壳聚糖交联膜结构及性能的研究

壳聚糖是一种天然生物高分子聚合物，是甲壳素脱乙酰化产物，具有很好的成膜特性．用一种金属离子把壳聚糖分子中的螫合基团络合保护后，用戊二醛交联，并在酸性条件下将该金属离子洗脱，得到了螯合基团依然保留的壳聚糖交联膜．对壳聚糖交联膜的结构及性能进行了研究．结果表明：金属离子有效地保护了壳聚糖分子上的络合基因，该膜的性能较好，对阴离子的选择透过性比较好，并将其应用于元素的分离．     

羧甲基壳聚糖/明胶共混膜的结构表征与吸湿保湿性

壳聚糖通过羧甲基化得到水溶性N，O-羧甲基壳聚糖，并将其配制成4Wt％水溶液，与4Wt％明胶水溶液共混，成功制得了羧甲基壳聚糖／明胶共混膜。采用红外光谱、x射线衍射、扫描电镜对共混膜进行结构表征，结果表明，共混膜中羧甲基壳聚糖和明胶分子间存在着较强的相互作用及良好的相容性。通过共混膜的力学性能测试，发现当羧甲基壳聚糖含量为20％时，共混膜的抗张强度达到最大值(75MPa)，分别比单独的羧甲基壳聚糖(45MPa)和明胶(43MPa)提高了66．7％和74％。经过吸湿和保湿性能测试，发现当羧甲基壳聚糖含量为80％时，吸湿率和保湿率分别为33．4％和69．2％，比单独的明胶膜分别提高了1．8倍和2．1倍。     

甲壳素和壳聚糖的接枝共聚改性

天然高分子甲壳素、壳聚糖由于分子链上大量存在的反应性官能团 ,易于通过自由基引发与乙烯基单体接枝共聚 ,也可与其它高分子链偶合制得接枝共聚物。通过接枝共聚改性 ,可以赋予甲壳素和壳聚糖以某些新的性能 ,扩大了其应用范围。本文对甲壳素、壳聚糖的接枝共聚改性反应进展、机理以及产物的性能等进行了介绍     

甲壳素和壳聚糖在离子液体中的溶解、材料化以及衍生化

甲壳素和壳聚糖是可再生的大分子生物质资源.由于分子内和分子间的强烈氢键作用,甲壳素和壳聚糖不能溶解在水或常规有机溶剂中,这极大地限制了其在诸多领域中的应用.离子液体作为一种新型绿色溶剂,对甲壳素和壳聚糖具有优良的溶解作用.本文综述了离子液体对甲壳素和壳聚糖的溶解性能和溶解机理,概述了均相溶液体系中纤维、膜、凝胶等材料的制备以及酰化、接枝共聚、交联、降解、希夫碱化等多种衍生化反应,总结了离子液体在甲壳素和壳聚糖化学研究中面临的挑战并对其进行了展望.     

纤维素/甲壳素共混膜的结构表征与抗凝血性能

以 6wt %NaOH 4wt%尿素为纤维素的新溶剂 ,采用溶液共混法制备出纤维素 甲壳素共混膜 ,为甲壳素在碱性溶液中制膜提供了新的方法 .红外光谱、X 射线衍射、扫描电镜和力学性能、抗凝血性能测试结果表明 ,共混膜中甲壳素含量低于 4 0wt%时 ,纤维素与甲壳素分子间具有良好的相容性 ;在纤维素中引入适量甲壳素可提高共混膜的抗张强度 ,共混膜的干、湿态抗张强度在甲壳素含量 10wt%时最大 ,其值分别为 89 1MPa和 4 3 7MPa ,比纯态纤维素膜的干、湿态抗张强度分别提高了 6 7%和 11 5 % ;甲壳素的引入可明显降低血小板在共混膜表面的粘附、凝聚与变性 ,增大共混膜的抗凝血参数 ,甲壳素含量达到 5 0wt%时 ,该共混膜具有良好的抗凝血性能     

壳聚糖接枝丙烯酸制备高强吸水材料

甲壳素（Chitin）年产量约为10-100亿吨,是仅次于纤维素（约为100亿吨）的第二大天然资源。开发利用这一自然资源宝库,具有十分重要的意义。甲壳素的脱乙酰化产物称为壳聚糖（Chitosan）。本工作对壳聚糖进行丙烯酸接枝改性,制得对蒸馏水吸水率大于800倍、吸自来水大于500倍,吸0．9％NaCl溶液吸液率130倍的吸液保液材料,该材料具有生物降解性,无环境污染,且制备工艺简单,成本低。     

壳聚糖衍生物吸附剂在蛋白质分离纯化中的应用

综述了近年来甲壳素及壳聚糖衍生物吸附剂、色谱填料、分离膜及医用免疫吸附剂在蛋白质分离纯化中的应用．引用文献65篇．     

壳聚糖固体聚合物电池用膜

壳聚糖是甲壳素脱乙酰基的产物，具有良好的成膜性、生物相容性、环保以及价格低廉等特点。作为一种碱性高分子膜材料，近年来已成为聚电解质研究领域中的研究热点。本文综述了壳聚糖固体聚合物电池用膜的研究现状，其改性工艺主要包括共混、化学改性、质子酸掺杂、无机盐掺杂等方法，比较了各种工艺处理后壳聚糖固体聚合物电解质膜的性能差异，并就壳聚糖固体聚合物电解质膜中离子传导机理中有待解决的问题进行探讨，并提出了进一步改进壳聚糖固体聚合物电解质膜性能的研究思路。     

热塑性甲壳素衍生物N,O-苄基壳聚糖的合成及表征

天然高分子的热塑化一直引起人们的极大关注．由于存在大量的分子内和分子间氢键,一般天然高分子都不能加热塑化,从而限制了其应用．纤维素和淀粉的热塑化改性已有了许多研究．典型的热塑性纤维素衍生物有乙基纤维素、醋酸纤维素和经丙基纤维素等[1,2],有些纤维素衍生物还具有热致液晶性．淀粉的某些衍生物也已有热塑性[3]．在分子结构上,甲壳素／壳聚糖比纤维素或淀粉多了乙酰氨基和氨基,更易形成氢键,分子间作用力更强．迄今,国内外已报道了大量甲壳素／壳聚糖衍生物,但均无热塑性．我们曾合成具有热塑性的氰乙基经丙基壳聚糖,但熔点与分解温度之间只有27℃E4J．热塑性甲壳素的研究不仅为甲壳素的加工利用开辟了新途径,而且也将为热致性甲壳素液晶的研究奠定基础,从而进一步丰富和深化目前以纤维素衍生物为主的热致胆舀液晶研究[5,6]．为此,本文研究了一种新的热塑性甲壳素衍生物,并从结构上讨论了其具有热塑性的原因．     

甲壳素纯度的高效液相色谱法测定

由于生物材料中甲壳素或壳聚糖是大分子，不溶于水，以及与蛋白质等结合在一起而难以定量测定，工业生产中尚无甲壳素或壳聚糖纯度的标准测定方法；采用甲壳素水解生成氨基葡萄糖，再用氯甲酸芴甲酯(FMOC—C1)进行衍生，利用液相色谱技术对衍生产物进行分析；结果表明，HPLC法是生物材料中甲壳素的一种灵敏的、特有的定性定量分析方法，为生物材料及工业化生产中甲壳素纯度的测定提供了一个方便的手段。     

Phase behavior of polystyrene–polyisoprene–toluene systems in the temperature range 15–45°c

The phase behavior of narrow molecular weight distribution samples of polystyrene and polyisoprene in the presence of toluene was investigated by means of gel permeation chromatography. Equilibrium phase diagrams, tie lines, and critical points for a number of partially miscible polystyrene-polyisoprene-toluene systems were generated at 15 and 30°C and 1 atm pressure. The data were combined with previously reported results at 45°C. Using the experimentally determined phase compositions along with literature values of the polymer–solvent interaction parameters, the polymer–polymer interaction parameters were evaluated using the Flory–Huggins theory. The influence of temperature, polymer molecular weight, and polymer–solvant interaction parameters on the size, shape, and location of the equilibrium phase curve, the location of the critical point, and the polymer–polymer interaction parameter was studied.     

Thermodynamic interactions of three SBS (styrene-butadiene-styrene) triblock copolymers with different solvents, by means of intrinsic viscosity measurements

The Hansen Solubility Parameter (HSP) and the Flory Huggins polymer-solvent interaction parameter of three SBS (styrene-butadiene-styrene triblock copolymer) rubbers have been determined by using intrinsic viscosity (IV) measurements. The obtained values indicated that, although all the tested compounds could be adequate as solvents, the aromatic ones are the most compatible for this kind of polymers. From these previous data, the activity coefficients of the solvent were also obtained and fitted to NRTL model. The calculated interaction parameters have a great importance in order to model, for example, the separation steps in the process of obtaining the rubber.     

Thermodynamic study on phase equilibrium of epoxy resin/thermoplastic blends

The experimental phase diagrams (cloud point curves) of three series of epoxy/thermoplastic blends, namely, epoxy/polystyrene (PS), epoxy/poly(ether sulfone) (PES), and epoxy/poly(ether imide) (PEI) as a function of molar mass and composition have been analysed from a thermodynamic point of view. A model based on the Flory–Huggins lattice theory considering the concentration dependence of the interaction parameter as predicted by Koningsveld was employed to determine the equilibrium compositions, and concentration and temperature dependent interaction parameters. Binodal, spinodal, and critical point data have been computed and show good agreement with experimental data.     

Investigation of thermodynamic properties of hyperbranched poly(ester amide) by inverse gas chromatography

Thermodynamic properties of the hyperbranched poly (ester amide) (Hybrane® 1200) were investigated by inverse gas chromatography (IGC) using 19 different solvents as the probes at infinite dilution. Retention data of probes were used for an extensive characterization of the polymer, which includes the determination of the Flory‐Huggins interaction parameter, the weight fraction activity coefficient, the total, partial, and additive solubility parameters. The analysis of the results indicated that the additive value of the solubility parameter is lower than the value obtained from a standard procedure. Furthermore, the solubility parameter decreases with increase of temperature. © 2008 Wiley Periodicals, Inc. J Polym Sci Part B: Polym Phys 46: 2166–2172, 2008     

Evaluation of solubility parameters during polymerisation of amine‐cured epoxy resins

A new procedure for the calculation of solubility parameter evolution during polymerisation has been developed for amine‐cured epoxy systems, which allows quantitative thermodynamic modelling of chemically induced phase separation (CIPS). Solubility parameters calculation, chemical analysis based on near infrared spectroscopy and curing kinetics results obtained by differential scanning calorimetry will allow to model the evolution of the Flory–Huggins interaction parameter in amine‐cured epoxy blends. The resin system investigated was based on a diglycidyl ether bisphenol A (DGEBA) epoxy resin cured with isophorone diamine (IPD) blended with various reactive epoxydised dendritic hyperbranched polymer modifiers (HBP), yielding a CIPS‐controlled morphology. The analysis showed the evolution of the different contributions to the solubility parameters to follow the polymerisation kinetics. The dispersive contribution had the highest value at all stages of polymerisation, but the hydrogen and polar contributions showed the largest variation. By evaluating the dynamic evolution of the solubility parameter components, the Flory–Huggins interaction parameter in the epoxy resin‐hyperbranched polymer blends has been modelled as a function of time. This procedure, combined with thermodynamic modelling, will enable to predict phase diagrams in CIPS thermosetting blends quantitatively. © 2000 John Wiley & Sons, Inc. J Polym Sci B: Polym Phys 38: 1883–1892, 2000     

CO2 sorption and transport in miscible poly(phenylene oxide)/polystyrene blends

The sorption and permeation of carbon dioxide gas in miscible blends of poly(phenylene oxide) and polystyrene was measured as a function of pressure at 35°C over the entire range of blend compositions. The results are well described quantitatively by the dual sorption and dual mobility models developed for glassy polymers. The Henry's law sorption parameter was analyzed by the Flory—Huggins theory of ternary mixtures to obtain an interaction parameter which quantifies the exothermic heat of mixing for this blend system. The Langmuir capacity term was successfully related to the unrelaxed volume of the glassy blends. Transport properties of the blends were found to lie well below predictions based on simple additivity which is consistent with the strong interaction between the two polymers.     

Solubility and Flory Huggins parameters of SBES, poly(styrene-b-butene/ethylene-b-styrene) triblock copolymer, determined by intrinsic viscosity

Solubility parameter and Flory Huggins interaction parameter of a triblock SBES have been obtained from intrinsic viscosity measurements. The solubility of the block copolymer in all solvents (methyl-cyclohexane, cyclohexane, cyclopentane, toluene and benzene) was found good except in the case of n-hexane. The results obtained are similar to other found in literature for SBR and SBS rubbers, and indicate that cyclohexane and cyclopentane and methylcyclohexane are the most compatible solvents for this kind of polymer.     

Phase segregation kinetics in segmented linear polyurethanes: Relations between equilibrium time and chain mobility and between equilibrium degree of segregation and interaction parameter

The kinetics of phase segregation of segmented linear polyurethanes, from a homogeneous single-phase system into a two-phase one, have been studied by measuring the heat capacity change at the glass transition of the soft phase. The extent of phase segregation at equilibrium is a linear function of the Flory–Huggins interaction parameter χ. For χ lower than about 3, no segregation can take place. This value, higher than expected theoretically, indicates forced compatibility due to chemical links between soft and hard blocks of the segmented polyurethanes. The time required to attain equilibrium is not a function of thermodynamic parameters but of the chain mobility. A linear relation is proposed between the logarithm of equilibrium time and the viscosity of the pure soft phase.     

Modeling the thermodynamic and transport properties of decahydronaphthalene/propane mixtures: Phase equilibria, density, and viscosity

The density and viscosity of propane mixed with 66/34 trans/cis-decahydronaphthalene were measured over a wide range of temperatures (323-423 K), pressures (2.5-208 bar), and compositions (0-65 mol% propane). For conditions giving two phases, the composition of the dense phase was measured in addition to the density and viscosity. The modified Sanchez-Lacombe Equation of State (MSLEOS) was used with a single linearly temperature-dependent pseudo-binary interaction parameter to correlate the phase compositions and densities. The compositions and densities of the mixtures were captured well with absolute average deviations between the model and the data of 5.3% and 2.3%, respectively. The mixture viscosities were computed from a free volume model (FVM) by using a single constant binary interaction parameter. Density predictions from the MSLEOS were used as input mixture density values required for the FVM. The FVM was found to correlate well with the mixture viscosity data with an absolute average deviation between the model and the data of 5.7%.     

Prediction of phase diagrams for new pH-thermo sensitive recycling aqueous two-phase systems

The recyclable aqueous two-phase systems formed by thermo-sensitive polymer (P_NB) and pH-sensitive polymer (P_ADB) have been prepared by our laboratory. In this study, the Flory–Huggins model derived from the lattice theories and the COVE model based on the McMillan–Mayer solution theory were used for correlations and predictions of phase diagrams. The interaction parameters between the solvent and the polymers of the Flory–Huggins model were calculated from solubility parameters. The interaction parameters between the polymers and the COVE coefficients were determined by fitting experimental data. Simulation of Flory–Huggins model and COVE model indicates that the deviation between prediction values and experimental data is less than 0.50%. The COVE model was more effective than the Flory–Huggins model to this system.