Removal of elemental mercury with Mn/Mo/Ru/Al2O3 membrane catalytic system

In this work, a catalytic membrane using Mn/Mo/Ru/Al₂O₃ as the catalyst was employed to remove elemental mercury (Hg⁰) from flue gas at low temperature. Compared with traditional catalytic oxidation (TCO) mode, Mn/Al₂O₃ membrane catalytic system had much higher removal efficiency of Hg⁰. After the incorporation of Mo and Ru, the production of Cl₂ from the Deacon reaction and the retainability for oxidants over Mn/Al₂O₃ membrane were greatly enhanced. As a result, the oxidization of Hg⁰ over Mn/Al₂O₃ membrane was obviously promoted due to incorporation of Mo and Ru. In the presence of 8 ppmv HCl, the removal efficiency of Hg⁰ by Mn/Mo/Ru/Al₂O₃ membrane reached 95% at 423 K. The influence of NO and SO₂ on Hg⁰ removal were insignificant even if 200 ppmv NO and 1000 ppmv SO₂ were used. Moreover, compared with the TCO mode, the Mn/Mo/Ru/Al₂O₃ membrane catalytic system could remarkably reduce the demanded amount of oxidants for Hg⁰ removal. Therefore, the Mn/Mo/Ru/Al₂O₃ membrane catalytic system may be a promising technology for the control of Hg⁰ emission.     

Catalytic activity of cerium-doped Ru/Al2O3 during ozonation of dimethyl phthalate

In this paper, factors influencing the mineralization of dimethyl phthalate (DMP) during catalytic ozonation with a cerium-doped Ru/Al₂O₃ catalyst were studied. The catalytic contribution was calculated through the results of a comparison experiment. It showed that doping cerium significantly enhanced catalytic activity. The total organic carbon (TOC) removal over the doped catalyst at 100 min reached 75.1%, 61.3% using Ru/Al₂O₃ catalyst and only 14.0% using ozone alone. Catalytic activity reached the maximum when 0.2% of ruthenium and 1.0% of cerium were simultaneously loaded onto Al₂O₃ support. Results of experiments on oxidation by ozone alone, adsorption of the catalyst, Ce ion’s and heterogeneous catalytic ozonation confirmed that the contribution of heterogeneous catalytic ozonation was about 50%, which showed the obvious effect of Ru-Ce/Al₂O₃ on catalytic activity.     

Fe2O3/AC脱除煤气中的Hg0

利用固定床反应器在模拟煤气条件下研究了活性焦(AC)负载Fe_2O_3催化剂(Fe_2O_3/AC)对气态Hg~0的脱除,考察了Fe_2O_3负载、煅烧温度、空速、Hg~0浓度、H_2S等对Fe_2O_3/AC催化剂脱除Hg~0的影响及Fe_2O_3/AC催化剂的再生性能,采用扫描电镜(SEM)表征了Fe_2O_3在Fe_2O_3/AC上的分布状态.结果表明,Fe_2O_3/AC具有较高的脱除Hg~0能力,明显高于载体AC,主要缘于Fe_2O_3对Hg~0的催化氧化作用.Fe_2O_3/AC催化剂上负载的活性组分Fe_2O_3并不是均匀的分布在载体AC表面上,而是成块簇状分布状态.300℃煅烧温度下制备的Fe_2O_3/AC催化剂脱除Hg~0的能力最高.在5000—15000 h~(-1)的空速和21—200μg·m~(-3)的Hg~0浓度范围内,Fe_2O_3/AC催化剂具有良好的脱除Hg~0的能力.H_2S与Hg~0在Fe_2O_3活性位上存在竞争吸附、反应会降低Fe_2O_3/AC对Hg~0的脱除能力,但H_2S反应生成的单质S和FeS_x又可促进Hg~0的脱除.脱除Hg~0后的Fe_2O_3/AC催化剂可进行再生,再生后Fe_2O_3/AC仍具有良好的脱除Hg~0的能力.     

还原温度对Pd-CeO2/Al2O3催化剂加氢脱硫性能的影响

采用浸渍法制备CeO2改性的Pd/Al2O3加氢脱硫催化剂,考察了还原温度和还原-氧化预处理对Pd/Al2O3和Pd-CeO2/Al2O3催化剂加氢脱硫性能的影响.结果表明,Pd/Al2O3的活性受还原温度的影响很小.Pd-CeO2/Al2O3还原温度的升高使CeO2发生迁移,导致催化剂表面Pd原子数减少,同时削弱了Pd-Ce界面效应,从而使催化剂的活性降低.还原-氧化预处理使Pd-CeO2/Al2O3的活性有较大提高,预处理能促使Pd的再分散,增加了对H2的吸附活化能力,在Pd-Ce的界面效应共同作用下使催化剂拥有较高的活性.     

UV/Fe3+/H2O2体系降解活性艳橙X-GN废水的研究

采用UV/Fe3 /H2O2体系光解活性艳橙X-GN模拟废水,考察了X-GN,Fe3 和H2O2的初始浓度、初始pH值及温度对光解的影响,探讨了X-GN的降解途径和机理.结果表明,在8W低压汞灯(λ＝254nm)照射下,UV/Fe3 /H2O2能够有效地降解X-GN,在pH=3.0,T=50 ℃,时间为120 min,Fe3 和H2O2的初始浓度分别为2.5×10-5 mol·l-1和1.5×10-4 mol·l-1时,对含200 mg·l-1 X-GN模拟废水的色度去除率和矿化率分别达到100%和90.15%.用IC和GC/MS对X-GN降解的中间产物和最终产物进行分析,推导出UV/Fe3 /H2O2体系中X-GN降解的途径和机理.     

Fe-C-H_2O_2协同催化氧化处理印染废水

用Fe-C-H2O2协同催化氧化体系对印染工业废水的降解脱色处理进行了研究。对影响印染废水降解的几种因素如铁屑/碳粒质量比、双氧水的质量分数、废水pH等进行考察。试验结果表明,对于色度为650度和ρ（COD）为468mg·L-1的印染废水,在废水pH=4.8的情况下,当铁屑/碳粒质量比为25∶1、H2O2用量为150mg·L-1、催化反应30min时,印染废水的脱色率达98%以上,CODCr去除率可达78%。与Fe-C微电解法相比,Fe-C-H2O2协同催化氧化方法对印染废水的脱色能力和去除COD,表现出了更好的处理效果。     

过渡金属对Pt Rh Pd/Al2O3催化剂性能的影响

研究了过渡金属(重点考察了铜)对Pt Rh Pd／Al2O3催化剂尾气净化效能的影响,并应用XRD,TPD,TPR等手段对过渡金属在Pt Rh Pd／Al2O3催化剂中的作用机制进行了探讨．结果表明,过渡金属对Pt Rh Pd／Al2O3催化剂具有较大的改性作用,过渡金属与混合贵金属产生的协同效应有利于催化剂活性的提高．     

Fe0.5Zn0.5Al2O4 尖晶石催化剂催化湿式氧化降解苯酚的稳定性

研究了Fe0.5Zn0.5Al2O4尖晶石型复合氧化物催化剂在催化湿式氧化处理苯酚废水中的性能.结果表明,在150℃下苯酚就能完全被去除,COD去除率达到94%.催化剂中铁的溶出量随着反应时间的增加经历了一个先增加后减小的过程;而且最终出水铁离子浓度随催化剂用量、氧分压、苯酚溶液pH值的增加而减少,随苯酚浓度的增加而增加.     

Evidence for a new mechanism of Fe2O3 decomposition in lightweight aggregate formation

Hematite (Fe₂O₃) chemical reduction into FeO and Fe₃O₄ by releasing O₂ at high temperatures is considered one of the generally accepted mechanisms for processing waste minerals and clay into lightweight aggregate construction materials. In many case studies, this mechanism has not been strictly confirmed. To verify whether hematite can effectively release O₂ at 1,000–1,260°C, a material containing hematite, simulating waste sediments from a Taiwanese reservoir, was shaped into pellets and fired into lightweight aggregates at high temperatures for 20 min and studied with various techniques. As revealed by the X-ray absorption near-edge structure technique, almost all the hematite remained as Fe(III) in the pellets when fired at 1,000–1,260°C, implying a negligible release of O₂ leading to the creation of pores. This finding shows that the generally accepted mechanism for lightweight aggregate formation associated with hematite decomposition into FeO, Fe₃O₄, and O₂ is invalid. Furthermore, Fe(III)-containing composites were formed in the fired pellets. Although firing at 1,000°C can trigger the decomposition of the components K₂CO₃, Na₂CO₃, and CaCO₃ with a release of CO₂, the sintering reaction was seemingly too weak to encapsulate the gases effectively. For pellets fired at 1,050–1,150°C, pores grew in size because the sintering reaction sufficed to generate a glassy phase that could better encapsulate gases.     

铝、铁聚合机理初探

向聚合氯化铁预聚体中缓慢加入Al3+离子和碱化剂制备铝、铁共聚物(CPAF);红外图谱和27Al核磁共振图谱解析、XRD相结构分析说明、Al3+、Fe3+离子进行了有效的共聚;聚集态形貌特征表明所制备的CPAF集中了聚合氯化铝(PAC)和聚合氯化铁(PFC)的优势形态,即聚集体细长,规整,尺寸较大且均匀;单分子分布形态的粒径测定结果表明,聚合度的大小顺序为:PAC>CPAF>PFC.     

Role of Rh promoter on increasing stability of Au/Al2O3 catalyst for CO oxidation at low temperature

The Au/Al₂O₃ and Au–Rh/Al₂O₃ catalysts were prepared by deposition–precipitation. The promotional effect of Rh on the performance of the Au/Al₂O₃ catalyst for CO oxidation was studied. The results indicate that using Au/Al₂O₃ catalyst, CO can be completely oxidized at 0°C or much lower temperature but the catalyst deactivated very fast. Rh can improve the stability of Au/Al₂O₃ catalyst more than 10 times, which gives an important hint to develop high stable catalyst for CO oxidation at low temperature.     

The effect of preparation conditions of Pt/Al2O3 on its catalytic performance for the H2-SCR in the presence of oxygen

Selective catalytic reduction of NO _x by H₂ in the presence of oxygen has been investigated over Pt/ Al₂O₃ catalysts pre-treated under different conditions. Catalyst preparation conditions exert significant influence on the catalytic performance, and the catalyst pre-treated by H₂ or H₂ then followed by O₂ is much more active than that pre-treated by air. The higher surface area and the presence of metallic Pt over Pt/Al₂O₃ pre-treated by H₂ or pretreated by H₂ then followed by O₂ can contribute to the formation of NO₂, which then promotes the reaction to proceed at low temperatures.     

低温种子聚合法制备磁载纳米TiO2光催化剂及其对苯酚的光催化降解

通过种子聚合法,以聚乙烯亚胺(PEI)处理过的纳米Fe2O4为磁核,在低温(95℃)、中性(pH=7左右)条件下,制备了一种磁载TiO2光催化剂.利用Zeta电位仪、透射电子显微镜(TEM)、X射线衍射仪(XRD)、傅里叶红外分光光度计(FT-IR)、振动样品磁强计(VSM)测试方法对磁核的表面电位、催化剂的形貌、物相...     

Correction to: Facile synthesis of the magnetic metal–organic framework Fe3O4/Cu3(BTC)2 for efficient dye removal

Environmental Chemistry Letters - Dyeing wastewaters present high hazards for the environment and human health. Advanced dye removal may be achieved by magnetic metal–organic frameworks...     

磁性Fe3O4@Mg(OH)2去除水中络合态三价铬

本实验采用一步水热法合成了Fe_3O_4@Mg(OH)_2材料,并将其用于吸附水中络合态的Cr(Ⅲ)-EDTA,通过X射线衍射(XRD)、红外光谱(FTIR)、比表面积(BET)、扫描电镜(SEM)、热重(TGA)和X射线光电子能谱(XPS)等来表征材料的结构和表面特性.结果表明,Mg(OH)_2已经成功的负载到了Fe_3O_4的表面,对水中络合态Cr(Ⅲ)-EDTA有较好的吸附能力,最大吸附量为15.52 mg·g~(-1),吸附等温线符合Langmuir等温线,吸附动力学可用拟二级动力学拟合,随着pH的增加吸附量不断减少,水中高浓度的阳离子对吸附产生促进作用,并且脱附实验证明材料有很好的可循环利用能力.     

Fe2+/H2O2催化氧化2,4-二氯苯氧乙酸的机理研究

利用Fe^2 ／H2O2对2,4-二氯苯氧乙酸(2,4-D)进行催化氧化,通过GC-MS和HPLC检测到反应过程的中间产物为2,4-二氯苯酚、邻氯苯酚和对氯苯酚,氯离子则是从这些中间产物上释放．通过离子色谱检测到小分子酸,如乙醇酸、乙醛酸、顺丁烯二酸．提出了2,4-D的Fe^2 ／H2O2降解的可能历程。     

Catalytic ozonation performance and surface property of supported Fe3O4 catalysts dispersions

Fe₃O₄ was supported on mesoporous Al₂O₃ or SiO₂ (50 wt.%) using an incipient wetness impregnation method, and Fe₃O₄/Al₂O₃ exhibited higher catalytic efficiency for the degradation of 2,4-dichlorophenoxyacetic acid and para-chlorobenzoic acid aqueous solution with ozone. The effect and morphology of supported Fe₃O₄ on catalytic ozonation performance were investigated based on the characterization results of X-ray diffraction, X-ray photoelectron spectroscopy, BET analysis and Fourier transform infrared spectroscopy. The results indicated that the physical and chemical properties of the catalyst supports especially their Lewis acid sites had a significant influence on the catalytic activity. In comparison with SiO₂, more Lewis acid sites existed on the surface of Al₂O₃, resulting in higher catalytic ozonation activity. During the reaction process, no significant Fe ions release was observed. Moreover, Fe₃O₄/Al₂O₃ exhibited stable structure and activity after successive cyclic experiments. The results indicated that the catalyst is a promising ozonation catalyst with magnetic separation in drinking water treatment.     

磁性Fe3O4/石墨烯异质结固定漆酶特性及其对水中双酚A的降解研究

以磁性石墨烯为载体制备了磁性石墨烯固定化漆酶,考察了固定化漆酶的酶学特性及其对双酚A（BPA）的降解效能。结果表明,氧化石墨烯的比表面积高达726.34 m2·g-1,与游离漆酶相比,经过石墨烯固定化后漆酶对酸的适应能力、耐热性和贮存稳定性均有所提高,pH值2.0~4.0范围内固定化漆酶活性较为稳定;加入变性剂尿素（1 mol·L-1）后,固定化漆酶的相对活性为87%,游离漆酶相对活性仅为63.02%,固定化导致抗变性剂能力增强。固定化漆酶和游离漆酶活性分别在45和40℃时达到最大值。与游离漆酶相比,固定化漆酶最佳反应温度升高了5℃,且在50℃时,固定化漆酶的相对活性依然保持在95.11%;25℃,pH值4.0条件下保存10 d,固定化漆酶活性为最初活性的82.57%;固定化漆酶具有良好的重复利用性,重复利用10次后,漆酶活性仍为最初活性的82.01%。固定化酶的米氏常数Km为5.38×10-4 mol·L-1,较游离酶的大,说明固定化酶与底物的亲和力比游离酶小。磁性石墨烯固定化漆酶具有良好的吸附能力,可吸附-催化氧化水中的 BPA,且石墨烯良好的吸附作用促进了催化反应,水中BPA质量浓度为15 mg·L-1时,经过18 h反应,BPA的去除率能达到82.14%左右。本研究的结果为石墨烯新型材料固定化漆酶及其应用提供了参考。