我国钛白粉工业发展现状与环境政策研究

针对我国钛白粉工业发展的现状与存在的问题,深入分析造成钛白粉上业现状的原因,并从环保角度提出对策与建议.     

非常规多水源双膜工艺处理后浓缩水的水质特性

利用常规和非常规多水源经RO处理后作为新水源,与非常规单一城市污水厂水源比较,多水源双膜处理工艺产生的浓水水质有所不同。浓水水质检测主要指标包括无机盐(Cl-、SO42-、TDS、全盐量)、有机物(BOD、COD)、氮营养物(NH4+-N、TN)、碱度、硬度等。通过实际工程运行水质动态监测,初步探讨了RO浓水的水质规律及其影响因素,为RO浓水处理处置技术深入研究奠定了基础。     

浸提分离法提取皂素清洁工艺研究

提出一种通过溶剂提取将游离皂苷与淀粉、纤维等成分分离，从源头上减少用水量、耗酸量和污染物排放量的皂素清洁生产工艺。首先对溶剂提取条件进行优化，得出最佳工艺条件为：90%（体积比）乙醇溶液，料液比1∶7，沸腾回流提取3 h，重复提取3次。然后通过气质联用（GC/MS）分析了皂素废水的有机物组成。研究结果表明，清洁工艺皂素产率为1.51%（降低3.82%），用酸量比传统工艺减少了71%，头道液COD浓度降低了46%，每100 g原料排放的COD总量下降了84%；皂素废水的有机物污染物主要为糠醛及其衍生物，清洁工艺废水的有机物含量更低，更易降解。     

废水中环氧丙烷降解菌株的培育及降解效果研究

本文通过对污泥的驯化筛选得到4株降解环氧丙烷废水的优势茵A、B、C、D，并对降解效果最好的一个菌株A进行研究，得到其最佳降解条件是温度为30℃、pH为5、废水浓度为20％、反应时间为9h，其COD去除率可达到63．24％左右。     

4A沸石去除水中Pb2＋的研究

在静态条件下，研究了4A沸石对废水中Pb2＋的吸附性能，并探讨了影响吸附的因素。实验表明：当温度为30℃，废水pH为5～6，0．01g4A沸石对100mg／LPb2＋溶液10mL吸附20min，Pb2＋的去除率可达到99％以上。在实验研究条件下，4A沸石对Pb2＋的吸附符合Langmuir和Freundlich等温吸附方程，相关系数为0．9819和0．9998。经计算，4A沸石对Pb2＋的饱和吸附量为125mg／g。4A沸石吸附水中Pb2＋达到吸附平衡的时间较短；溶液pH值的变化对吸附效果影响不显著；温度从室温略微升高，Pb2＋的去除率略有增大。吸附在4A沸石上的Pb“可回收利用，处理后的4A沸石可以再生，且重复使用性能较好。     

UASB+A/O工艺处理大豆蛋白生产废水

介绍了采用UASB+ A/O工艺处理大豆蛋白生产废水的工程,包括大豆蛋白生产废水的特点、废水处理的工艺流程、主要构筑物以及工艺运行的控制事项、处理效果和效益分析.工程实践表明,采用UASB+ A/O工艺处理大豆蛋白生产废水效果良好,运行稳定,出水能够达到《污水综合排放标准》(GB 8978-1996)三级标准,并且工艺过程能够产生经济效益,减少了系统的运行费用,达到了资源化的目的.     

大蒜加工废水的活性污泥培养驯化研究

试验选用生活污水处理厂、化肥厂、友谊河的活性污泥作为菌种进行培养实验,培养过程中,考查温度、营养物质的添加等因素对污泥培养的影响,结果证明,大蒜废水本身有机物和其他无机物之间的比例还是比较协调的,营养物质米泔水的添加对大蒜加工废水COD的降解帮助不大.然而,温度对大蒜加工废水活性污泥的培育影响显著,从整体上看,随着温度的升高,COD去除率也增加.实验还显示经过培养,当水温为15℃时,系统的沉降性能变差,出水未沉降絮体增多,并出现污泥膨胀现象,综合考虑,确定25℃为最佳培养温度.     

亚甲基蓝分光光度法测定废水硫化物的不确定度评定研究

分析了应用亚甲基蓝分光光度(GB/T16489-1996)测定废水硫化物测试过程中不确定度影响因素,主要来源为硫化物标准溶液、标准曲线拟合、随机效应、分光光度计和取样体积这五部分。本测量合成相对标准不确定度0.025 9;其中由测定样品质量引入的不确定度为0.024 7;由样品体积引入的不确定度为0.007 7。本次废水中硫化物测量结果为:0.110±0.006 mg/L,k=2(包含概率约为95%)。     

N2O emission from a sequencing batch reactor for biological N and P removal from wastewater

Nitrous oxide （N2O） is a greenhouse gas that can be released during biological nitrogen removal from wastewater. N2O emission from a sequencing batch reactor （SBR） for biological nitrogen and phosphorus removal from wastewater was investigated, and the aims were to examine which process, nitrification or denitrification, would contribute more to N2Oemission and to study the effects of heterotrophic activities on N2O emission during nitrification. The results showed that N2O emission was mainly attributed to nitrification rather than to denitrification. N2O emission during denitrification mainly occurred with stored organic carbon as the electron donor. During nitrification, NaO emission was increased with increasing initial ammonium or nitrite concentrations. The ratio of N2O emission to the removed ammonium nitrogen （N2O- N/NH4-N） was 2.5% in the SBR system with high heterotrophic activities, while this ratio was in the range from 0.14% to 1.06% in batch nitrification experiments with limited heterotrophic activities.     

Reuse of heavy metal-accumulating Cynondon dactylon in remediation of water contaminated by heavy metals

Phytoremediation technology is regarded as a simple and efficient way to remove heavy metals from contaminated soil. A reasonable disposal of metal hyperaccumulators is always and resource-saving. The a major issue in waste reuse heavy metal-accumulating Cynondon dactylon （L.） was investigated where heavy metals were desorbed by a facile acid-treatment. The result indicated that more than 90% of heavy metals （Zn, Pb and Cu） was extracted from Cynondon daetylon with 0.2 mmol· L^-1 HCl. The plant residue was used to adsorb heavy metals ions. The adsorption fitted the Langmuir isotherm model with the saturation adsorption capacity of 9.5 mg·g^-1 Zn^2＋, 36.2 mg·g^-1 Pb2＋ and 12.9 mg·g^-1 Cu^2＋, and the surface eomplexation and the backfilling of heavy metal imprinting cavities existed simultaneously during the adsorption. The treatment of wastewaters indicated that the plant residue exhibited a high removal rate of 97% for Cu. Also, the material could be recycled. The method offers a new disposal approach for heavy metal hyperaccumulator.