活性粉末混凝土的耐酸性

为了考察活性粉末混凝土在严酷环境下的耐酸性能,试验研究了硫酸溶液和醋酸溶液对活性粉末混凝土强度的影响,并比较研究了硫酸溶液对普通水泥基材料和高强水泥基材料的影响。70d浸泡龄期的试验结果表明:在浸泡早期,3种水泥基材料的耐硫酸性能差别不明显,随着暴露时间的延长,活性粉末混凝土比普通水泥基材料和高强水泥基材料呈现出较好的耐硫酸性能;弱离解的醋酸溶液对活性粉末混凝土的侵蚀作用比强离解的硫酸溶液更强。前者与3种水泥基材料的孔隙率、孔隙结构、抗渗性及抗裂性等因素有关,后者则与醋酸溶液的强扩散性有关。     

纳米硫化镉量子点细胞毒性作用机制

为初步探讨硫化镉量子点(CdS QDs)的细胞毒性作用机制,采用MTT毒性实验比较了CdS QDs和常规CdS对仓鼠肺细胞(CHL)的毒性效应以及细胞内外活性氧水平.结果表明,1)在较低暴露浓度(≤20μg·mL-1)时,CdS QDs细胞毒性显著高于常规CdS,而在较高暴露浓度(>20μg·mL-1)时,两者相差不大.2)在较低暴露浓度(≤40μg·mL-1)时,添加N-乙酰半胱氨酸(NAC)可显著降低CdS QDs的细胞毒性,而在较高暴露浓度(>40μg·mL-1)时,添加NAC对CdS QDs的细胞毒性没有明显影响.添加NAC对常规CdS细胞毒性没有显著影响.综合实验结果推测CdS QDs的细胞毒性与暴露剂量有关:在低浓度(<20μg·mL-1)时,主要是活性氧的氧化损伤作用;在中等浓度(20~40μg·mL-1)时,活性氧和Cd2+的释放共同作用;在高浓度(>40μg·mL-1)时,则是Cd2+的释放占主导地位.     

高速铁路声屏障

提出我国高速铁路(铁路客运专线)声屏障主要结构形式和应有的性能。重点分析高速列车气动力的形成、影响因素、计算方法及其对声屏障的作用。提出了高速铁路声屏障的设计要点及其对声屏障的设计建造的建议。     

介质阻挡放电降解苯乙烯的研究

研究了介质阻挡放电(DBD)常压下降解流动态苯乙烯时,不同电压、流速、初始浓度及湿度下苯乙烯的降解情况.结果表明,DBD降解苯乙烯15~20min即可达稳定,产物主要为CO、CO₂和H₂O;电压4800V时有少量带苯环的气态及固态物质产生,且随电压的升高而减少,到7500V时红外光谱已无法检测到;高电压下放电可以取得90%左右的降解率,产生带苯环的气态物质和结焦物质较少.流速在1.5cm/s,浓度为3000mg/m³,相对湿度为20%左右时,降解效果最好.     

介质阻挡放电等离子体直接分解NOx的影响因素

在以 γ- Al₂O₃小球作为填充物的介质阻挡放电条件下 ,研究放电电压 ( 9～ 16k V)、交流电源频率 ( 50～ 1600 Hz)、NO入口浓度 ( 50～1800 ml/m³)、气体空速 (1000～ 6500 h^-1)、反应温度 ( 20～250℃ )、介质小球比表面积及加入 O₂等因素对 NO分解率的影响 .发现提高放电电压、放电频率及介质小球比表面积能显著增加 NO分解率 ,O₂ 的加入对 NO的等离子体分解有强抑制作用 .     

In situ sequential treatment of a mixed contaminant plume

Groundwater plumes often contain a mixture of contaminants that cannot easily be remediated in situ using a single technology. The purpose of this research was to evaluate an in situ treatment sequence for the control of a mixed organic plume (chlorinated ethenes and petroleum hydrocarbons) within a Funnel-and-Gate. A shallow plume located in the unconfined aquifer at Alameda Point, CA, was found to contain up to 218,000 μg/l of cis-1,2 dichloroethene (cDCE), 16,000 μg/l of vinyl chloride (VC) and <1000 μg/l of 1,1 dichloroethene (1,1 DCE), trans-1,2 dichloroethene (trans-1,2 DCE) and trichloroethene (TCE). Total benzene, toluene, ethylbenzene and xylenes (BTEX) concentrations were <10,000 μg/l. Contaminated groundwater was funneled into a gate, 3.0 m wide, 4.5 m long and 6.0 m deep (keyed into the underlying aquitard) where treatment occurred. The initial gate segment consisted of granular iron, for the reductive dechlorination of the higher chlorinated ethenes. The second segment, the biosparge zone, promoted aerobic biodegradation of petroleum hydrocarbons and any remaining lesser-chlorinated compounds, stimulated by dissolved oxygen (DO) and carbon dioxide (CO₂) additions via an in situ sparge system (CO₂ was used to neutralize the high pH produced from reactions in the iron wall). Groundwater was drawn through the gate by pumping two wells located at the sealed, downgradient, end. Over a 4-month period an estimated 1350 g of cDCE flowed into the treatment gate and the iron wall removed 1230 g, or 91% of the mass. The influent mass of VC was 572 g and the iron wall removed 535 g, corresponding to 94% mass removal. The other chlorinated ethenes had significantly lower influent masses (3 to 108 g) and the iron wall removed the majority of the mass resulting in >96% mass removal for any of the compounds. In spite of these high removal percentages, laboratory column tests indicated that at these levels of chlorinated contaminants, surface saturation of the iron grains likely contributed to lower than expected reaction rates. In the biosparge zone, mass removal of cDCE appeared to occur predominantly by biodegradation (65%) with volatilization (35%) being an important secondary process. The dominant removal process for VC was volatilization (70%) although significant biodegradation was also indicated (30%). Laboratory microcosm results confirmed the potential for aerobic biodegradation of cDCE and VC. When average influent field concentrations for cDCE and VC were 220,000 and 46,000 μg/l, respectively, the sequential treatment unit removed 99.6% of the total mass and when the influent concentrations decreased to 26,000 and 19,000 μg/l for cDCE and VC, respectively, >99.9% removal within the treatment gate was attained. BTEX compounds were found to be significantly retarded in the iron treatment zone. Although they did eventually break through the granular iron, and into the gravel transition zone, none of these compounds was detected in the biosparge zone. No noticeable interferences between the anaerobic (reductive) and aerobic parts of the system occurred during testing. The results of this experiment show that in situ treatment sequences are viable, although further work is needed to optimize performance.     

乳化液膜法提取活性艳蓝KN-R工艺研究

利用表面活性剂TH-1、民用煤油、载体N235和内水相NaOH溶液组成的液膜体系,采用正交试验法,对提取活性艳蓝KN-R工艺进行了研究。结果表明:以5%TH-1,5%N235,10%NaOH,油内比Roi为1∶1.5的乳状液膜体系,处理初始浓度为6000mg/L活性艳蓝KN-R废水,在pH值为1,传质温度为25℃,乳水比Rew为1∶5的传质条件下,提取率可达94.8%。     

垃圾污染质在天然黏土屏障中运移情况的调查

通过对杨府山垃圾卫生填埋场的实地调查,重点调查了距垃圾场外边缘以南500m土壤中重金属含量,与国家环保局给出的土壤背景值比较,发现对人类健康有较大影响的Pb,Mn,Cu,Cd的浓度值均大大超过国家规定标准,污染指数分别达到了5.9959,2.0974,4.2021,2.4864,9.2204,其中镉的污染最为严重,并讨论了天然黏土屏障在污染质运移过程中的控制作用,及今后屏障材料的发展方向。该研究结果对该地区进行环境治理的必要性提供了科学依据。     

天然水体腐殖质对双酚A光降解影响的研究

以中压汞灯模拟太阳光光源,研究了双酚A(BPA)在水体腐殖质中的光降解过程,探讨了不同来源的腐殖质、腐殖质浓度、BPA初始浓度、溶解氧等因素对BPA光解速率的影响,实验结果表明,BPA在纯水体系中直接光解很慢,但在腐殖质溶液中光解迅速,符合拟一级动力学反应,改变BPA初始浓度对BPA光解速率的影响不明显,增大溶解氧浓度会抑制BPA光解,通过活性氧分子探针鉴定了腐殖质吸收光辐射产生的羟基与单线态氧,利用GC-MS鉴定了双酚A在Nordic湖富里酸(NOFA)中的光敏化降解产物,推测出BPA敏化降解的可能历程为能量转移导致的直接光解、羟基加成和羟基氧化。     

用水解酸化池-膜生物反应器处理活性艳红X-3B废水

采用水解酸化池-膜生物反应器处理含活性艳红X-3B的模拟废水,研究了水力停留时间（HRT）对水解酸化池废水处理效果的影响,考察了水解酸化池-膜生物反应器对废水的处理效果及膜生物反应器中污泥沉降性能对膜污染的影响。实验结果表明：水解酸化池HRT为16h时,废水的可生化性最好,挥发性脂肪酸质量浓度与COD比值为0．5;HRT为17h时,废水脱色率达69％,而COD的去除率受HRT影响较小;膜生物反应器主要起去除废水中COD的作用;水解酸化池-膜生物反应器处理后废水的脱色率和COD去除率分别为83％和97％;膜生物反应器中活性污泥沉降性能的变化直接影响膜污染的速率。