A semipermeable membrane equilibrator for halomethanes in seawater

An equilibrator for sampling the partial pressures of halomethanes in seawater was designed and built, incorporating semipermeable membrane tubing to carry the gas phase. The equilibrator was tested for its ability to equilibrate chloromethane, bromomethane, iodomethane, and CFC-11. The residence time required for these halomethanes to equilibrate in the tubing (30 to 60 s) was determined experimentally. In a laboratory test, concentrations calculated from equilibrator measurements and based on published solubility values were found to differ by 6% to 16% from concentrations measured with a purge-and-trap apparatus, but uncertainties in the solubility values are likely to contribute significantly to the differences. In a comparison at sea, no significant difference was found between the semipermeable membrane equilibrator and another, more conventional equilibrator, except a 1.3% difference for CFC-11. This study demonstrates the feasibility of using semipermeable membranes in this and related applications.     

旋转流膜生物反应器特性的探索

通过人工配水方式对旋转切向流膜生物反应器与一体式膜生物反应器在CODCr去除率、NH3 N去除率、膜透水性能等方面进行了对比试验 ,研究表明虽然二者在有机物去除方面相差不大 ,但前者膜抗污染能力强、透水量大。     

Assessment of the Usefulness of Semipermeable Membrane Devices for Long-Term Watershed Monitoring in an Urban Slough System

Semipermeable membrane devices (SPMDs) were deployed at eight sites within the Buffalo Slough, near Portland, Oregon, to (1) measure the spatial and seasonal distribution of dissolved polycyclic aromatic hydrocarbon (PAH) and organochlorine (OC) compounds in the slough, (2) assess the usefulness of SPMDs as a tool for investigating and monitoring hydrophobic compounds throughout the Columbia Slough system, and (3) evaluate the utility of SPMDs as a tool for measuring the long-term effects of watershed improvement activities. Data from the SPMDs revealed clear spatial and seasonal differences in water quality within the slough and indicate that for hydrophobic compounds, this time-integrated passive-sampling technique is a useful tool for long-term watershed monitoring. In addition, the data suggest that a spiking rate of 2–5 μg/SPMD of permeability/performance reference compounds, including at least one compound that is not susceptible to photodegradation, may be optimum for the conditions encountered here.     

聚四氟乙烯覆膜滤料的特性与应用

介绍了覆膜滤料的特性与应用,覆膜滤料与传统滤料相比较所具有的优点.提出在许多复杂的烟气治理中应大力推广使用覆膜滤料以满足生产要求和达到日益严格的环保排放标准,从而改善环境质量,节能降耗.     

消毒技术去除饮用水中病原微生物的研究进展

饮用水中存在着不同种类的病原微生物,这些病原微生物给人体健康带来危害。本文简要介绍常规消毒技术去除饮用水中病原微生物的研究现状;常规消毒剂仍然是现代饮用水处理工艺使用的主要消毒剂;近些年来,对常规消毒剂联合消毒的协同作用和联合消毒剂的概念提出了探讨,认为联合消毒荆是今后饮用水去除病原微生物的发展趋势;膜技术这种物理消毒技术,由于其高效性而得到广泛关注,膜消毒去除病原微生物也成为当今消毒技术研究的热点。     

渗透汽化复合膜分离废水中的低浓度甲醇

采用两种商品化渗透汽化复合膜--GKSS-GS膜和PDMS-P膜分离模拟低浓度甲醇废水,考察了操作温度、甲醇质量分数、废水流量对膜渗透汽化性能的影响.实验结果表明:随温度升高、废水中甲醇质量分数的增大,两种膜的渗透通量都呈增加趋势;GKSS-GS膜的分离系数变化较明显,而PDMS-P膜的分离系数变化较小;废水流量对渗透通量和分离系数的影响均较小.在最佳条件下,GKSS-GS膜的渗透通量为914.6 g/(m~2·h),分离系数为5.6;PDMS-P膜的渗透通量为1 887.2 g/(m~2·h),分离系数为4.8.     

TiO_2/GeO_2复合膜光催化氧化处理活性蓝染料废水

自制了一种新的TiO_2/GeO_2复合膜光催化氧化反应器,研究了该反应器对经臭氧氧化处理后的活性蓝染料废水的光催化氧化降解过程.在过氧化氢加入量为400 mg/L、光照120 min的条件下,COD去除率可达92.5%,处理后废水COD为39.4 mg/L,达到GB8978-1996<污水综合排放标准>.     

两级过滤膜生物反应技术在中水深度处理中的应用

分析了国内外城市中水深度处理回用技术的应用现状,系统介绍了自主研发的以膜法工艺为核心的中水深度处理回用新技术——两级过滤膜生物反应技术（DF—MBR）,对其基本原理、技术优势及工程应用情况进行了介绍,工程实践及其运行效果表明,该技术具有广阔的市场应用前景和推广价值。     

Lysosomal enlargement and lysosomal membrane destabilisation in mussel digestive cells measured by an integrative index

Lysosomal responses (enlargement and membrane destabilisation) in mussel digestive cells are well-known environmental stress biomarkers in pollution effects monitoring in marine ecosystems. Presently, in laboratory and field studies, both responses were measured separately (in terms of lysosomal volume density - Vv - and labilisation period -LP) and combined (lysosomal response index - LRI) in order to contribute to their understanding and to develop an index useful for decisions makers. LRI integrates Vv and LP, which are not necessarily dependent lysosomal responses. It is unbiased and more sensitive than Vv and LP alone and diminishes background due to confounding factors. LRI provides a simple numerical index (consensus reference = 0; critical threshold = 1) directly related to the pollution impact degree. Moreover, LRI can be represented in a way that allows the interpretation of lysosomal responses, which is useful for environmental scientists.     

A/O膜生物反应器处理高浓度氨氮废水试验研究

对A/O膜生物反应器处理高浓度氨氮废水进行了研究,着重考察硝化液回流比和C/N对系统脱氮效能的影响.研究表明,当硝化液回流比为2、C/N为6时.系统对COD、氨氮、TN的平均去除率分别达96.17%、97.76%、76.29%;A/O膜生物反应器稳定运行期间,氨氮容积负荷去除量与进水氨氮容积负荷呈现良好的线性关系;当A/O膜生物反应器内MLSS稳定在9～13 g/L时,上清液COD较低,膜压差增长缓慢.