蜂窝状堇青石载体Al2O3涂层的原位合成

 采用改进的原位合成法（原位－浸涂法）在蜂窝状堇青石载体表面制备了多孔氧化铝涂层．着重研究了制备条件对涂层负载、晶相及其孔结构性质的影响，并与其他方法制备的涂层进行了比较．结果表明，采用多次原位合成法制备能提高氧化铝涂层的牢固度，但每次负载量偏低；原位－浸涂法适宜的制备参数为：水解温度83℃，水／异丙醇铝摩尔比60，pH值3．5～4．0，焙烧温度500℃．原位－浸涂法有利于制备Al2O3涂层，具有较好的牢固度，而且涂层的孔径分布窄，具有较大的比表面积、比孔体积和平均孔径．     

聚乙烯吡咯烷酮包裹核壳型Fe_3O_4/Au纳米粒子的制备

采用改进的Polyol合成法,以聚乙烯吡咯烷酮（PVP）为表面活性剂制备PVP包裹的单分散的Fe3O4/Au纳米粒子.透射电镜（TEM）和X射线衍射（XRD）分析证实了Fe3O4/Au的核壳型纳米结构,并确定了纳米粒子的尺寸大小和分布.UV-Vis测定显示了所制备的纳米粒子具有光学活性,而振动样品磁强计（VSM）测量显示纳米粒子具有优异的磁化率.     

TiO_2/PVDF复合中空纤维膜的制备和表征

采用相转化法制备了二氧化钛 (TiO2 ) 聚偏氟乙烯 (PVDF)复合中空纤维膜 .应用牛血清白蛋白截留实验、扫描电子显微镜、热重分析、X射线衍射分别对复合膜的分离性能、微观结构、热稳定性和晶相组成进行了分析 .结果表明复合膜的性能与纯PVDF膜的相比有显著的改善 ,其中对牛血清白蛋白的截留率从 3 2 7%提高到 86 6 7% ,单根纤维的断裂应力从 3 35MPa提高到 4 70MPa ,提高了 4 0 3% .氮气吸附实验测定的孔径分布进一步表明复合膜的孔径分布变窄 ,孔径变小 .     

Pd-Ag/PTFE复合膜的制备及表征

本文以不同孔径的聚四氟乙烯（PTFE）为基膜，采用化学镀法分别将Ag、Pd沉积到PIFE膜孔及膜面上，制得了镀层均匀、结合力较好的Pd-Ag／PTEE复合膜，并考察了PTFE基膜孔径对镀层结合力的影响，以及化学镀工艺对金属钯沉积速率、复合膜孔结构和截面电阻率的影响。结果表明，适当的基膜孔结构有利于提高镀层结合力；PTFE膜经化学镀修饰后，孔径减小，孔径分布变窄，孔隙率降低，膜截面电阻率降低10^6数量级，且孔径减小顺序与截面电阻率减小顺序一致。     

甲烷单加氧酶化学模拟的初步研究

制备了两种新的甲烷单加氧酶模拟酶：（1）固载于分子筛上的单氧桥联双核铁配合物Fe2(O)(H2O)2-(phen)4(ClO4)；（2）在表面修饰的介孔分子筛上原位合成的氧桥、羧基桥联双核铁配合物Fe2(O)（μ－CH3COO）2－(H2O)2-(phen)2Cl2。利用紫外漫反射、红外漫反射、拉曼光谱、N2吸脱附分析及元素分析等手段，对模拟酶进行结构分析。结果表明，Fe2(O)(H2O)2-(phen)4(ClO）4主要是以配合物中的桥氧与分子筛表面硅羧基成氢键固载；原位合成的Fe2(O)（μ－CH3COO）2(H2O)2-(phen)2Cl2中，一个羟基来自表面修饰的分子筛，催化反应结果表明在，温和条件下、以叔丁基过氧化氢为氧化剂，这两种模拟酶均催化环已烷氧化。     

复合氧化物CeO2-Co3O4催化氧化CO的性能

以共沉淀法制备CeO2-Co3O4复合氧化物，研究复合氧化物CeO2-Co3O4低温催化氧化CO的性能。通过采用热重分析（TG）、比表面积测试（BET）、X射线衍射分析（XRD）、程序升温还原（TPR）以及原位红外漫反射（FT-IR）等表征手段，详细探讨了铈含量对于复合氧化物CeO2-Co3O4低温催化氧化CO性能的影响。结果表明：复合氧化物CeO2-Co3O4催化氧化CO的性能明显优于单一氧化物CeO2和CO3O4，     

磁场诱导沉淀聚合制备一维Fe3O4/P（MAA-DVB）纳米链

采用溶剂热法制备了单分散Fe3O4纳米粒子,以甲基丙烯酸（MAA）和二乙烯基苯（DVB）为聚合单体,在沉淀聚合过程中通过磁场诱导自组装制备了一维高磁响应性永久连接的Fe3O4/P（MAA-DVB）纳米链.采用扫描电镜（SEM）,透射电镜（TEM）,X射线衍射仪（XRD）,热重分析（TGA）及振动样品磁强计（VSM）等对其形貌、磁含量和磁响应性等进行了分析表征.结果表明,该法制备的一维Fe3O4/P（MAA-DVB）纳米链的磁含量为91%时,其比饱和磁化强度为72emu/g.在外磁场存在条件下,一维Fe3O4/P（MAA-DVB）纳米链将按外界磁场的方向取向.此外,每个豆荚内的Fe3O4纳米粒子规则的排列在一条线上,并通过P（MAA-DVB）聚合物使其均匀分布.     

多壁碳纳米管负载Fe3O4磁性纳米粒子表面吸附增强过氧化酶的催化活性

采用共沉淀法制备了Fe3O4磁性纳米粒子,将其负载于氨基吡啶修饰多壁碳纳米管(MWCNT-AP)上,得到具有良好的分散性和超顺磁性的Fe3O4/MWCNT-AP复合物.通过傅里叶变换红外(FT-IR)光谱、X射线衍射(XRD)和磁滞回线测量等方法对Fe3O4/MWCNT-AP复合物进行了表征.扫描电镜(TEM)结果表明:Fe3O4磁性纳米粒子多集中于碳纳米管MWCNT-AP的端部,形成的复合物在极性溶剂中具有良好的分散性和超顺磁性;辣根过氧化酶(HRP)可通过物理作用吸附于Fe3O4/MWCNT-AP复合物表面.酸性条件下(pH 4.0),Fe3O4/MWCNT-AP复合物使HRP的最大反应速率(Vmax)提高了3倍.     

导电聚苯胺-四氧化三钴复合材料的合成及性能表征

采用原位聚合法制备导电聚苯胺-四氧化三钴（PANI-Co3O4）复合材料。研究了Co3O4含量对复合材料电导率的影响。通过傅里叶红外光谱（FT-IR）、X射线衍射（XRD）、热失重法（TGA）和微分热失重法（DTG）等测试手段对复合材料的结构和性能进行了表征,并考察了复合材料在硫酸铜电解液体系中的电化学性能。结果表明：...     

聚4-乙烯基吡啶原位修饰PVDF膜及其负载磷钨杂多酸催化剂的研究

以聚偏氟乙烯(polyvinylidene fluoride,PVDF)微滤膜为基膜,4-乙烯基吡啶(4-vinylpyridine,4VP)为功能单体,采用表面引发电子活化再生原子转移自由基聚合(SI-AGET ATRP)法在基膜表面原位改性,并通过接枝聚合物侧链上的吡啶基团与Keggin型磷钨杂多酸(H3PW12O40·n H2O,HPW)之间的静电作用,制备了新型混合催化膜.实验结果表明,接枝聚合过程表现出"活性"/可控表面引发接枝聚合性质,基膜表面接枝聚合物量随聚合反应时间呈现线性增加,当反应时间为16 h,聚合物接枝量达到2.25 mg/cm2,聚合物接枝量的增多致使其相互堆积并坍塌,造成膜表面出现块状聚集体.然后,利用溴代十六烷对接枝聚合物进行季铵化改性,制得表面含有吡啶鎓盐的阳离子复合膜,通过接枝聚合物侧基中的吡啶和吡啶鎓盐基团与磷钨杂多酸之间的静电作用促使其在改性膜表面上有效负载.负载后的磷钨杂多酸均匀的分布在膜表面及孔道中,并保持其化学结构.负载催化剂前后膜的接触角从80.4°减小到57.8°,体现了亲水性催化剂的负载对膜表面润湿性的显著影响.     

膜相渗透原位化学聚合法制备PAn/CA复合透膜

采用膜相渗透原位化学聚合法,使苯胺(An)原位化学聚合于醋酸纤维素(CA)基体膜的微孔壁中,得到均匀分布的PAn/CA复合导电透膜.通过研究聚合反应条件对复合透膜的导电性能和CO₂/O₂表观分离性能的影响,获得了制备性能较优的PAn/CA复合导电透膜的适宜条件.结果表明,采用膜相渗透化学原位聚合法制备的PAn/CA复合导电透膜,平均孔径明显变小,孔径分布变窄,具有优于CA基体膜的微孔结构形态.     

Modified liquid displacement method for determination of pore size distribution in porous membranes

A new method called constant pressure liquid displacement method (CPLM) was developed and tested to measure the pore size distribution of porous membranes. The permeability, defined as a ratio of the flow rate to the pressure applied, used to be assumed constant either for a conventional liquid displacement method or for a bubble point method, leading to the erroneous interpretation of the pore size distribution. However, it was possible to eliminate such an assumption by measuring the flow rates experimentally at a standard low pressure through the pores penetrated with a permeating liquid according to the proposed method. The pore size distribution for a hydrophobic PVDF membrane was successfully measured by the CPLM and compared with those measured by two different methods such as the conventional liquid displacement method and the mercury intrusion method.     

四乙基氢氧化铵改性聚偏氟乙烯接枝聚丙烯酸油水分离膜的制备

使用四乙基氢氧化铵(TEAH)液相本体改性聚偏氟乙烯(PVDF), 以过氧化苯甲酰(BPO)为引发剂, 将丙烯酸(AA)接枝到改性PVDF骨架上, 合成了聚偏氟乙烯接枝聚丙烯酸(PVDF-g-PAA)共聚物, 通过浸没沉淀法制备了PVDF-g-PAA亲水性油水分离膜. 通过傅里叶变换红外光谱(FTIR)、 扫描电子显微镜(SEM)和过滤试验分析了膜的结构和分离性能. 研究了不同接枝条件对PVDF-g-PAA膜接枝率的影响. 同时, 通过膜接枝率与膜表面接触角的关系确定最佳接枝条件. 结果表明, TEAH使PVDF脱去HF产生碳碳双键且PAA接枝到改性的PVDF骨架上, 膜内外孔隙分布均匀; PVDF-g-PAA膜的接触角随着接枝率的提高而降低. 接枝单体AA含量为45%, 接枝温度为85 ℃, 接枝4 h制备的PVDF-g-PAA膜的接枝率为20.1%, 孔隙度为65.3%, 平均孔径为78.0 nm, 接触角为57.5°, 且在60 s内接触角降至14.3°; 纯水通量提高到571.33 L/(m²·h), 截留率和水通量恢复率分别达到94.3%和88.7%, 且通量衰减率仅为9.8%. 与纯PVDF膜相比, PVDF-g-PAA膜的分离性能显著提高.     

Positron annihilation lifetime spectroscopy study of polyvinylpyrrolidone-added polyvinylidene fluoride membranes: Investigation of free volume and permeation relationships

Polyvinylidene fluoride (PVDF) membranes were prepared via the phase inversion method from casting solutions containing PVDF, dimethylformamide (DMF), and polyvinylpyrrolidone (PVP) as pore former. PVP was used in the casting solution in a range of 0–5 wt % and extracted. The effect on membranes of using PVP in the casting process was analyzed by X-ray diffraction, differential scanning calorimetry, scanning electron microscopy, viscosity, and water permeability techniques. With an increase of PVP from 0 to 5 wt %, the PVDF casting solution viscosities increased from 858 to 1148 cP; the resulting PVDF membrane thickness increased; and the crystallinity of PVDF membranes decreased from 40.0 to 33.3%, which indicates that the addition of PVP inhibits the degree of crystallization in the PVDF membranes. SEM results revealed the shape and size of macropores in the membranes; these macropores changed after PVP addition to the casting solutions. The impact of structural changes on free-volume properties was evaluated using positron annihilation lifetime spectroscopy (PALS) studies. PALS analysis indicated no effect on the average radius (~3.4 Å) of membrane free-volume holes from the addition of PVP to the casting solution. However, the percentage of o-Ps pick-off annihilation intensity, I₃, increased from 1.7 to 5.1% with increased PVP content. Further, increasing the PVP content from 0.5 to 5% resulted in an increased final pure water permeability flux. For instance, the 210 min flux for a 14% PVDF + 0.5% PVP membrane was found to be 3.3 times greater than a control membrane having the same PVDF concentration. © 2020 Wiley Periodicals, Inc. J. Polym. Sci. 2020 , 58, 589–598     

氧化剂对PAn/PTFE复合导电膜结构和性能影响的研究

分别以过硫酸铵和正钒酸钠作氧化剂,应用膜相渗透原位化学聚合法制备聚苯胺(PAn)/聚四氟乙烯(PTFE)复合导电膜,比较考察了两种氧化剂条件下膜孔中苯胺的聚合生长行为.扫描电镜、孔径分布及电化学测试结果表明:选用两种氧化剂分别制备的复合膜,均具有较小的膜孔径;与过硫酸铵相比,使用正钒酸钠作氧化剂时,复合膜的结构更为致密,且在保持较高表面电导率(2.62S·cm-1)的同时,断面电导率提高了1～2个数量级,电化学活性增强.     

Novel proton-conductive nanochannel membranes with modified SiO2 nanospheres for direct methanol fuel cells

A novel approach is proposed to prepare a proton-conductive nanochannel membrane based on polyvinylidene difluoride (PVDF) porous membrane with modified SiO₂ nanospheres. The hydrophilic PVDF porous membrane with a 450-nm inner pore size was chosen as the supporting structure. Pristine SiO₂ with a uniform particle size of 95–110 nm was synthesized and functionalized with –NH₂ and –COOH, respectively. Through-plane channels of porous membrane and arranged functional nanoparticles in pores could contribute to constituting efficient proton transfer channels. The characteristics such as morphology, thermal stability, water uptake, dimensional swelling, proton conductivity and methanol permeability as proton exchange membranes, of the SiO₂ nanospheres, and the composite membrane were investigated. The formation of ionic channels in membrane enhanced the water uptakes and proton conduction abilities of the composite membranes. PVDF/Nafion/SiO₂–NH₂ exhibited superior proton conductivities (0.21 S cm^?1) over other samples due to several proton sites and the acid–base pairs formed between –NH₂ and –SO₃H. Furthermore, all the composite membranes exhibited improved methanol resistance compared with Nafion. Therefore, such a design based on porous membrane provided feasibility for high-performance proton exchange membrane in fuel cell applications.     

Thin layer molecularly imprinted microfiltration membranes by photofunctionalization using a coated alpha-cleavage photoinitiator.

A novel approach towards thin-layer molecularly imprinted polymer (MIP) composite membranes was developed based on using benzoin ethyl ether (BEE), a very efficient alpha-scission photoinitiator. The triazine herbicide desmetryn was used as the template, and a mixture of the functional monomer 2-acrylamido-2-methyl-1-propane sulfonic acid (AMPS) and the cross-linker N,N'-methylene-bis-acrylamide (MBAA) in methanol was copolymerised via photoinitiation followed by deposition on the surface of either hydrophobic or hydrophilically precoated polyvinylidene fluoride (PVDF) microfiltration membranes. Blanks were prepared under identical conditions, but without the template. Especially, the degree of functionalization (DF) of the PVDF membranes with poly(AMPS-co-MBAA), the membrane permeabilities and non-specific vs. MIP-specific template binding from aqueous solutions during fast filtration were studied in detail to evaluate the effects of the preparation conditions, in particular the coating of the membrane surface with the photoinitiator prior to UV irradiation and the influence of the precoated hydrophilic layer on PVDF. Significant template specificities of the MIP membranes compared with the blanks were only achieved for the preparations including coating the two types of PVDF membranes with BEE. In contrast, a homogeneous photoinitiation of the copolymerisation in the membrane pore volume yielded functional layers with similar DF but with only non-specific desmetryn binding. All data clearly indicate the significant contribution of MIP stabilization by the support material in layers of optimum thickness to the MIP specificity. Main advantages of the novel approach are the potential to synthesize MIP composite membranes by controlled deposition onto any kind of polymer support, and the very fast MIP preparations due to a very efficient photoinitiator and small MIP layer thickness. Due to the mechanical and chemical stability in combination with high permeabilities, thin-layer MIP composite membranes have a large application potential, e.g., in solid phase extraction.     

PREPARATION OF POLYVINYLIDENE FLUORIDE／POLYVINYL DIMETHYLSILOXANE COMPOSITE HOLLOW FIBER MEMBRANES AND THEIR SEPARATION PROPERTIES

Microporous polyvinylidene fluoride (PVDF) hollow fibre membranes were spun using the dry-wet phase inversion method. By means of dip-coating technique, a uniform coating with thickness of around 5-12μm of polyvinyl dimethylsiloxane (PVDMS) was formed on the surface of porous PVDF hollow fibers. The structural parameters of PVDF substrate membrane were estimated by gas permeation test. Using N2/O2 as the medium, the separation properties of PVDMS-PVDF composite hollow fiber membranes were also evaluated experimentally. The experimental data of both permeability and selectivity are in good agreement with the theoretical results predicted by the presented pore-distribution model, in order to obtain the compact composite membrane free of defects by the dip-coating technique, the thickness of PVDMS skin must be higher than 5μm.     

Methane oxidation over mixed-conducting SrFe(Al)O3-delta-SrAl2O4 composite

The steady-state CH4 conversion by oxygen permeating through mixed-conducting (SrFe)0.7(SrAl2)0.3Oz composite membranes, comprising strontium-deficient SrFe(Al)O3-delta perovskite and monoclinic SrAl2O4-based phases, occurs via different mechanisms in comparison to the dry methane interaction with the lattice oxygen. The catalytic behavior of powdered (SrFe)0.7(SrAl2)0.3Oz, studied by temperature-programmed reduction in dry CH4 at 523-1073 K, is governed by the level of oxygen nonstoichiometry in the crystal lattice of the perovskite component and is qualitatively similar to that of other perovskite-related ferrites, such as Sr0.7La0.3Fe0.8Al0.2O3-delta. While extensive oxygen release from the ferrite lattice at 700-900 K leads to predominant total oxidation of methane, significant selectivity to synthesis gas formation, with H2/CO ratios close to 2, is observed above 1000 K, when a critical value of oxygen deficiency is achieved. The steady-state oxidation over dense membranes at 1123-1223 K results, however, in prevailing total combustion, particularly due to excessive oxygen chemical potential at the membrane surface. In combination with surface-limited oxygen permeability, mass transport limitations in a porous layer at the membrane permeate side prevent reduction and enable stable operation of (SrFe)0.7(SrAl2)0.3Oz membranes under air/methane gradient. Taking into account the catalytic activity of SrFeO3-delta-based phases for the partial oxidation of methane to synthesis gas and the important role of mass transport-related effects, one promising approach for membrane development is the fabrication of thick layer of porous ferrite-based catalyst at the surface of dense (SrFe)0.7(SrAl2)0.3Oz composite.