污泥活性炭强化SBR法处理垃圾渗滤液的实验研究

为了进一步处理垃圾渗滤液,试验采用污泥活性炭强化序批式间歇反应器（SBR）法进行处理,通过对比普通SBR法试验,得出投加污泥活性炭强化SBR法处理垃圾渗滤液的效果要远远高于普通SBR法。当污泥活性炭的投加量为1.2 g/L,容积负荷为0.5～1.5 kg BOD₅/(m³·d)时,进水1 h,曝气10 h,沉淀1.5 h,闲置1.5 h,处理效果最好,COD的去除率达到了85%,NH³-N的去除率达到了90%。     

对苯二甲酸生产废水回用实验研究

采用高级氧化工艺对对苯二甲酸生产废水进行处理,系统考察了氧化剂投加量、废水pH等对处理效果的影响,得出了最佳工艺条件。经过处理的PTA废水,水质达到了车间用水的要求。本方法具有处理效果好、操作简单和环境友好等优点。     

含磁粉生物反应器处理苯酚废水

采用含磁粉生物反应器对质量浓度为120～350 mg/L的苯酚模拟废水进行强化生物处理.实验结果表明:添加适量磁粉可使废水中DO提高约10%;与不含磁粉生物反应器比较,含磁粉生物反应器工艺使填料挂膜时间缩短1～2 d,填料上附着微生物量增多;质量浓度为350 mg/L的苯酚模拟废水在20 h内的苯酚去除率可达80%,降解时间缩短了10 h.初步分析了添加磁粉提高生物反应器处理废水效率的机理.实验证实了含磁粉生物反应器工艺的合理运用是强化处理含酚废水的有效途径.     

NaCl和KCl对厌氧污泥抑制的动力学研究

在厌氧颗粒污泥和厌氧絮状污泥系统中,进行盐质量浓度(NaCl或KCl质量浓度,下同)对厌氧污泥抑制动力学的研究,得到不同拟合的COD降解动力学方程及参数.实验结果表明:当盐质量浓度为10～30 g/L时,KCl对厌氧污泥的COD比降解速率的抑制程度大于NaCl;当盐质量浓度由0 g/L增至10 g/L时,半速率常数逐渐增加;当盐质量浓度由10 g/L增至30 g/L时,半速率常数逐渐减小;在厌氧污泥系统中,NaCl抑制作用下的盐抑制常数高于KCl,且颗粒污泥的盐抑制常数高于絮状污泥.     

改性高岭土处理含酸性媒介染料的印染废水

用十六烷基三甲基溴化铵(CTMAB)改性的高岭土处理以水溶性酸性媒介染料为主的印染废水.实验结果表明,当CTMAB-高岭土加入量为0.6 g/L、用石灰乳控制废水pH为9.5～10.0、聚丙烯酰胺的加入量为2.0 mg/L时,废水的处理效果最佳,废水色度和COD去除率分别达到98.0%和92.0%以上,出水色度和COD达到了GB4287-92<纺织染整工业水污染物排放标准>一级排放标准.     

煤基活性炭生产与再生研究

对煤基活性炭生产过程中的炭化、活化机理进行了简单的论述,分析了制备工艺中影响煤基活性炭质量的各种因素,从经济和环保角度出发,介绍了活性炭再生及其评价方法.最后,根据活性炭应用领域的不断扩大,介绍了我国活性炭生产的发展趋势..     

电子废物回收处理项目的BOT建设方式初探

在综合概述目前我国电子废物环境管理困境及其障碍性因素的基础上,提出了按BOT（建设-运营-转让）建设方式规划电子废物回收处理项目的建议,简述了BOT目方式的基本特征和项目实施过程中值得商榷的几个问题。     

泡沫分离法处理含Cr~(6+)废水

采用间歇式泡沫分离法处理含Cr~(6+)废水,考察了各因素对Cr~(6+)去除效果的影响。通过正交实验分析确定的废水处理最佳工艺条件:废水pH 4.00,气体流量0.90 L/min,阳离子表面活性剂加入量300 mg/L。进水Cr~(6+)质量浓度为10 mg/L时,间歇运行的Cr~(6+)去除率为97.80%,连续运行的Cr~(6+)去除率为95.89%,出水均可达标排放。动力学实验结果表明,泡沫分离法去除Cr~(6+)的过程符合一级动力学的特征。对泡沫分离柱放大后的废水连续流实验分析结果表明,泡沫分离Cr~(6+)的效果比较稳定,但分离设备对废水处理效果有一定的影响。     

Experimental Study of the Criteria of Flow Laminarization in Two-Dimensional Dense Gas Plumes

Laminarization of flow in a two-dimensional dense gas plume was experimentally investigated in this study. The plume was created by releasing CO₂ through a ground-level line source into a simulated turbulent boundary layer over an aerodynamically rough surface in a meteorological wind tunnel. The bulk Richardson number (Ri_*), based on negative plume buoyancy, plume thickness, and friction velocity, was varied over a wide range so that the effects of stable stratification on plume laminarization could be observed. A variety of ambient wind speeds as well as three different sizes of roughness arrays were used so that possible effects of roughness Reynolds number (Re_*) on plume laminarization could also be identified. Both flow visualization methods and quantitative measurements of velocity and intermittency of turbulence were used to provide quantitative assessments of plume laminarization.Flow visualization provided an overall picture of how the plume was affected by the negative buoyancy. With increasing Ri_*, both the plume depth and the vertical mixing were significantly suppressed, while upstream propagation of the plume from the source was enhanced. The most important feature of the flow revealed by visualization was the laminarization of flow in the lower part of the plume, which appeared to be closely related to both Ri_* and Re_*.Measurements within the simulated dense gas plumes revealed the influence of the stable stratification on mean velocity and turbulence intensity profiles. Both the mean velocity and turbulence intensity were significantly reduced near the surface; and these reductions systematically depended on Ri_*. The roughness Reynolds number also had considerable influence on the mean flow and turbulence structure of the dense gas plumes.An intermittency analysis technique was developed and applied to the digitized instantaneous velocity signals. It not only confirmed the general flow picture within the dense plume indicated by the flow visualization, but also clearly demonstrated the changes of flow regime with variations in Ri_* and Re_*. Most importantly, based on this intermittency analysis, simple criteria for characterizing different flow regimes are formulated; these may be useful in predicting when plume laminarization might occur.     

近十年生态工程在中国的进展

我国生态工程近 1 0多年有进一步发展 ,研究和应用对象扩展为社会 -经济 -自然复合生态系统 ,目标明确为可持续发展 ,从追求一维的经济增长或环境与自然保护 ,走向富裕、健康、文明三维一体的复合生态繁荣。在充实“整体、协调、循环、自生”的生态工程原理和生态控制论的基础上 ,总结出生态工程设计的 8项原则。方法论发展为从物理过程的量化走向生态过程的序化 ,从工程结构的优化走向生态格局的进化 ,从机器的人工智能走向人的生态智能。技术路线发展了硬件、软件、心件耦合 ;多学科、多技术的系统组合 ;调控复合生态系统全生态过程 ;寓环境保护于生产和消费中 ,寓废弃物处理于利用中 ;结构和功能纵横耦合成食物链网式、生命周期式、生态系统式等网络结构