表面活性剂及其组合洗脱污染土壤中的硫丹

采用序批实验和并行解吸法,研究了添加和不添加Na2SiO3两种情况下,非离子表面活性剂和阴/非离子混合表面活性剂对污染老化土壤中α-、β-硫丹的洗脱效果与动力学特征.结果表明,不添加Na2SiO3时,α-、β-硫丹的洗脱率顺序为Tween80/SDS>Tween 80>Triton X-100.Triton X-100/SDS在100～500 mg·L-1和800～1 000 mg·L-1时的洗脱率分别低于和高于相应浓度的Triton X-100;添加Na2SiO3后,硫丹的洗脱率顺序为Tween 80/SDS>Tween 80>Triton X-100/SDS>Triton X-100,4种洗脱模式对硫丹的洗脱能力均显著提高,其中α-硫丹的洗脱率分别是不加Na2SiO3的1.17～2.73、1.87～4.02、1.85～6.56和1.87～2.85倍.硫丹的洗脱过程可用4参数2室一级动力学模型描述,存在明显的快速洗脱和慢速洗脱阶段;β-硫丹的洗脱速率和洗脱率均低于相应处理的α-硫丹,表明β-硫丹较难从土壤中洗脱;添加Na2SiO3可增大硫丹的快速和慢速洗脱速率常数,减少慢速洗脱的百分率.与其它洗脱模式比较,添加Na2SiO3的Tween 80/SDS能够高效、快速洗脱污染土壤中的硫丹,是一种优良的混合洗脱剂.     

Effect of transition metal doping under reducing calcination atmosphere on photocatalytic property of TiO2 immobilized on SiO2 beads

TiO₂ immobilized on SiO₂ (TiO₂/SiO₂) have been prepared by sol-gel method and various ions of transition metals (Cr³⁺, Co²⁺, Ni²⁺, Cu²⁺, and Zn²⁺) were doped on the photocatalyst using wet impregnation method under reducing calcination atmosphere. The photocatalytic activity of metal doped TiO₂/SiO₂ towards phenol degradation under black light irradiation were investigated and compared with undoped TiO₂/SiO₂. The results showed that the photoresponse of Cu²⁺ and Zn²⁺ doped TiO₂/SiO₂ were larger than undoped TiO₂/SiO₂, indicating that the photogenerated carriers were separated more efficiently in Cu²⁺ and Zn²⁺ doped TiO₂/SiO₂. The reactivity was in the order of Cu²⁺ > Zn²⁺ > Ni²⁺ > Cr³⁺ > Co²⁺. The different photoreactivity was ascribed to combine effect of the different ionic radii and photocorrison tendency of the dopants. The sample was also characterized by surface analytical methods such as X-ray diffraction, scanning electron micrograph/electron dispersive X-ray analyzer and UV-Vis absorption spectrum.     

Fe2O3 particles as superior catalysts for low temperature selective catalytic reduction of NO with NH3

Fe203 particle catalysts were experimentally studied in the low temperature selective catalytic reduction （SCR） of NO with NH3. The effects of reaction temperature, oxygen concentration, [NH3]/[NO] molar ratio and residence time on SCR activity were studied. It was found that Fe203 catalysts had high activity for the SCR of NO with NH3 in a broad temperature range of 150-270℃, and more than 95% NO conversion was obtained at 180℃ when the molar ratio [NH3]/[NO] = 1, the residence time was 0.48 seconds and 02 volume fraction was 3%. In addition, the effect of SO2 on SCR catalytic activity was also investigated at the temperature of 180℃. The results showed that deactivation of the Fe2O3 particles occurred due to the presence of SO2 and the NO conversion decreased from 99.2% to 58% in 240 min, since SO2 gradually decreased the catalytic activity of the catalysts. In addition, X-ray diffraction, Thermogravimetric analysis and Fourier transform infrared spectroscopy were used to characterize the fresh and deactivated Fe2O3 catalysts. The results showed that the deactivation caused by SO2 was due to the formation of metal sulfates and ammonium sulfates on the catalyst surface during the de-NO reaction, which could cause pore plugging and result in suppression of the catalytic activity.     

Adsorption of Cr(Ⅲ) from acidic solutions by crop straw derived biochars

Cr（Ⅲ） adsorption by biochars generated from peanut, soybean, canola and rice straws is investigated with batch methods. Adsorption of Cr（Ⅲ） increased as pH rose from 2.5 to 5.0. Adsorption of Cr（Ⅲ） led to peak position shifts in the FFIR-PAS spectra of the biochars and made zeta potential values less negative, suggesting the formation of surface complexes between Cr^3＋ and functional groups on the biochars. The adsorption capacity of Cr（Ⅲ） followed the order： peanut straw char 〉 soybean straw char 〉 canola straw char 〉 rice straw char, which was consistent with the content of acidic functional groups on the biochars. The increase in Cr^3＋ hydrolysis as the pH rose was one of the main reasons for the increased adsorption of Cr（Ⅲ） by the biochars at higher pH values. Cr（llI） can be adsorbed by the biochars through electrostatic attraction between negative surfaces and Cr^3＋, but the relative contribution of electrostatic adsorption was less than 5%. Therefore, Cr（Ⅲ） was mainly adsorbed by the biochars through specific adsorption. The Langumir and Freundlich equations fitted the adsorption isotherms well and can therefore be used to describe the adsorption behavior of Cr（Ⅲ） by the crop straw biochars. The crop straw biochars have great adsorption capacities for Cr（Ⅲ） under acidic conditions and can be used as adsorbents to remove Cr（Ⅲ） from acidic wastewaters.     

不同裂解条件对生物炭稳定性的影响

在300⁵00℃温度下热裂解水稻秸秆、玉米秸秆制备生物炭,并采用红外光谱(FTIR)和元素分析的方法,以生物炭表面官能团和元素组成为主要考察指标,研究了不同裂解温度、不同保留时间对生物炭稳定性的影响。生物炭红外光谱图结果显示,生物质原材料经过裂解炭化过程,原材料分子结构中所含醚键(C-O-C)、羰基(C=O)等基团消失。随着裂解温度升高,生物炭中甲基(-CH3)和亚甲基(-CH2)也逐渐消失,而芳环结构增加,生物炭芳香化程度增强。延长生物炭制备过程中的保留时间亦有相同结果。生物炭元素组成的结果显示,裂解温度升高及保留时间延长均能使生物炭的H/C比下降,同时裂解温度对生物炭H/C的影响更加显著。相比水稻秸秆生物炭,玉米秸秆生物炭的芳环骨架更加明显,芳香化程度更高。     

基于ImageJ评价泥炭岩心存储对色相与彩度的影响

利用ImageJ软件对2008年在红原泥炭地开展钻探时的泥炭岩心照片和2009年分样时的岩心照片进行表面色彩分析.对比分析发现,存储以前和存储以后泥炭岩心的表面色彩发生改变,表现在样品存储后基于RGB色彩体系的三元色值和灰度值均有降低(变暗),且各色值变化幅度降低.就各色值在剖面上的变化特征而言,样品存储前和存储后的变...     

非离子表面活性剂对污泥调理脱水效果的影响

现有污泥脱水技术仅使污泥含水率降到80%左右,难以满足日益严格的污泥处置要求.以污泥比阻（SRF）、脱水率为考察指标,比较了两大类非离子型表面活性剂（辛基酚聚氧乙烯醚OPEO型和烷基糖苷APG）对剩余污泥的脱水效果,并对原泥及调理后污泥进行了显微观察.结果表明,非离子表面活性剂可使污泥絮体粒径变小,不规则程度降低,改善了污泥的脱水性能,而且烷基糖苷APG脱水效果优于OPEO型.APG投加量为0.05%干固体时,污泥比阻即可降低到原泥的42%,脱水率可达到93%.以烷基糖苷APG为调理剂进行板框脱水实验,结果表明,当APG投加量为0.05%干固体时,脱水泥饼含水率比原泥脱水泥饼含水率低约10%,脱水率可达到97%.本研究为APG应用于污泥脱水,改善污泥脱水性能提供一些参考.     

酿酒酵母吸附Pb(Ⅱ)的表面特性研究

为深入探讨酿酒酵母吸附Pb（Ⅱ）的微观作用机制,本文利用表面显微分析技术（SEM-EDS、TEM-EDS、AFM）研究了酿酒酵母细胞吸附重金属离子Pb（Ⅱ）前后的细胞表面变化.研究结果表明,酿酒酵母细胞与Pb（Ⅱ）作用后,细胞表面除吸附Pb（Ⅱ）外,同时产生大量更高浓度的含Pb（Ⅱ）沉淀,导致Pb（Ⅱ）从溶液中被去除.酵母与Pb（Ⅱ）反应前,酵母细胞表面可检测到的主要元素包括C、O、N、P、S、K、Mg;酵母与Pb（Ⅱ）作用后,细胞表面始终保持C、O、P吸收峰,而N、K、Mg、S吸收峰随反应条件不同而减弱、消失或增强.P作为细胞表面组分可能与Pb（Ⅱ）结合.酵母与Pb（Ⅱ）作用过程中,重金属离子促进酵母细胞释放细胞内含物.原子力显微镜（AFM）证实,云母片表面对酵母吸附Pb（Ⅱ）后细胞的铺展变形作用明显增大.     

电袋复合除尘技术在燃煤电厂中的应用

电袋复合式除尘技术综合了电除尘和布袋除尘的收尘优点,通过除尘负荷的合理分配,实现了电除尘和布袋除尘的有机结合;采用基于表面过滤原理的新型滤料,可克服常规滤料清灰后除尘效率降低及滤袋易破损等缺点。电袋复合式除尘器在徐州坝山环保热电有限公司的应用实践表明,电袋复合式除尘器可保持高效稳定除尘同时节能,粉尘排放浓度达到了30 ...     

Evaluation of reusing alum sludge for the coagulation of industrial wastewater containing mixed anionic surfactants

A coagulation-flocculation process is typically employed to treat the industrial wastewater generated by the consumer products industry manufacturing detergents, soaps, and others. The expenditure of chemicals including coagulants and chemicals for pH adjustment is costly for treating this wastewater. The objective of this study was to evaluate the feasibility of reusing the aluminum sulfate (alum) sludge as a coagulant or as a coagulation aid so that the fresh alum dosage can be minimized or the removal e ciency can be enhanced. The experiments were conducted in a jar-test apparatus simulating the coagulation-flocculation process for simultaneous removals of organic matters, anionic surfactants, suspended solids, and turbidity. At the optimum initial pH value of 10 and the fresh alum concentration of 400 mg/L, the total suspended solids (TSS), total chemical oxygen demand (TCOD), total anionic surfactants, and turbidity removal e ciencies were 71.5%, 76.4%, 95.4%, and 98.2%, respectively. The addition of alum sludge as a coagulant alone without any fresh alum addition could significantly remove the turbidity, TCOD, and anionic surfactants. The TSS was left in the supernatants after the settling period, but would subsequently be removed by adding the fresh alum. The TSS, TCOD, and turbidity removal e ciencies were also enhanced when both the alum sludge and the fresh alum were employed. The TCOD removal e ciency over 80% has been accomplished, which has never fulfilled by using the fresh alum alone. It is concluded that the alum sludge could be reused for the treatment of industrial wastewater generated by the consumer products industry.