STAC有机膨润土的表征及其处理垃圾渗滤液的研究

文章以钙基蒙脱石为原料,经钠化后与十八烷基三甲基氯化铵(又称1831,简称STAC)进行离子交换反应,合成有机膨润土,通过XRD、IR 、SEM等测试仪,对有机膨润土的结构进行了分析,同时利用改性后的STAC有机膨润土对某垃圾填埋场中的渗滤液进行处理,用GC/MS对处理前后垃圾渗滤液中主要有机组分进行了分析,结果表明,...     

不同进水条件对SBR工艺脱氮除磷效能的影响

采用人工配水,研究进水在不同pH值,碳源类型,碳氮比条件下,厌氧/好氧/缺氧(A/O/A)sBR工艺对生物法脱氮除磷效能的影响.结果表明:不同的进水条件对反应器的影响较大,当pH值为7.5,乙酸钠为碳源,碳氮比为1.4时,反应器运行效果最佳,系统对PO43--P,NH4+-N的去除率分别达到97.28%,99.5%.N...     

垃圾焚烧飞灰中二噁英削减技术研究

二噁英(PCDD/Fs)是多氯代二苯并二噁英和多氯代二苯并呋喃的总称,因具有生物蓄积性、高毒性、难降解等特点而备受关注。垃圾焚烧是二噁英的重要来源,而其中超过50%的二噁英以飞灰形式排出。文章综述了热分解法、光降解法、机械化学法、生物降解法等飞灰二噁英毒性削减技术的国内外研究进展,并在此基础上对飞灰二噁英削减技术研究和管理提出了建议。     

供碳源载体及其在低碳氮比污水处理中的应用研究

为解决低C/N污水的脱氮问题,本实验自行研制开发了一种新型碳聚合物载体.对该载体进行低C/N污水的生物膜脱氮研究,考察了HRT、pH、DO、温度等因素对系统同步硝化反硝化脱氮效果的影响.结果表明:在C/N比为4、pH=8、DO=1 mg/L、HRT=6 h,T=24℃的条件下,氨氮及总氮的去除率分别可以达到90%和70...     

用GC/MS分析火灾后苯板产生固体废物中的有机物

采用GC/MS方法对某苯板厂火灾后产生的固体废弃物进行检测分析.结果表明,在苯板火灾后产生的固体废弃物中检测出61种化合物,其中被美国EPA列入优先污染物的苯系物、萘和蒽等占总有机物12.2％.     

聚硅酸对不同形态铝沉积行为的影响

针对给水管网中残余铝沉积和再溶解现象可能引起的水质问题,研究了聚硅酸对不同水解聚合形态铝沉积、再溶解的影响,并以石英微晶天平为表征手段,初步探讨了聚硅酸对不同形态铝沉积、再溶解过程影响的机理.结果表明,聚硅酸能显著改变不同水解聚合形态铝的沉积、再溶解行为.聚硅酸可与3种水解聚合形态的铝迅速结合而生成可沉积产物,但产物性质不同.以单体形态为主的Al_0与聚硅酸的反应产物性质较稳定,部分以溶解态存在,部分以非溶解态(可沉积态)存在;尽管铝的两种聚合形态Al_(13)和Al_(30)与聚硅酸反应也生成了部分可沉积产物,但随着时间的推移,这些产物又逐渐向溶解态转化.铝硅比对Al_0体系中铝的沉积溶解行为影响较小,而对Al_(13)和Al_(30)影响较大,且在0.2∶20(以Al和SiO_2计的质量比)时,沉积态铝的溶解速率最快.     

模拟水体硝态氮对黄菖蒲生长及其氮吸收的影响

为了对挺水植物在水环境与水生态修复中的应用提供参考依据,选取黄菖蒲(Iris pseudacorus L.)为对象,通过模拟水培实验,对比研究了6种水体硝态氮质量浓度(10.68、23.88、42.22、63.33、82.92、97.13 mg·L~(-1))下,黄菖蒲地上和地下生物量、根冠比、叶绿素含量、氮累计吸收量以及对硝态氮去除效果的差异,以期明确模拟水体硝态氮质量浓度对黄菖蒲生长及其氮吸收能力的影响.结果显示,首先,不同硝态氮质量浓度对黄菖蒲地上部分(茎叶)生长的影响大于地下部分(根);当硝态氮质量浓度为10.68 mg·L~(-1)时,黄菖蒲的根冠比增加;当硝态氮质量浓度为42.22~97.13 mg·L~(-1)时,黄菖蒲的根冠比减少.其次,黄菖蒲适宜生长的硝态氮质量浓度为23.88~63.33 mg·L~(-1);硝态氮质量浓度低于10.68 mg·L-1或高于82.92mg·L-1时,均会对黄菖蒲的叶绿素合成产生抑制作用.再次,黄菖蒲对氮的累积量随硝态氮质量浓度增加而增加,且地下部分对氮的累积能力优于地上部分;6种浓度下,单株黄菖蒲的氮累计吸收量为10.56~75.43 mg,其地下部分依次为地上部分的7.2、2.3、2.5、2.1、1.6以及1.5倍.此外,黄菖蒲对氮的利用效率与硝态氮质量浓度之间成显著的幂函数关系,且地上部分的氮利用效率高于地下部分.最后,黄菖蒲对硝态氮的去除率随硝态氮质量浓度增加而增加,6种浓度下黄菖蒲对硝态氮的去除率介于94.9%和99.3%之间,且水体中硝态氮质量浓度随时间延续呈指数函数降低.结果表明,黄菖蒲对硝态氮有很好的去除效果,但黄菖蒲的生长及其对氮的吸收与去除效率受水体硝态氮质量浓度影响显著,且地上部分较地下部分更为敏感.     

Effects of metal and acidic sites on the reaction by-products of butyl acetate oxidation over palladium-based catalysts

Catalytic oxidation is widely used in pollution control technology to remove volatile organic compounds. In this study, Pd/ZSM-5 catalysts with different Pd contents and acidic sites were prepared via the impregnation method. All the catalysts were characterized by means of N2 adsorption- desorption, X-ray fluorescence （XRF）, HE temperature programmed reduction （H2-TPR）, and NH3 temperature programmed desorption （NH3-TPD）. Their catalytic performance was investigated in the oxidation of butyl acetate experiments. The by-products of the reaction were collected in thermal desorption tubes and identified by gas chromatography/mass spectrometry. It was found that the increase of Pd content slightly changed the catalytic activity of butyl acetate oxidation according to the yield of CO2 achieved at 90%, but decreased the cracking by-products, whereas the enhancement of strong acidity over Pd-based catalysts enriched the by-product species. The butyl acetate oxidation process involves a series of reaction steps including protolysis, dehydrogenation, dehydration, cracking, and isomerization. Generally, butyl acetate was cracked to acetic acid and 2- methylpropene and the latter was an intermediate of the other by-products, and the oxidation routes of typical by-products were proposed. Trace amounts of 3-methylpentane, hexane, 2-methylpentane, pentane, and 2-methylbutane originated from iso4merization and protolysis reactions.     

Pd/activated carbon sorbents for mid-temperature capture of mercury from coal-derived fuel gas

Higher concentrations of Hg can be emitted from coal pyrolysis or gasification than from coal combustion, especially elemental Hg. Highly efficient Hg removal technology from coal-derived fuel gas is thus of great importance. Based on the very excellent Hg removal ability of Pd and the high adsorption abilities of activated carbon（AC） for H2 S and Hg, a series of Pd/AC sorbents was prepared by using pore volume impregnation, and their performance in capturing Hg and H2 S from coal-derived fuel gas was investigated using a laboratory-scale fixed-bed reactor. The effects of loading amount, reaction temperature and reaction atmosphere on Hg removal from coal-derived fuel gas were studied. The sorbents were characterized by N2 adsorption, X-ray diffraction（XRD） and X-ray photoelectron spectroscopy（XPS）. The results indicated that the efficiency of Hg removal increased with the increasing of Pd loading amount, but the effective utilization rate of the active component Pd decreased significantly at the same time. High temperature had a negative influence on the Hg removal. The efficiency of Hg removal in the N2-H2S-H2-CO-Hg atmosphere（simulated coal gas） was higher than that in N2-H2S-Hg and N2-Hg atmospheres, which showed that H2 and CO, with their reducing capacity, could benefit promote the removal of Hg. The XPS results suggested that there were two different ways of capturing Hg over sorbents in N2-H2S-Hg and N2-Hg atmospheres.     

V2O5/TiO2催化剂脱除NO的研究

采用了等体积浸渍法制备二氧化钛负载钒氧化物催化剂（V2O5/TiO2）,研究了V2O5负载量、反应温度、烟气流量、氨氮比以及运行时间各因素对NH3选择性催化还原NO反应（SCR）效率的影响.研究结果表明：经过500℃温度下煅烧,烟气流量为200ml/min,负载量为7wt％的V2O5/TiO2催化剂,在400℃温度下反应,NO脱除率可达70.5％.