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％.     

浙江省污水污泥处理处置状况的调查

通过对丽水、宁波、衢州、诸暨等浙江省境内十几个地区的污水处理厂的调查发现:目前浙江省内的污水处理工艺中,A2/O、A/O、氧化沟三种工艺占了近50%的份额。而SBR因其方法特点正在受到越来越多的重视。在污泥处理工艺中,填埋占了最大的一部分,有近70%的污水处理厂将产生的污泥进行填埋处理。目前,污泥处理技术单一,需要继续探寻污泥的减量和资源化技术,为日益增多的污泥探寻出路。     

UASB+接触氧化法处理CMC废水

CMC废水属于高盐分高有机物废水,废水COD为50 000~80 000 mg/L,含盐量为13%左右,不适合直接生化处理。本文采用CMC废水和循环冷却水按一定比例混合后一起处理,混合后的废水采用UASB+接触氧化法的处理工艺处理。工程运行表明:稀释后的CMC废水中的盐分稳定在1.4%以内,该处理工艺能够确保出水达到《污水综合排放标准》(GB8978-1996)中三级排放标准。     

SBR法处理低C/N污水的工程应用——以某基地污水处理站改造工程为例

低C/N污水的生化处理过程中,由于碳源不足,不能满足硝化和反硝化的要求,造成出水NH3-N超标。采用SBR工艺对某基地污水处理站厌氧处理后的低C/N污水进行改造,处理后出水COD去除率达到97%以上,NH3-N去除率达到93%以上。     

抽水蓄能电站工程建设中生态环境监理工作实践探讨

水利水电工程建设是促进国家经济发展的重要建设项目之一,抽水蓄能电站工程建设的重要性正在不断凸显。抽水蓄能电站工程的建设与生态环境有着密切的关系,由于抽水蓄能电站工程长期大规模的开发利用破坏了周边生态环境的稳定,加强工程建设中的环境监理工作是将生态破坏程度降到最低的必然要求。以抽水蓄能电站为实例,通过制定科学合理的环境监理方案,将生态环境监理要点落实到施工建设当中,以期最大限度地减少对生态环境的破坏。     

氟化铵制备氟化钙最优条件研究

试验采用氟化铵与石灰石粉、石灰乳反应制取氟化钙,研究了反应温度、物料浓度、物料过量系数等各主要参数变化对氟化钙结晶、过滤速度、氟收率及其含量的影响,摸索出最优反应条件。     

扬州市区水环境质量现状及防治对策

通过对扬州市区境内河流和地下水的环境质量进行调查分析,结果表明：河流水质较好,城区污水都排入污水处理厂且处理厂正常运行,水质达标排放,主要的污染物是有机污染物;地下水达到水质标准,由于地质原因,主要污染指标为总硬度和总矿化度。但仍应加大污染防治力度,针对水环境现状和问题,采取有效措施,坚持深入开展环境宣传教育,依靠科技进步,科学防治环境污染,控制污染源,实行达标制度,提高人们自身环保意识,促进水资源的可持续利用。     

电化学氧化PFOA阳极材料筛选及其机制研究

全氟辛酸(PFOA)具有环境持久性及内分泌干扰性,传统的生物降解及高级氧化法对PFOA的去除效果微弱.本研究采用电化学氧化法降解PFOA,选取BDD(掺硼金刚石电极)、Pt、Ti、Ti/RuO2、Ti/RuO2-IrO2、Ti/In2O3、Ti/SnO2-Sb2O5-IrO2、Ti/SnO2-Sb2O5-RhO2、Ti/SnO2-Sb2O5、Ti/SnO2-Sb2O5-CeO2和Ti/SnO2-Sb2O5-Bi2O3这11种阳极材料为备选电极.采用线性扫描伏安法测试析氧电位(OEP),评价11种电极对PFOA的降解效果和脱氟效果,并采用超声-电化学协同方法间接证明PFOA分子在电极表面的直接电子转移是降解反应的第一步.Ti/SnO2-Sb2O5-Bi2O3、Ti/SnO2-Sb2O5-CeO2、Ti/SnO2-Sb2O5和BDD对PFOA有较好的电氧化效果,降解率分别是89.8%、89.8%、93.3%和98.0%.Pt、Ti/SnO2-Sb2O5-RhO2、Ti/SnO2-Sb2O5-IrO2和Ti/In2O3对PFOA的电氧化效果微弱,降解率分别是2.1%、2.3%、12.5%和3.1%.而Ti、Ti/RuO2和Ti/RuO2-IrO2对PFOA没有电氧化能力.PFOA分子经过电极表面的直接电化学氧化发生脱羧反应,后经过逐步脱掉CF2单元的循环生成短链的全氟羧酸类化合物C6F13COO-、C5F11COO-、C4F9COO-和C3F7COO-.