焙烧温度对Ti(SO_4)_2/CS催化二甲醚直接氧化合成聚甲氧基二甲醚性能的影响

采用等体积浸渍法制备了活性炭球(CS)负载Ti(SO_4)_2的双功能催化剂,考察了焙烧温度对Ti(SO_4)_2/CS催化剂选择氧化二甲醚(DME)直接合成聚甲氧基二甲醚(DMMx)催化性能的影响。结果表明,不同焙烧温度制备的Ti(SO_4)_2/CS催化剂表现出明显的催化活性差异,280℃焙烧的30%Ti(SO_4)_2/CS催化剂具有最佳性能,DME转化率为11.7%,DMM1-3的选择性达到75.8%,其中,DMM_(2,3)选择性在30%以上。采用SEM、XRD、Raman、TG、NH_3-TPD及XPS等表征手段研究了催化剂的结构及表面性质。焙烧温度改变了活性炭球表面官能团的分布,进而影响了Ti(SO_4)_2的分散状态,调变了酸中心种类和数量,尤其是弱酸和中强酸的比例,使催化剂表面酸性强弱呈现不同梯度,催化剂的酸性和氧化还原性位达到比较合理的匹配,进一步促进了C-O链的增长。     

给不用硫酸铁制备氢氧化铁胶体加几个注释

通过对Fe_2(SO_4)_3的水溶性和用FeCl_3溶液制备Fe(OH)_3胶体分散系中的成分及硫酸盐(SO_4~(2-))对Fe(OH)_3胶体稳定性的影响的分析,得出不宜用Fe_2(SO_4)_3制备Fe(OH)_3胶体的原因是SO_4~(2-)比Cl-较易被界面吸附,所以在溶剂化层内的负电荷数增加,扩散层内的负电荷数减少,扩散层变薄,Fe(OH)_3胶粒相互碰撞容易发生聚沉。     

不同前驱体制备的SO_4~(2-)/AC催化剂在二甲醚直接氧化合成聚甲氧基二甲醚中的反应性能

分别用硫酸、硫酸铵作为前驱体,活性炭(AC)作为载体,采用浸渍法制备了SO_4~(2-)/AC双功能催化剂(SO_4~(2-)离子和AC载体分别提供催化剂的酸性和氧化还原性),考察了其在二甲醚(DME)直接氧化合成聚甲氧基二甲醚(DMMx)反应中的催化性能。结果表明,不同前驱体制备的SO_4~(2-)/AC催化剂表现出显著的催化活性差异。40%H_2SO_4/AC催化剂具有较好的反应活性,DME转化率为8.4%,DMM1-2的选择性达到59.7%,并且没有COx的生成;而在40%(NH_4)_2SO_4/AC催化剂上,反应主要生成了COx,DMM选择性仅2.7%,且无DMM2生成。XRD、BET、NH_3-TPD及O_2-TPD-MS等表征结果显示,H_2SO_4/AC催化剂中适量的弱酸性位和氧化还原性位有利于DME直接氧化合成DMMx。经过SO_4~(2-)修饰的催化剂促进了O2在活性炭表面的活化;前驱体H_2SO_4的加入提高了催化剂表面的弱酸性位数量,而(NH_4)_2SO_4的引入却促使催化剂表面产生中强酸性位。     

制备工艺对Mn-Fe/ZSM-5催化剂在NH3-SCR催化还原反应中催化性能的影响

分别采用共沉淀法和浸渍法、不同铁前驱物以及不同焙烧温度等研究了制备工艺对Mn-Fe/ZSM-5催化剂的结构、化学组分及NH3-SCR活性的影响。结果显示,当采用Fe(NO3)3作为Fe前驱物,并用共沉淀法制备、300°C焙烧条件下得到的MFZ-CP-N-300样品低温活性最优,在120°C时,其NO的转化率达到96.7%,120-300°C范围内NO转化率始终保持在95%以上。同时利用XRD、NH3-TPD、XPS、SEM、TEM、氮吸附等手段对催化剂结构、晶相、酸位、锰铁氧化物的化学形态及表面的形貌特征进行表征分析。结果表明锰铁氧化物分别以MnO2-Mn2O3和Fe2O3的形式高度分散于催化剂表面,特别是当Mn4+/Mn3+比例为1.254时,有较强的表面中强酸和较多的酸位数,从而增加了NH3的吸附能力,提高NO的转化率。     

钕铁硼废料(NH_4)_2SO_4焙烧法回收稀土

将钕铁硼废料与(NH_4)_2SO_4混合后焙烧,选择性回收钕铁硼废料中的稀土成分。采用单因素控制变量的方法对焙烧过程中的焙烧温度、焙烧时间、钕铁硼与(NH_4)_2SO_4混料质量比进行研究,结合稀土、铁等浸出率的影响,结果表明:焙烧温度400℃,焙烧时间120 min,钕铁硼与(NH_4)_2SO_4混料质量比1∶2,该条件下稀土可以获得较高的浸出率,约为92%,而Fe的浸出率仅为3%。通过对原料和焙烧后的产物进行热力学、扫描电镜、 X射线衍射和热重差热分析,综合分析得知钕铁硼废料中的主要成分REFeO_3, Fe_2O_3, RE_2O_3和Al_2O_3等发生硫酸化反应,生成RE_2(SO_4)_3和(NH_4)_3Fe(SO_4)_3及(NH_4)Al(SO_4)_2等。升高温度不利于REFeO_3的反应,从而抑制大部分Fe的硫酸化。经过焙烧,稀土以可溶性硫酸盐的形式存在,铁铝等杂质保持一个低的浸出率大部分留在渣中。     

制备工艺对Mn-Fe/ZSM-5催化剂在NH_3选择催化还原NO反应中催化性能的影响（英文）

分别采用共沉淀法和浸渍法、不同铁前驱物以及不同焙烧温度等研究了制备工艺对Mn-Fe/ZSM-5催化剂的结构、化学组分及NH3-SCR活性的影响.结果显示,当采用Fe(NO3)3作为Fe前驱物,并用共沉淀法制备、300℃焙烧条件下得到的MFZ-CP-N-300样品低温活性最优,在120℃时,其NO的转化率达到96.7%,120~300℃范围内NO转化率始终保持在95%以上.同时利用XRD、NH3-TPD、XPS、SEM、TEM、氮吸附等手段对催化剂结构、晶相、酸位、锰铁氧化物的化学形态及表面的形貌特征进行表征分析.结果表明锰铁氧化物分别以Mn O2-Mn2O3和Fe2O3的形式高度分散于催化剂表面,特别是当Mn4+/Mn3+比例为1.254时,有较强的表面中强酸和较多的酸位数,从而增加了NH3的吸附能力,提高NO的转化率.     

SO_4~(2-)功能化处理对Fe_2O_3催化剂上氨选择性催化还原NO_x性能的促进机理研究

采用沉淀法制备了Fe(OH)_3和Fe_2O_3。通过硫酸化处理得到SO_4~(2-)/Fe(OH)_3和SO_4~(2-)/Fe_2O_3两种催化剂,并将其应用于氨选择性催化还原NO_x(NH_3-SCR)反应,研究了SO_4~(2-)功能化处理对Fe_2O_3催化剂上NH_3-SCR脱硝性能的促进机理。结果表明,与纯的Fe_2O_3相比,硫酸化处理得到的催化剂上SCR活性得到显著提升;其中,SO_4~(2-)/Fe(OH)_3表现出更加优异的催化性能,在250-450℃时NO_x转化率高于80%,且具有优异的稳定性和抗H_2O+SO_2性能。XRD、Raman、TG、FT-IR、H_2-TPR、NH_3-TPD和in situ DRIFTS等表征结果显示,硫酸功能化处理能抑制Fe_2O_3的晶粒生长,同时SO_4~(2-)与Fe~(3+)结合形成硫酸盐复合物,提高了催化剂表面酸性位点的数量和酸强度,抑制了Fe_2O_3上的氨氧化反应,从而提高了其脱硝催化性能。     

焙烧温度对Mn-Fe/CeO2-TiO2催化剂低温NH3选择性催化还原NO的影响

采用等体积浸渍法制备了Mn-Fe/CeO2-TiO2催化剂,考察了不同焙烧温度对其NH3选择性催化还原(SCR)NO活性及催化剂性能的影响。并用N2吸附-脱附,X射线衍射(XRD)和X射线光电子能谱(XPS)等手段对催化剂进行了表征。活性结果表明,随着焙烧温度的升高,Mn-Fe/CeO2-TiO2催化剂的催化活性先升高后降低。其中焙烧温度为500℃时Mn/CeO2-TiO2的NH3-SCR活性最佳,该催化剂在113～250℃之间表现出了良好NO去除效率。表征结果表明,500℃焙烧时,催化剂中Fe和Mn物种在CeO2-TiO2表面的分散效果最好。500℃焙烧时Mn-Fe/CeO2-TiO2表面Mn以+4价存在,Fe以+3、+2价存在,而Ce以+4、+3存在。     

(NH4)2SO4在TiO2表面上的行为研究

硫助金属氧化物(sulfate promoted metal oxides)是一类新型固体酸催化剂,可用于多种酸催化反应.用(NH_4)_2SO_4、SO_3、SO_2或H_2S 作为助剂,以Fe_2O_3、TiO_2和ZrO_2为底物均可制得硫助金属氧化物(SPMO).     

生物质铁盐催化加氢热解产生生物油与气态烃的研究

利用加压固定床反应器进行了松木催化加氢热解实验(终温600-700℃、氢压5.0 MPa),考察了硝酸铁和硫酸亚铁两种铁盐对热解产物产率及分布的影响。研究发现,Fe(NO_3)_3能够显著促进生物炭加氢生成甲烷,碳转化率高达97.4%,CH_4产率达21.2%,无水生物油产率为32.8%(产率基准均为干燥无灰生物质),生物油中含氧量降低,轻质芳烃产率增加,其中,苯、甲苯和二甲苯(BTX)产率为2.6%。而FeSO_4迥异于Fe(NO_3)_3,具有抑制气态烃和生物油生成的作用。机理研究表明,Fe(NO_3)_3在加氢过程中主要形成α-Fe,并促使生物炭形成无定型和多孔结构,从而有利于其加氢生成甲烷,而FeSO_4则部分转化为Fe_2S_3,由此可致使铁催化剂失活。     

Synthesis of Fe‐MCM‐41 from silatrane and FeCl3 via sol–gel process and its epoxidation acivity

An iron‐containing mesoporous molecular sieve, or Fe‐MCM‐41, was successfully synthesized the via sol–gel technique using silatrane and FeCl₃ as the silicon and iron sources, and was characterized using various techniques. Many factors were investigated, namely, reaction temperature and time, calcination rate, and iron amount in the reaction mixture. It was found that the optimum conditions in which to synthesize Fe‐MCM‐41 was to carry out the reaction at 60 °C for 7 h using a 1 °C min^?1 calcination rate and a 550 °C calcination temperature. The catalytic activity and selectivity of styrene epoxidation using hydrogen peroxide showed that the selectivity of the styrene oxide reached 65% at a styrene conversion of 22% over the 1%wt catalyst. Copyright © 2008 John Wiley & Sons, Ltd.     

掺杂TiO2介孔材料的合成与表征

基于溶胶-凝胶过程, 以非表面活性剂有机小分子三乙醇胺为模板剂, 合成了TiO2及Fe3+/V5+-TiO2介孔材料. 利用XRD, TEM, BET, UV-Vis DRS等手段表征了材料的结构、形貌、比表面积、孔径分布及吸光性能. 研究结果表明, 用乙醇萃取法脱除模板剂可形成具有蠕虫状孔道结构的TiO2介孔材料, 而利用焙烧法在450 ℃脱除模板剂时可引起孔道的塌陷. 掺杂Fe3+或V5+可稳定材料的介孔结构, 适宜的掺杂摩尔分数为0.5％. 于450 ℃下焙烧后, 掺杂Fe3+/V5+的TiO2的平均孔径分别为10.5和9.6 nm, 比表面积分别达到103.59和90.80 m2/g. 相对于P25光催化剂, 掺杂Fe3+或V5+的TiO2吸光带边红移至可见光区, 说明掺杂离子在此合成过程中可有效地进入TiO2的晶格结构而引起其微观电子结构的改变.     

Elimination of 4‐chlorophenol in aqueous solution by the Novel Pd/MIL‐101(Cr)‐Hydrogen‐Accelerated catalytic fenton system

Excessive consumption of Fe (II) and massive generation of sludge containing Fe (III) from classic Fenton process remains a major obstacle for its poor recycling of Fe (III) to Fe (II). Therefore, the MHACF‐MIL‐101(Cr) system, by introducing H₂, Pd⁰ and MIL‐101(Cr) into Fenton reaction system, was developed at normal temperature and pressure. In this system, the reduction of Fe^III back to Fe^II by solid catalyst Pd/MIL‐101(Cr) for the storage and activation of H₂, was accelerated significantly by above 10‐fold and 5‐fold controlled with the H₂‐MIL‐101(Cr) system and H₂‐Pd⁰ system, respectively. However, the concentration of Fe (II) generated by the reduction of Fe (III) could not be detected with the only input of H₂ and without the addition of MOFs material. In addition, the apparent consumption of Fe (II) in MHACF‐MIL‐101(Cr) system was half of that in classical Fenton system, while more Fe (II) might be reused infinitely in fact. Accordingly, only trace amount of Fe (II) vs H₂O₂ concentration was needed and hydroxyl radicals through the detection of para‐hydroxybenzoic acid (p‐HBA) as the oxidative product of benzoic acid (BA) by·OH could be continuously generated for the effective degradation of 4‐chlorophenol(4‐CP). The effects of initial pH, concentration of 4‐CP, dosage of Fe²⁺, H₂O₂ and Pd/MIL‐101(Cr) catalyst, Pd content and H₂ flow were investigated, combined with systematic controlled experiments. Moreover, the robustness and morphology change of Pd/MIL‐101(Cr) were thoroughly analyzed. This study enables better understanding of the H₂‐mediated Fenton reaction enhanced by Pd/MIL‐101(Cr) and thus, will shed new light on how to accelerate Fe (III)/Fe (II) redox cycle and develop more efficient Fenton system.     

Fe-MSU-1介孔分子筛的合成及其催化苯酚羟基化性能

以月桂醇聚氧乙烯醚为模板剂,在中性条件下成功合成了Fe-MSU-1介孔分子筛.采用X射线衍射、傅里叶变换红外光谱、紫外-可见吸收光谱、电子自旋共振谱、透射电镜、低温N2吸附和电感耦合等离子体原子发射光谱对样品进行了表征.考察了Fe-MSU-1分子筛在苯酚羟基化反应中的催化性能以及工艺条件对苯酚羟基化反应的影响.结果表明,Fe3 离子进入了分子筛骨架,Fe-MSU-1分子筛具有均一的蠕虫状介孔结构,平均孔径约为2.9nm.在焙烧后的Fe-MSU-1样品中,Fe3 主要以四配位的形式存在,无骨架外Fe2O3物种形成.以水为溶剂,在苯酚/H2O2摩尔比为3,反应温度353K,反应时间7h的条件下,苯酚和H2O2的转化率以及苯二酚的选择性分别达到20.4%,96.9%和99.6%.     

Heterogeneous Fenton degradation of azo dye 4BS over Co–Mn–Fe ternary hydrotalcites

This work described the application of Co–Mn–Fe hydrotalcites (Co–Mn–Fe LDHs) as heterogeneous catalysts for Fenton reaction process. The Co–Mn–Fe LDHs were synthesized by the co-precipitation method and were characterized by X-ray diffractometry (XRD), infrared spectroscopy (IR), zeta potential, and BET surface area measurement. The catalytic activity of different kinds of hydrotalcites was evaluated by the degradation of Direct Scarlet 4BS (4BS). The Co–Mn–Fe LDHs showed the best catalytic performance among four catalysts. The presence of the Mn²⁺/Mn³⁺ at surface of catalyst could accelerate the reduction of Co³⁺–Co²⁺, and then increased in the catalytic activity of the Co–Mn–Fe LDHs. The effect of initial pH, catalyst dosage, dye concentration, and reaction temperature on the degradation of 4BS had been investigated. Radical reaction mechanism was proposed by the addition of radical scavenger. The degradation kinetic followed pseudo-first-order model. The activation energy of Co–Mn–Fe LDHs was determined to be 37.3 kJ/mol. The catalytic activity of Co–Mn–Fe LDHs was maintained after four cycles of reaction, which proved the reusability of catalyst. Finally, the possible reaction mechanisms involved in the heterogeneous Fenton system were proposed.     

Selective chemical vapor deposition synthesis of double-wall carbon nanotubes on mesoporous silica

Double-wall carbon nanotubes (DWNTs) have been selectively synthesized over Fe/Co loaded mesoporous silica by catalytic chemical vapor deposition of alcohol. Several silica materials with desired pore diameter and morphology have been investigated for the DWNT growth. The diameter distribution and selectivity of the DWNT are found to depend on the reaction temperature, pore size, and thermal stability of the support material. A high-yield synthesis of DWNTs has been achieved at 900 degrees C over high-temperature stable mesoporous silica. The outer diameter of DWNTs is found to be in the range of 1.5-5.4 nm with a "d" spacing of 0.38 +/- 0.02 nm between inner and outer layers, which is much larger than those of multiwall carbon nanotubes.     

Highly loaded and thermally stable Cu-containing mesoporous silica-active catalyst for the NO + CO reaction

We report the synthesis of a highly loaded and thermally stable Cu-containing mesoporous silica, which was developed by making use of poly(acrylic acid) (Pac) assembled with surfactant (C(16)TAB), as template. On this backbone, TEOS and Cu(II) hydrolysis takes place leading to the development of the final mesostructure. Poly(acrylic acid) is used not only as a micelle structural component but also as a complexation agent for Cu(II) species resulting in high metal loading and increased thermal stability of the mesoporous network. The original uncalcined material possesses hexagonal ordering, while upon calcination it is transformed into a wormlike mesoporous network with metal loading >14 wt % Cu. An evaluation of its performance as heterogeneous catalyst in NO reduction by CO shows catalytic activity comparable with that of noble metal catalysts. Complete NO conversion, with >90% selectivity to N(2), was achieved between 190 and 200 degrees C. The material retained its structure and catalytic activity after 24-h testing at the maximum catalytic conversion of NO and CO.     

Fe-Al 柱撑膨润土的制备及其非均相Fenton降解橙黄II

通过离子交换方法制备不同Fe含量的Fe-Al柱撑膨润土,并且研究了其作为非均相Fenton催化剂降解橙黄II的性能.通过X射线粉末衍射(XRD),比表面积(SBET),傅里叶变换红外(FTIR)光谱,拉曼(Raman)光谱和扫描电子显微镜(SEM)研究其结构特征.结果显示,钠化膨润土的层间距为1.24 nm,经过柱撑之后,Al柱撑膨润土的层间距增大到1.77 nm,Fe-Al柱撑膨润土为1.72 nm左右,并且比表面积也有明显增大.XRD和Raman结果表明Fe/(Fe+Al)摩尔比达到20%时,样品中出现α-Fe2O3,膨润土未能形成柱撑.在橙黄II初始浓度为100 mg L-1,催化剂用量为1.0 g L-1,温度为40°C,pH为3.0,H2O2初始浓度为10 mmol L-1的条件下,考察了柱撑膨润土的Fenton催化活性.结果表明,Fe-Al柱撑膨润土的催化性能随着Fe含量的增多先增大后略有降低,当Fe/(Fe+Al)摩尔比为10%时达到最大,橙黄II溶液在4 h内色度去除率和化学需氧量(CODCr)去除率分别达到100%和87.73%,并且降解反应为非均相Fenton反应.研究了Fe-Al柱撑膨润土的重复使用性.催化剂循环使用4次,仍然具有良好的活性.     

A new mesoporous micelle-templated silica route for enzyme encapsulation

A new mesoporous micelle-templated silica (MTS) route for enzyme encapsulation is presented. The pore structure is given by a new association oflecithin (double chain surfactant) and dodecylamine as cosurfactant. To enhance and to well protect the enzyme activity, lactose was loaded in the synthesis. The mixed-micelles give after the addition of tetraethyl orthosilicate a well-ordered mesoporous material with a spongelike rigid structure stable after calcination at 550 degrees C. The size of the pores lies between 30 and 40 A, matching well with the size of the lipases. The activity of this heterogeneous catalyst was tested in the hydrolysis of the ethylthiodecanoate. These new biocatalysts were very active, more than hydrophobic sol-gel materials and commercially available sol-gel encapsulated lipase. This new MTS synthesis route allows one to encapsulate in one-step various enzymes, even those that are very fragile.     

Synthesis and characterization of ordered hexagonal and cubic mesoporous tin oxides via mixed-surfactant templates route

Ordered hexagonal and cubic mesoporous tin oxides were synthesized for the first time in the presence of mixed cationic and neutral surfactants (a mixture of cetyltrimethylammonium bromide cationic surfactant and dodecylamine neutral surfactant) with different alkali and simple inorganic precursors at room temperature. In the synthesis systems, the dodecylamine neutral surfactant may function as a polar organic cosolvent and cosurfactant. The formation of the tin oxide mesostructured material was proposed to be due to the presence of hydrogen-bonding interactions between the supramolecular template and inorganic precursors Sn4+ and OH-, which were assumed to self-assemble around the cationic surfactant molecules. The materials are characterized by X-ray powder diffraction, transmission electron microscopy, thermogravimetric analysis, and N2 adsorption/desorption isotherm. The surface areas of materials evaluated from the N2 sorption isotherms are about 248 m(2)/g for hexagonal mesoporous tin oxide (SnH) and 281 m(2)/g for cubic mesoporous tin oxide (Sn-C) for calcination at 350 degrees C.