Field measurements of dissociation of ammonium nitrate at a Beijing site

ＦｉｅｌｄｍｅａｓｕｒｅｍｅｎｔｓｏｆｄｉｓｏｃｉａｔｉｏｎｏｆａｍｍｏｎｉｕｍｎｉｔｒａｔｅａｔａＢｅｉｊｉｎｇｓｉｔｅＳｈｅｎＪｉ，ＺｈａｏＱｉａｎｘｕｅＲｅｓｅａｒｃｈＣｅｎｔｅｒｆｏｒＥｃｏＥｎｖｉｒｏｎｍｅｎｔａｌＳｃｉｅｎｃｅｓ，Ｃ...     

Effects of acid deposition on forests in south China

１ＩｎｔｒｏｄｕｃｔｉｏｎＷｉｔｈｔｈｅｆａｓｔｇｒｏｗｉｎｇｏｆｍｏｄｅｒｎｉｎｄｕｓｔｒｙａｎｄｓｈａｒｐｌｙｉｎｃｒｅａｓｉｎｇｏｆｅｎｅｒｇｙｃｏｎｓｕｍｐｔｉｏｎｐｒｉｍａｒｉｌｙｃｏａｌ，ａｉｒｐｏｌｕｔｉｏｎａｎｄａｃｉｄｄｅｐｏｓｉｔ...     

长江水体氯化过程中强致突变物前驱物的筛选

ＭＸ「３－氯－４－（二氯甲基）－５－羟基－２（５Ｈ）－呋喃酮」是饮用水液氯消毒中产生的一种具有强致突变性的副产物,利用一系列ＸＡＤ吸附树脂和大孔离子交换树脂将长江水中的溶解态有机物分离为溶解态腐殖酸类,憎水弱酸类,憎水碱类,憎水中性物类,亲水酸类,亲水碱类６种组分,分别对不同组分的有机物进行氯化处理,用ＧＣ／ＭＳ选择离子峰面积法测定产物中的ＭＸ。     

某些剧毒有机废料在高温至超临界水中的处理实验

为了探索毒害有机废料的处理条件和反应机制,用二氨基乙二肟,氨基氰和蜜胺作初始试料,在温度１５０－４００℃,压力１００－７００×１０＾５Ｐａ的条件下进行了水热实验研究,部分密胺实验还添加了Ｈ２Ｏ２,实验结构表明,在水热条件下,尤其在超临界水中,二氨基乙二肟和氨基氰既可以通过热解作用而聚合成较高分子量的氮杂环混合物,进而水解转化成ＣＯ２和ＮＨ３,也可以直接发生水解作用,生成ＣＯ２和ＮＨ３,添加氧化剂可     

水解酸化─厌氧─好氧─混凝─吸附工艺处理洁霉素生产丁提高浓度有机废水

采用水解酸化厌氧好氧混凝吸附工艺处理洁霉素生产丁提高浓度有机废水，工程实践表明，ＣＯＤＣｒ和ＢＯＤ５去除率在９９％以上，所排废水各项指标达到国家排放标准。     

粉煤灰吸附去除弱酸性艳蓝印染废水

利用粉煤灰对弱酸性艳蓝印染废水进行了处理。研究表明：粉煤灰的粒径、灰水比、废水pH值以及振荡吸附时间对粉煤灰的吸附能力均有较大影响。在以下工艺条件下：20℃,粉煤灰的粒径200目,灰水比为1：30,pH为2．0,振荡吸附2．5h,弱酸性艳蓝印染废水经粉煤灰处理后,COD值由576mg／L降至71mg／L,COD去除率可达87．7％：废水色度可从10000倍降为50倍,色度的去除率达99．5％,出水pH为6．5。出水水质达到了国家印染废水一级排放标准(GB4287—92)。     

土柱淋洗法修复铬污染土壤的水力梯度优化试验

针对重金属污染土壤的修复,淋洗法是一种比较成熟的方式,但目前研究主要聚焦于淋洗剂的选择,而关于水力停留时间对淋洗效果影响的研究相对较少.水力梯度是影响水力停留时间的重要因素,优化水力梯度能够缩短修复周期,降低淋洗成本,有效提高淋洗效率,为现场淋洗修复工程应用提供参考.本文针对人工制备的不同质地的铬污染土壤进行了土柱淋洗...     

腐殖酸与钙离子共存下ZVI界面沉积过程

为精准分析环境介质在零价铁（ZVI）界面沉积过程和沉积层特性,采用喷涂方法制备ZVI负载芯片,应用耗散式石英晶体微天平（QCMD）研究了腐殖酸（HA）与钙离子（Ca（Ⅱ））在ZVI界面沉积吸附过程的差异,并探讨了Ca（Ⅱ）浓度与HA/Ca（Ⅱ）投加顺序对沉积过程的影响机理.结果表明,在反应体系中先通入HA相较先通入Ca（Ⅱ）,ZVI表面形成的沉积层质量更高、沉积层结构更稳定;HA沉积后可促进Ca（Ⅱ）沉积,然而Ca（Ⅱ）先沉积后HA沉积量较少,很大程度上与吸附层外层结构组成差异相关.此外,发现随着Ca（Ⅱ）浓度从10mg/L升高至200mg/L,Ca（Ⅱ）沉积速率加快,界面沉积量增多.QCMD耗散变化研究发现,当Ca（Ⅱ）浓度从10mg/L提高至100mg/L,沉积层耗散变化值（ΔD）逐渐下降,沉积层转变为刚性结构;Ca（Ⅱ）浓度继续加大到200mg/L,ΔD升高趋势,沉积层构象呈现疏松态.应用QCMD可实时监测ZVI钝化层形成的动态变化过程,提供了ZVI界面吸附层变化特征等关键信息.     

紫外催化过硫酸盐深度处理垃圾焚烧厂渗滤液

为研究垃圾焚烧厂渗滤液生化出水的处理特性,对比了单独紫外(UV)体系、单独过硫酸盐(PS)体系以及紫外/过硫酸盐(UV/PS)体系深度处理垃圾渗滤液效果,发现UV/PS体系对渗滤液中有机污染物的去除效果较另外两体系的效果优异,因此采用UV/PS体系处理典型难降解有机物腐殖酸并考察体系的处理效能.在初始腐殖酸浓度为200...     

Regeneration of commercial selective catalyst reduction catalysts deactivated by Pb and other inorganic elements

The regeneration of commercial SCR(Selective Catalyst Reduction) catalysts deactivated by Pb and other elements was studied.The deactivated catalyst samples were prepared by chemical impregnation with mixed solution containing K_2SO_4,Na_2SO_4,CaSO_4,Pb(NO_3)_2and NH_4H_2PO_4.A novel method combining Ethylenediaminetetraacetic acid disodium salt(EDTA-2Na) and H_2SO_4solution(viz.catalysts treated by dilute EDTA-2Na and H_2SO_4 solution in sequence) was used to recover the activity of deactivated samples,and the effect was compared with single H_2SO_4,oxalic acid,acetic acid,EDTA or HNO_3 solutions.The surface structure,acidity and reducibility of samples were characterized by N_2adsorption–desorption,inductively coupled plasma optical emission spectrometer(ICP-OES),scanning electron microscopy(SEM),X-ray diffraction(XRD),X-ray fluorescence(XRF),H-2-temperature programmed section(H_2-TPR),NH3-temperature programmed desorption(NH3-TPD) and in situ DRIFTS.Impurities caused a decrease of specific surface area and surface reducibility,as well as Br?nsted acid sites,and therefore led to severe deactivation of the SCR catalyst.The use of an acid solution alone possibly eliminated the impurities on the deactivated catalyst to some extent,and also increased the specific surface area and Br?nsted acid sites and promoted the surface reducibility,thus recovered the activity partially.The combination of EDTA-2Na and H_2SO_4 could remove most of the impurities and improve the activity significantly.The removal of Pb should be an important factor for regeneration.Due to a high removal rate for Pb and other impurities,the combination of EDTA-2Na and H_2SO_4 solutions provided the best efficiency.