石墨纳米纤维用作质子交换膜燃料电池催化剂载体

利用质子交换膜燃料电池用过的废旧碳纸,采用球磨法制备了石墨纳米纤维(GNF,BET比表面积为229·3m2/g),并以GNF作为载体制备了Pt/GNF催化剂(电化学比表面积为98m2/g).与传统的以VulcanXC-72碳黑为载体的Pt/XC-72催化剂相比,其电化学比表面积及Pt粒径大小相近.采用恒电位氧化法考察了GNF,XC-72,Pt/GNF和Pt/XC-72的电化学稳定性.结果表明,在相同条件下,XC-72的峰电流增加了60%,而GNF增加了2%;Pt/XC-72的腐蚀电流比Pt/GNF的大40%;恒电位氧化60h后,Pt/XC-72约有84·7%的电化学比表面积损失,Pt/GNF仅损失37·2%.这表明GNF的抗腐蚀性优于XC-72,有希望成为质子交换膜燃料电池抗腐蚀的催化剂载体.     

新型L-羟脯氨酸聚合物键合手性固定相的制备及对手性化合物的拆分

以单分散亲水性交联聚甲基丙烯酸环氧丙酯-甲基丙烯酸乙二醇双酯(PGMA/EDMA)树脂为载体,制备新型L-羟脯氨酸聚合物键合高效手性配体交换固定相。该固定相在配体交换分离模式下,以0.2mol/LNaAc和0.1mmol/LCu(Ac)2水溶液(pH5.2)为流动相,柱温为30℃～50℃,对衍生和非衍生的D,L-氨基酸和α-羟基酸等9种手性化合物进行了高效液相色谱拆分。详细考察了流动相pH值、温度、流速和进样量对手性分离的影响,选择了合适的色谱分离条件。结果表明,所拆分的9种手性化合物,有5种手性化合物能得到基线分离,最好的分离因子α=2.32。     

Dynamic interaction between oppositely charged vesicles: aggregation, lipid mixing, and disaggregation

We investigated dynamic interactions between oppositely charged small unilamellar vesicles using positively charged vesicles containing 1,2-dioleoyl-3-trimethylammonium-propane or 3beta-[N-(N('),N(')-dimethylaminoethane)-carbamoyl] cholesterol and negatively charged vesicles containing L-alpha-phosphatidyl-DL-glycerol. Aggregation, lipid bilayer mixing, contents mixing and contents leakage were systematically examined using optical density measurements, fluorescence resonance energy transfer assays, fluorescence quenching assays, light-scattering analyses, and freeze-fracture transmission electron microscopy. The oppositely charged vesicles aggregated immediately. Lipid mixing was observed, but there was no mixing of the contents. The vesicle aggregates disaggregated spontaneously after several minutes. The surface potential of the disaggregated vesicles was neutralized. From these results, we infer that the lipids in the external monolayers were exchanged between the oppositely charged vesicles while the internal monolayers remained intact. The two types of cationic lipids used exhibited different speeds of disaggregation.     

废铬革屑的综合回收利用

碱法水解铬鞣废革屑得到的胶原蛋白灰分含量较高,达不到产品质量标准。针对此问题,利用较为廉价的氧化钙作碱性试剂处理废铬革屑,确定了最优实验方案:碱用量为6%,反应温度为85℃,反应时间为6h。在此基础之上,进一步研究了降低胶原灰分含量的方法:对革屑进行预处理,将胶原液静置过夜过滤除杂,并以不同用量的离子交换树脂处理,当其用量为革屑质量的20%时可使灰分含量降低到国家标准。从水解残余物铬饼中制得了商品氧化铬和硫酸铬,提高了废革屑的利用价值,减少了环境污染。     

基于分形B-S定价模型的认购权证价格行为实证分析

针对证券收益率呈现"尖峰厚尾"的分布特征,在分析传统B-S权证定价模型的不足基础上,本文提出了基于分形理论的B-S权证定价模型,并利用分形B-S权证定价模型和传统B-S模型分析认购权证价格变化的行为。实证结果发现,两种模型的理论价格均低估了市场价格,且低估的程度具有显著统计性,其中以分形B-S模型评价结果最接近市场价格,评价绩效好。探讨影响分形B-S权证模型理论价格与市场价格差异的主要因素,结果发现距到期日时间的长短、价内外程度以及流动性在解释价差程度上具有统计的显著性。     

Block copolymer micelles with dye loaded on their shells or cores

We prepared reversible micelles with dye loaded on the shells or cores by ion exchange. A poly(4-styrylmethyl triphenylphosphonium chloride)-block-polystyrene diblock copolymer prepared from poly(4-vinylbenzylchloride)-block-polystyrene and triphenylphosphine was reacted with methyl orange in a mixed solvent of benzene and acetonitrile to produce poly[4-styrylmethyl triphenylphosphonium 4-(4-dimethylamino)phenylazobenzenesulfonate]-block-polystyrene. The loading of the methyl orange on the micellar shells or cores was dependent on the composition of the mixed solvents. Dynamic light scattering demonstrated that the loading of the dye on the cores significantly expanded the micelles when compared to that on the shells. The loading of the dye on the cores shifted the UV wavelength of the methyl orange, whereas that on the shells produced no changes in the UV wavelength. Transmission electron microscopy confirmed the formation of the spherical micelles.     

Application of polysulfone (PSf)– and polyether ether ketone (PEEK)–tungstophosphoric acid (TPA) composite membranes for water electrolysis

The ion exchange membrane using polysulfone (PSf) and polyether ether ketone (PEEK) as a basic material was prepared to apply in the polymer electrolyte membrane electrolysis (PEME). The sulfonated block copolymer of PSf and poly(phenylene sulfide sulfone) (SPSf-co-PPSS) and the sulfonated PEEK (SPEEK) were blended with tungstophosphoric acid (TPA) to avoid water swelling at elevated temperatures led to decrease in mechanical strength. These prepared ion exchange membranes showed some interesting characteristics including physicochemical stabilities, mechanical and membrane properties.The prepared ion exchange membrane was utilized to prepare the membrane electrode assembly (MEA). MEA consisted of Pt/PEM/Pt was prepared by equilibrium and non-equilibrium impregnation–reduction (I–R) methods. The prepared MEA by non-equilibrium I–R method was used in the PEME unit cell. The cell voltages of the MEA using SPSf-co-PPSS/TPA and SPEEK/TPA membranes were 1.83 V and 1.90 V at 1 A/cm² and 80 °C, with platinum loadings of 1.12 and 1.01 mg/cm², respectively.     

Composite Nafion membrane embedded with hybrid nanofillers for promoting direct methanol fuel cell performance

A special type of hybrid nano-particles was incorporated into the Nafion^® matrix to form a composite membrane. These nano-particles possessed a core–shell structure consisting of silica core (<10 nm) and a densely grafted oligomeric ionmer layer, which was synthesized via atom transfer radical polymerization (ATRP) on the particles’ surface. Besides considerable improvement in the proton conductivity of the membrane, the presence of these hybrid nano-particles in the Nafion^® matrix also repressed its methanol permeability by almost four times. The composite membrane also demonstrated superior performance when tested in a single cell membrane-electrolyte assembly (MEA) under direct methanol fuel cell (DMFC) operating condition. It was found that the composite membrane enabled a power density output that was 1.5 times greater than that of pristine Nafion^®.     

Preparation and characterization of Type II anion exchange membranes from poly(2,6-dimethyl-1,4-phenylene oxide) (PPO)

To separate hydrophilic anions from hydrophobic ones, Type II PPO-based anion exchange membranes were developed. Different from Type I (with both trimethylbenzylammonium and triethylbenzylammonium groups), Type II has an excellent hydrophobicity modifier as fixed groups: dimethyethanolammonium groups, which were introduced into PPO (poly(2,6-dimethyl-1,4-phenylene oxide)) by following benzyl bromination of PPO and subsequent quaternary amination with a dimethylethanolamine (DMEA) aqueous solution. The membrane's intrinsic properties are dependent on DMEA concentration and amination temperature. The optimum conditions for membrane preparation are as follows: amination temperature 70 °C, time 30–48 h, and DMEA concentration 1:3–1:5 (v/v, DMEA to water). The obtained Type II anion exchange membranes had an IEC of 1.5 mmol/g dry membrane, water content of 30%, and membrane area resistance of 30 Ω cm². The introduced dimethyethanolammonium groups can block hydrated anions from the access to membranes but let hydrophobic anions transport; hence, an effective separation between hydrophilic and hydrophobic anions can be achieved during electro-membrane operation.     

Modeling of the mass transfer and conduction behavior in electro-electrodialysis with oil/water emulsion as the catholyte

In this paper, a mathematic model has been developed to simulate a modified two-phase electro-electrodialysis (MTPEED) process in which an oil/water (O/W) emulsion is used as the catholyte. Previous results have demonstrated that the process is highly efficient in the recovery of organic acids. The fundamental aspects of this model are expressed by the overall mass transport equation and the total voltage equation. The mass transport equation includes several parameters, such as the electro-migration coefficient, the solute diffusion coefficient, the electro-osmotic coefficient, the concentration-osmotic coefficient as well as the current density and membrane selectivity coefficient. The voltage equation includes the electrode potential, the membrane potential, the solution resistance and the membrane resistance. The extraction equilibrium and the conductivity of the O/W emulsion were experimentally determined and calibrated. The model can predict the lactic acid concentration and the solution volume versus operating time well. In the context of this model, we discuss the operating mode's effect on the MTPEED process and the quantitative effect of some design variables.