aqueous diffusion aim at organic compounds and are not valid for sparingly soluble mineral phases (e.g. metal oxides and silicates). However, the general findings on how different liquid-to-solid ratios and specific surface area influence equilibration time scales also apply to other mass transfer mechanisms.     

Implications of Heterogeneous Chemistry of Nitric Acid for Nitrogen Deposition to Marine Ecosystems: Observations and Modeling

Size resolved particle composition and nitric acid (HNO₃)measurements from the ASEPS'98 experiment conducted in the BalticSea are used to provide observational evidence of substantialgas-particle transfer of oxidized nitrogen (N) compounds in themarine boundary layer. We then focus on the importance ofHNO₃ reactions on sea salt particles in determining spatio-temporal patterns of N dry deposition to marine ecosystems.Modelling results obtained assuming no kinetic or chemical limiton HNO₃ uptake and horizontally homogeneous conditions withnear-neutral stability, indicate that for wind speeds 3.5 – 10 ms^-1 transfer of HNO₃ to the particle phase to formparticle nitrate (NO₃ ^-) may decrease the N depositionvelocity by 50%. We extend this research using the CHEM-COASTmodel to demonstrate that, in a sulphur poor environment undermoderate wind speeds with HNO₃ concentrations representativeof those found in the marine boundary layer, inclusion ofheterogeneous reactions on sea spray significantly reducesmodelled NO₃ ^- deposition in the near coastal zone.     

水夹点技术研究进展

水夹点技术是一种优化企业用水系统、以提高水的重复利用率为目标的过程集成技术。综述了水夹点技术的研究进展,重点介绍了浓度组合曲线法、用水和水源组合曲线法、D—S组合曲线法、新图解目标法、中水道技术、基因算法工具箱等方法,展望了水夹点技术的研究发展趋势。