层叠层技术组装纳米沸石——沸石涂饰纤维和沸石空 心纤维

以纳米沸石为基元构件,通过层(layer-by-layer)组装技术在碳纤维模板上成功制备了纳米沸石涂饰纤维(zeolitecoatedfibers),焙烧除去碳纤维模板后,制微了完整的沸石空心纤维(hollowzeolitefibers),并系统研究了它们的制备条件和材料结构。发现纳米沸石胶体溶液的pH值是制备沸石涂饰纤维和空心沸石纤维的关键因素,其它条件,诸如吸附液的离子强度,每层吸附后的干燥以及每次干燥前是否用PDDA溶液预浸泡,对纤维的完美性也有影响。通过改变吸附纳米沸石的类型和层数可能调变沸石层的组成和厚度,而交替吸附不同的纳米沸石可能制备复合沸石涂饰纤维及复合空心沸石纤维。     

由纳米晶前驱体组装有序介孔silicalite-1分子筛

采用两步法将不同尺寸的silicalite-1分子筛纳米晶种通过自组装合成了一系列有序介孔silicalite-1分子筛。首先将强碱性的silicalite-1前驱体分别加热不同时间得到纳米晶种,然后在类似合成SBA-15的强酸性条件下组装成有序的介孔材料。合成条件的剧烈变化阻止了分子筛晶种的继续长大,并在三嵌段共聚物模板的诱导下组装成有序介孔材料。这种“自下而上”的方法制备有序介孔分子筛同时包含微孔和介孔。氮气吸脱附结果表明所制备的介孔分子筛材料均表现了很大的比表面积(730 m2/g以上)。     

由纳米晶前驱体组装有序介孔silicalite-1分子筛（英文）

采用两步法将不同尺寸的silicalite-1分子筛纳米晶种通过自组装合成了一系列有序介孔silicalite-1分子筛.首先将强碱性的silicalite-1前驱体分别加热不同时间得到纳米晶种,然后在类似合成SBA-15的强酸性条件下组装成有序的介孔材料.合成条件的剧烈变化阻止了分子筛晶种的继续长大,并在三嵌段共聚物模板的诱导下组装成有序介孔材料.这种"自下而上"的方法制备有序介孔分子筛同时包含微孔和介孔.氮气吸脱附结果表明所制备的介孔分子筛材料均表现了很大的比表面积(730 m2/g以上).     

SiO2纳米粒子对溶胶凝胶涂层性能的影响

在高强钢表面制备了防护性溶胶凝胶涂层,并研究了不同浓度二氧化硅纳米粒子的加入对于涂层形貌、耐蚀性和硬度的影响。采用扫描电子显微镜(SEM)和电子能谱(EDS)观察了涂层的微观结构和成分;采用显微硬度计测试了涂层的硬度;采用电化学方法研究了二氧化硅纳米粒子的浓度对于涂层耐蚀性能的影响;采用傅里叶红外光谱研究涂层的化学结构,进而探讨了二氧化硅纳米粒子对于涂层的强化机理。结果显示涂层加入二氧化硅纳米粒子的最佳浓度为500 mg.L-1,此条件下的涂层表面均匀致密,有较高的硬度并且在3.5%NaCl溶液中体现出较好的耐蚀作用。纳米粒子在溶胶中反应形成活性羟基基团并与硅烷发生反应生成空间网状结构,从而强化涂层。     

高度b取向Silicalite-1分子筛膜的制备

以正硅酸乙酯(TEOS)为硅源, 四丙基氢氧化铵(TPAOH)为模板剂, 通过调变合成silicalite-1分子筛溶胶组成及反应时间等合成参数, 用原位水热晶化法在玻璃基底上制备了表面平整、连续性好且高度b取向的silicalite-1分子筛膜. 研究了溶胶组成及基底表面粗糙度与分子筛膜中晶体取向的关系, 讨论了晶化条件对分子筛膜厚度及膜中微晶尺寸及分布的影响, 实现了silicalite-1 沸石分子筛在基底表面的高度取向生长和膜中晶体大小及膜层微结构的调控. 本文描述的制备方法简单且重复性好. 此外, 还利用扫描电子显微镜(SEM)和X射线衍射(XRD)等分析方法对样品进行了表征.     

Poly(St-co-DMC)/SiO_2杂化及空心杂化纳米粒子的合成及表征

采用无皂乳液聚合法合成了聚(苯乙烯-co-甲基丙烯酰氧乙基三甲基氯化铵)(poly(St-co-DMC))纳米粒子,平均粒径约为100 nm.以此纳米粒子为模板,在接近室温及p H为中性的温和条件下,以四甲氧基硅烷(TMOS)为硅源,合成了poly(St-co-DMC)/Si O2杂化纳米粒子,TEM结果显示该纳米粒子具有明显的核壳结构,Si O2主要沉积在壳层.进一步通过四氢呋喃溶解制备得到具有空心结构的纳米粒子,这种空心结构纳米粒子的FTIR图谱中既有Si O2的信号,也有poly(St-co-DMC)的信号,说明空心纳米粒子的壳层不完全是Si O2,对空心纳米粒子的TGA结果分析计算得到Si O2的含量仅为69.7%,说明纳米粒子的壳层为杂化壳层,并且,这种壳层的厚度随着反应温度的升高、反应时间的延长、TMOS用量的增加及聚合物模板中DMC含量的增加而增大.     

多尺度结构Ag/PA6纳米纤维膜的制备及其催化性能

随着工业的进步,废水处理特别是印染废水的处理成为亟待解决的问题.银纳米粒子因其特殊的物理化学性能而表现出催化活性,但银纳米粒子的团聚限制了其使用,所以出现了一系列新的载体材料,如微球、薄膜和纤维等.其中电纺纳米纤维由于具有高比表面积,作为载体材料具有非常大的优势,而将常规电纺纳米纤维作为载体也已有报道.但是,将具有更高比表面积的电纺纳米纤维作为载体,特别是一种类似于树枝状结构的多尺度纳米纤维作为载体还鲜有报道.本文制备了一种多尺度结构的PA6纳米纤维膜,该纳米纤维膜由直径为50?120 nm的主纤维和10?50 nm的分支纤维构成;由于分支纤维的出现,多尺度结构纳米纤维膜的比表面积得到了提高,可以为银纳米粒子的负载提供更多附着位点.制备的多尺度结构纳米纤维膜通过银胶溶液浸渍成功地负载银纳米粒子,对制备的纳米纤维膜的形态、化学结构以及对亚甲基蓝的催化性能进行了探讨.SEM,EDS和TEM结果表明,银纳米粒子成功地负载在多尺度结构纳米纤维的表面,并且银纳米粒子的粒径以及负载量可以通过变换银胶溶液的浓度合理调控.此外,与常规PA6纳米纤维膜相比,多尺度结构纳米纤维膜更有利于银纳米粒子的分散,同样通过银胶溶液A浸渍,负载在多尺度结构纳米纤维上银纳米粒子粒径为8.6 nm,而负载在普通PA6纳米纤维上银纳米粒子粒径为11.2 nm.XPS分析表明,银纳米粒子成功地负载到多尺度结构纳米纤维上,并且经不同银胶溶液处理,纳米纤维膜的载银量不同.通过O的高能XPS分析发现,银纳米粒子与PA6分子间形成了配位键,这在一定程度上有利于Ag纳米粒子的固定,阻止了Ag纳米粒子的团聚.Ag/PA6纳米纤维膜以及多尺度结构Ag/PA6纳米纤维膜催化降解实验表明,多尺度结构Ag/PA6纳米纤维膜具有较高的催化活性,反应2 h后对10 mg/L亚甲基蓝的降解率达到98.13%,并且降解过程符合伪一级动力学.不同浸渍液浓度处理纳米纤维膜催化实验表明,Ag纳米粒子的大小以及含量都会影响纳米纤维的催化活性,纳米粒子粒径越小,其催化活性越高;不同NaBH4加入量催化体系催化实验表明,随着NaBH4加入量的增大,催化体系的降解率增高,其对催化体系的催化性能起着至关重要的作用;其他条件一定,随着染料初始浓度的增大,催化体系的催化性能下降;循环实验表明,经5次循环之后,其降解率仍高达83.5%,该纳米纤维膜具有一定的循环使用性能.     

介孔-微孔复合材料的水热稳定性及其催化裂化性能

采用无模板剂的溶胶凝胶法制备了一系列具有均一介孔和MFI沸石微孔的复合材料.与MCM-41相比,包含silicalite-1沸石结构的复合材料的水热稳定性得到显著改善.1,3,5-三异丙苯的催化裂化反应结果表明,与商品HZSM-5沸石相比,包含ZSM-5沸石结构的复合材料具有更高的催化活性和抗积炭性能.三异丙苯的转化率...     

多尺度结构Ag/PA6纳米纤维膜的制备及其催化性能（英文）

随着工业的进步,废水处理特别是印染废水的处理成为亟待解决的问题.银纳米粒子因其特殊的物理化学性能而表现出催化活性,但银纳米粒子的团聚限制了其使用,所以出现了一系列新的载体材料,如微球、薄膜和纤维等.其中电纺纳米纤维由于具有高比表面积,作为载体材料具有非常大的优势,而将常规电纺纳米纤维作为载体也已有报道.但是,将具有更高比表面积的电纺纳米纤维作为载体,特别是一种类似于树枝状结构的多尺度纳米纤维作为载体还鲜有报道.本文制备了一种多尺度结构的PA6纳米纤维膜,该纳米纤维膜由直径为50-120 nm的主纤维和10-50 nm的分支纤维构成;由于分支纤维的出现,多尺度结构纳米纤维膜的比表面积得到了提高,可以为银纳米粒子的负载提供更多附着位点.制备的多尺度结构纳米纤维膜通过银胶溶液浸渍成功地负载银纳米粒子,对制备的纳米纤维膜的形态、化学结构以及对亚甲基蓝的催化性能进行了探讨.SEM,EDS和TEM结果表明,银纳米粒子成功地负载在多尺度结构纳米纤维的表面,并且银纳米粒子的粒径以及负载量可以通过变换银胶溶液的浓度合理调控.此外,与常规PA6纳米纤维膜相比,多尺度结构纳米纤维膜更有利于银纳米粒子的分散,同样通过银胶溶液A浸渍,负载在多尺度结构纳米纤维上银纳米粒子粒径为8.6 nm,而负载在普通PA6纳米纤维上银纳米粒子粒径为11.2 nm.XPS分析表明,银纳米粒子成功地负载到多尺度结构纳米纤维上,并且经不同银胶溶液处理,纳米纤维膜的载银量不同.通过O的高能XPS分析发现,银纳米粒子与PA6分子间形成了配位键,这在一定程度上有利于Ag纳米粒子的固定,阻止了Ag纳米粒子的团聚.Ag/PA6纳米纤维膜以及多尺度结构Ag/PA6纳米纤维膜催化降解实验表明,多尺度结构Ag/PA6纳米纤维膜具有较高的催化活性,反应2 h后对10 mg/L亚甲基蓝的降解率达到98.13%,并且降解过程符合伪一级动力学.不同浸渍液浓度处理纳米纤维膜催化实验表明,Ag纳米粒子的大小以及含量都会影响纳米纤维的催化活性,纳米粒子粒径越小,其催化活性越高;不同NaBH_4加入量催化体系催化实验表明,随着NaBH_4加入量的增大,催化体系的降解率增高,其对催化体系的催化性能起着至关重要的作用;其他条件一定,随着染料初始浓度的增大,催化体系的催化性能下降;循环实验表明,经5次循环之后,其降解率仍高达83.5%,该纳米纤维膜具有一定的循环使用性能.     

基于葡聚糖自组装胶体粒子的分子印迹传感器的制备及电化学性能

首先,以光敏小分子肉桂酸(CINN)为疏水基元,通过酯化反应对葡聚糖(Dex)进行疏水改性,制备双亲性大分子Dex-CINN;然后,利用选择性溶剂法诱导Dex-CINN与模板分子葡萄糖(Glu)共组装,制备分子印迹胶体粒子(MINPs)。通过红外光谱(FT-IR)和核磁共振氢谱(1 HNMR)确定Dex-CINN的化学结构及改性率。利用Zeta电位及纳米粒度仪和透射电子电镜(TEM)对MINPs的粒径、电位及形貌进行表征。利用滴涂或电泳沉积的方法使MINPs在电极表面二次组装构建MINPs涂层,通过光交联固定涂层结构,再洗脱除去模板分子后得到分子印迹传感涂层。通过扫描电子显微镜(SEM)对两种分子印迹传感涂层的形貌进行表征,并进一步利用循环伏安法(CV)、差分脉冲溶出伏安法(DPSV)对比研究两种分子印迹传感涂层的分析检测性能。研究结果表明:通过滴涂或电泳沉积的方法均能在电极表面制备分子印迹传感涂层;相比于滴涂法,电泳沉积法所制备的分子印迹传感涂层连续均匀,所形成的传感器对Glu具有更好的响应性以及识别能力,检测下限更低。     

A simple synthesis of mesoporous carbons with tunable mesopores using a colloidal template-mediated vapor deposition polymerization

Mesoporous carbons with highly uniform and tunable mesopores were fabricated by one-step vapor deposition polymerization (VDP) using colloidal silica particles as templates and polyacrylonitrile (PAN) as a carbon precursor.     

破碎-絮凝法分离细长碳纳米管与碳纤维

根据碳纤维与细长碳纳米管耐磨性能与絮凝沉降性能的差异，提出了一种有效分离细长碳纳米管与碳纤维的物理方法——破碎-絮凝法.该方法包括研磨破碎、液相分散、絮凝沉降、过滤分离等步骤，可高效去除混杂于细长碳纳米管样品中的碳纤维，同时还可去除螺旋状碳纤维及细小碳颗粒等易悬浮杂质.纯化过程对细长碳纳米管无损伤.用电子显微镜和热重分析表征了纯化效果，并初步分析了纯化机理.     

Synthesis of porous carbon balls from spherical colloidal crystal templates

Spherical inverse opal (IO) porous carbon was produced utilizing silica colloidal crystal spheres as templates. The spherical colloidal crystals were obtained through the self-assembly of monodisperse particles inside an emulsion droplet with confined geometry. The templates were inverted using a carbon precursor, phenol-formaldehyde (PF) resol. We demonstrated a two-step synthesis involving the subsequent infiltration of the PF resol precursor into the spherical colloidal crystal template and a one-step synthesis using a silica colloidal solution containing dissolved PF resol. In the former case, the sizes of the IO carbon balls were controlled by the size of the colloidal crystal templates, and diameters of a few micrometers up to 50 μm were obtained. The average diameter of the macropores created by the silica particles was 230 nm. Moreover, meso-/macroporous IO carbon balls were created using block-copolymer templates in the PF resol. In the one-step synthesis, the concentration of PF resol in the colloidal solution controlled the diameter of the IO carbon balls. IO balls smaller than 3 μm were obtained from the direct addition of 5% PF resol. The one-step synthesis produced rather irregular porous structures reflecting the less ordered crystallization processes inside the spherical colloidal crystals. Nitrogen adsorption and cyclic voltammetry measurements were conducted to measure the specific area and electroactive surface area of the IO carbon balls. The specific area of the mesopores-incorporated IO carbon balls was 1.3 times higher than that of bare IO carbon balls. Accordingly, the meso-/macroporous porous carbon balls exhibited higher electrocatalytic properties than the macroporous carbon balls.     

Preparation and hydrogen storage properties of zeolite-templated carbon materials nanocast via chemical vapor deposition: effect of the zeolite template and nitrogen doping

Carbon materials have been prepared using zeolite 13X or zeolite Y as template and acetonitrile or ethylene as carbon source via chemical vapor deposition (CVD) at 550-1000 degrees C. Materials obtained from acetonitrile at 750-850 degrees C (zeolite 13X) or 750-900 degrees C (zeolite Y) have high surface area (1170-1920 m(2)/g), high pore volume (0.75-1.4 cm(3) g(-1)), and exhibit some structural ordering replicated from the zeolite templates. Templating with zeolite Y generally results in materials with higher surface area. High CVD temperature (> or =900 degrees C) results in low surface area materials that have significant proportions of graphitic carbon and no zeolite-type structural ordering. The nitrogen content of the samples derived from acetonitrile varies between 5 and 8 wt %. When ethylene is used as a carbon precursor, high surface area (800-1300 m(2)/g) materials are only obtained at lower CVD temperature (550-750 degrees C). The ethylene-derived carbons retain some zeolite-type pore channel ordering but also exhibit significant levels of graphitization even at low CVD temperature. In general, the carbon materials retain the particle morphology of the zeolite templates, with solid-core particles obtained at 750-850 degrees C while hollow shells are generated at higher CVD temperature (> or =900 degrees C). We observed hydrogen uptake of up to 4.5 wt % and 45 g H(2)/L (volumetric density) at -196 degrees C and 20 bar for the carbon materials. The hydrogen uptake was found to be dependent on surface area and was therefore influenced by the choice of zeolite template and carbon source. Zeolite Y-templated N-doped carbons had the highest hydrogen uptake capacity. Gravimetric and volumetric methods gave similar uptake capacity at 1 bar (i.e., 1.6 and 2.0 wt % for zeolite 13X and Y-templated N-doped carbons, respectively). Our findings show that zeolite-templated carbons are attractive for hydrogen storage and highlight the potential benefits of functionalization (nitrogen-doping).     

Preparation of Carbon Nanotubes by the Catalysis of Polymer Metal Complex on Porous Al203 Matrix

At present, synthesis of carbon nanotubes (CNTs) is normally conducted on a vapor-to-solid interface at ca. 500-3500℃ via various vapor phase methods, such as are discharge, laser ablation, catalytic pyrolysis and chemical vapor deposition, etc.1-2 Recently, channel materials (such as channels of alumina and of AlPO4-5 zeolite) 3 have been utilized as solid-state templates to grow CNTs inside the channel. Here we described a novel method to prepare the carbon nanotubes based on the decomposition of C2H2 gas on the Co-Ni catalyst anchored by polymer complex on the porous A12O3 matrix. The degree of graphitization of synthesized CNTs and catalysts are of great interest.     

Design and characterization of three-dimensional carbon nanotube foams

We demonstrate a new method that makes use of colloidal silica templates to fabricate porous three-dimensional architectures of carbon nanotubes (CNTs). CNTs were grown on monolayered and multilayered structures of colloidal silica using chemical vapor deposition. Porous CNT membranes and three-dimensional carbon nanotube foams were obtained by treating these silica-CNTs structures with HF. The membranes and foams of CNT so obtained were chemically and mechanically stable and were characterized by using scanning electron microscopy and energy dispersive spectroscopy.     

Preparation of submicron polypyrrole/poly(methyl methacrylate) coaxial fibers and conversion to polypyrrole tubes and carbon tubes

In an effort to prepare electrically conductive nanofiber and nanotube materials, polypyrrole/poly(methyl methacrylate) coaxial fibers have been prepared using polymer fibers produced from an electrospinning process. Poly(methyl methacrylate) (PMMA) fibers with an average diameter of 230 nm were initially fabricated by electrospinning as core materials. The PMMA fibers were subsequently coated as templates with a thin layer of polypyrrole (PPy) by in-situ deposition of the conducting polymer from aqueous solution. Hollow PPy tubes were produced by dissolution of the PMMA core from PPy/PMMA coaxial fibers. High-temperature (1000 degrees C) treatment under inert atmosphere converted PPy/PMMA coaxial fibers into carbon tubes by complete decomposition of PMMA fiber core and carbonization of the PPy wall. Scanning electron microscopy (SEM), transmission electron microscopy (TEM), and FT-IR spectroscopy confirmed the formation of the PPy/PMMA coaxial fibers, PPy tubes, and carbon tubes.     

Deposition of oriented zeolite A films: in situ and secondary growth

Zeolite A suspensions with a monomodal, narrow particle size distribution have been prepared. The suspended particles in a TMAOH water solution at pH 9 are negatively charged with a zeta potential of −43 mV. Modification of the external surface of the zeolite particles by a silylation reaction produces particles that, when they are suspended in water, are positively charged and have a zeta potential of +40 mV.The suspensions of the negatively or positively charged particles can be used for the preparation of adsorbed layers of particles on oppositely charged substrates by electrostatic attraction. This deposition process leads to a high coverage of the substrate with well-adhered particles. The cubic morphology of the zeolite particles results in preferential orientation after deposition. The particles are oriented with their {h 0 0} planes (cube faces) parallel and perpendicular to the substrate (out-of-plane orientation). The particles are randomly oriented with respect to the direction perpendicular to the substrate (in-plane orientation). Although, under optimized conditions, the coverage is high and only one adsorption cycle is necessary, the particles are not closely packed.Alternately, the zeolite particle suspensions can be used to deposit close-packed arrays of particles by convective particle transport during dip coating on substrates bearing the same charge as the zeolite particles. Using monodispersed zeolite A suspensions and slow speed dip coating close-packed hexagonal colloidal crystals were prepared. The type of colloidal crystal deposits formed range from continuous sublayers, monolayers, or multilayers to isolated discoidal clusters consisting of few zeolite particles. Factors affecting the deposited layer(s) structure are particle concentration of the suspension and withdrawal speed. In addition to close packing, the layers prepared by dip coating exhibit preferred orientation with the particle faces lying parallel and perpendicular to the substrate surface. Moreover, this second route of precursor film formation by colloidal crystallization leads to domains of well-aligned zeolite particles in three dimensions, i.e. with their faces parallel to each other. The oriented domains span the length of several particles; however, low angle boundaries and other defects during colloidal crystallization prevent the formation of macroscopically three-dimensionally ordered zeolite particles.The precursor layers were subjected to secondary growth in order to prepare continuous intergrown films. Secondary growth proceeds initially by local epitaxy on the deposited particles. Later in the process, deposition proceeds by incorporation of particles from solution along with re-nucleation on the growing film. The intergrown films have predominately [h 0 0] out-of-plane orientation; however, after extended secondary growth treatment a population of [h h h] grains appears on the surface of the regrown films.     

Understanding interactions in zeolite colloidal suspensions: A review

Over the last five years significant progress has been made in understanding interactions in zeolite colloidal suspensions by elucidating the molecular interactions between zeolite crystal surface and species such as water, cations, and organic templates. This is the outcome of multidisciplinary work involving the generation of experimental data concerning the magnitude of ζ-potential, the theoretical and experimental identification of the zeolite crystal surface structure, combined with theoretical models spanning different length scales.