聚苯乙烯-聚4-乙烯基吡啶两亲嵌段共聚物在CO_2膨胀液体中的组装行为（英文）

嵌段共聚物的自组装行为和其组装形成的胶束聚集体的形貌因在生物医学、药物传输和催化等方面的潜在应用而引起了科学家们的极大兴趣。本工作报道了利用二氧化碳膨胀液体(CXLs)对嵌段共聚物聚苯乙烯-聚4-乙烯基吡啶(PS-b-P4VP)的自组装聚集体(SAA)进行组装结构调控的初步探索。研究发现利用CXLs的抗溶剂效应可以成功调节共聚物PS-b-P4VP的自组装行为。研究结果表明,CXLs的压力及共聚物的组成是影响SAA结构的主要外部因素,CXLs的抗溶剂效应及其对共聚物溶剂化构型的影响是控制SAA形貌转变的主要内在因素。不同组成的共聚物,在CXLs中其SAA的结构形貌均表现出了对压力的显著响应特性。共聚物PS_(168)-b-P4VP_(420)的自组装聚集体的结构由常压(0.1 MPa)下以球形胶束为主转变为高压下(6.35 MPa)以互联棒状胶束结构为主,而PS_(790)-b-P4VP_(263)的SAA结构则由常压下的小型囊泡过渡到6.35 MPa下的大复合囊泡(LCVs)。但是对于PS_(153)-b-P4VP_(1530),随着压力的调节,其SAA的结构由常压(0.1 MPa)下的大复合胶束(LCMs)转变为6.35 MPa下的大复合囊泡(LCVs)。特别是,我们发现在本工作考察的实验条件下,在常规溶剂甲苯中控制SAA结构的主要因素是共聚物的组成;而在CXLs条件下,PS壳链与溶剂CXLs间的接触面积随压力调节而发生的改变,可能是控制SAA形貌转变的主要因素。此外,随着CXLs压力升高而引起的PS与P4VP嵌段间双亲性差别的减小,会引起P4VP核-PS壳的界面间的表面张力发生改变,这也是触发SAA形貌转变的诱因之一。本工作充分显示了CXLs方法有助于可控调节自组装聚集体(SAA)的形貌和组装行为,为研发复合纳米材料开辟了一条崭新的绿色途径。     

磷钨酸对对苯撑乙烯撑寡聚物-b-聚(2-乙烯基吡啶)自晶种行为的影响※

自晶种具有操作简便和聚合物组装基元适用性广的优点, 它是利用结晶-柔性(crystalline-coil)两嵌段共聚物活性结晶驱动自组装制备长度和组成可控的聚合物纳米纤维的重要策略. 而多金属氧酸及其衍生物具有独特的化学组成和几何结构以及优异的电/磁/光等物理性能. 以对苯撑乙烯撑寡聚物-b-聚(2-乙烯基吡啶)(OPV₅-b-P2VP₄₂)和磷钨酸(H₃O₄₀PW₁₂)分别为模型结晶-柔性两嵌段共聚物和多金属氧酸, 系统考察了磷钨酸对OPV₅-b-P2VP₄₂自晶种行为的影响. 研究发现OPV₅-b-P2VP₄₂的种子纤维在加热退火时的抗溶解能力随着磷钨酸的量增大而增强. 这可能是由于P2VP中的吡啶基元与磷钨酸金属原子间的络合作用, 而非吡啶与磷钨酸间的氢键作用, 使P2VP链间发生交联/聚集, 这不仅可平衡或减弱P2VP链间的排斥力和拉伸作用, 还将提升种子纤维断裂和解离所需的能量.     

以PS-b-P2VP为模板剂诱导调控聚苯胺形貌、尺寸及电化学性能

采用可逆加成-断裂链转移自由基聚合（RAFT）法合成了具有pH响应性的两亲嵌段共聚物聚苯乙烯-b-聚（2-乙烯基吡啶）（PS₁₀₁-b-P2VP₇₀），并以其胶束为"模板"，通过氧化聚合制备聚苯胺（PANI）.通过调节PS₁₀₁-b-P2VP₇₀胶束溶液的pH值，探究PANI颗粒形貌的可控调节及颗粒尺寸与PANI电化学性能之间的关系.利用凝胶渗透色谱（SEC）和核磁共振氢谱（¹H NMR）确定了PS₁₀₁-b-P2VP₇₀的分子量分布及结构；利用傅里叶变换红外光谱（FTIR）、透射电子显微镜（TEM）、粒度测试、循环伏安（CV）、计时电位（Chronopotentio-metry）及交流阻抗谱（EIS）对PANI结构、形貌和电化学性能进行了表征.结果表明"模板"法合成的PANI形貌尺寸得到了很好的控制，在pH ≤ 4时其尺寸随pH值的增加而减小；当pH=5时，模板剂中P2VP段疏水性的明显增大导致其胶束颗粒聚集为尺寸较大的聚集体，并使其诱导的PANI颗粒平均粒径显著增大；当pH=4时PANI颗粒在溶液中的平均粒径为141 nm，呈"串状"形貌且分散性最好.PANI具有快速充放电能力和良好的赝电容特性，随颗粒尺寸减小样品电化学性能增强.pH=4时样品电化学活性最好，循环伏安曲线面积最大，放电比容量最高，在电流密度为1 A/g时，其放电比容量可达1411.88 F/g，且该样品阻抗值最小.     

中间嵌段为亲水性的BAB型三嵌段共聚物水溶液中初级聚集体的二次聚集行为研究

采用TEM和AFM研究了PS(聚苯乙烯)₄₃-b-PEO(聚氧乙烯)₄₅-b-PS₄₃和PS₃₉-b-P4VP(聚4-乙烯基吡啶)₉₈-b-PS₃₉三嵌段共聚物在水介质中的球形胶束、囊泡和蠕虫状胶束之间的二次聚集行为.实验发现,初级聚集体的二次聚集具有不同的复杂程度.对称性的初级聚集体,如球形胶束和囊泡,其二次聚集表现出球形对称性;而非对称性初级聚集体(如蠕虫状胶束)二次聚集开始倾向于非对称性.BAB型的嵌段设计有利于初级聚集体的二次聚集发生.     

PS-b-P4VP/PFOA配合物在氯仿中的自组装及形态表征

全氟辛酸(PFOA)与聚苯乙烯-b-聚-4-乙烯吡啶(PS-b-P4VP)的配合能诱导嵌段共聚物在其共同溶剂氯仿中胶束化. 胶束化不仅能形成棒状聚集体, 还能得到椭球形胶束. 当嵌段共聚物PS-b-P4VP浓度为1.0 g/L时, 使用光散射和扫描电镜研究了MR值(全氟辛酸与聚合物中吡啶环的物质的量比)在1/30到1/10之间的聚集行为及形态. 发现即使当MR值小到1/30时仍然形成稳定的聚集体. 通过扫描电镜观察发现: 改变MR值可以获得不同形态的聚集体.     

两亲性/双疏性嵌段共聚物共混体系的自组装行为研究

采用耗散粒子动力学方法,研究了两亲性嵌段共聚物和双疏性嵌段共聚物共混体系的自组装行为,探讨了双疏性嵌段共聚物的浓度以及双疏性嵌段共聚物的嵌段体积分数对聚集体结构的影响.结果表明,随着双疏性嵌段共聚物浓度的增加,聚集体发生自囊泡到棒状胶束再到同心圆多舱胶束的转变,且当浓度较高时,同心圆多舱胶束的同心圆层数量与浓度密切相关.当双疏性嵌段共聚物中的嵌段体积分数降低时,球形胶束由同心圆结构转变为非同心圆结构.此外,利用Minkowski泛函方法表征了多舱胶束的形成过程,发现这是一个先形成大尺度球形结构、再形成小尺度内核结构的分级组装过程.     

剪切作用对PS-b-P2VP-b-PEO三嵌段共聚物多节状蠕虫胶束形成的影响

实验研究了剪切(搅拌)对ABC三嵌段共聚物PS720-b-P2VP200-b-PEO375在溶液中自组装形成的胶束形态的影响,研究结果表明剪切对多节状蠕虫胶束的生成和结构有着重要作用.在1500 r/min剪切速率时,嵌段共聚物自组装形成的球形胶束首先聚集形成蠕虫胶束的梭状轮廓,然后再经过不断地融合与调整形成蠕虫胶束节状部分的盘状结构,同时球的融合趋于沿着垂直于梭状结构的主轴方向(即流场方向).溶剂THF对PS嵌段充分的溶胀使得球形胶束进一步调整形成盘状结构,从而使梭状胶束聚集体顺利地向多节状蠕虫胶束过渡.通过透射电镜(TEM)和扫描电镜(SEM)对胶束形态进行表征,结果表明,多节状蠕虫胶束是剪切作用下球形胶束二次自组装的结果.     

基于P4VP-b-PBzMA嵌段聚合物在乙醇中的聚合诱导自组装

聚合诱导自组装是一种基于活性聚合的新型自组装策略,其特点是可以在较高固含量体系中一步制备不同形貌的聚集体结构.利用可逆加成-断裂链转移聚合(RAFT)活性聚合,在乙醇溶液中合成新型P4VP-b-PBz MA嵌段共聚物,发现聚合诱导自组装过程中聚集体结构发生球→蠕虫→囊泡的连续转变.亲溶剂链段P4VP的变化可有效调控聚集体的结构和尺寸.此外,采用无规共聚方法,研究了P4VP-b-(PHPMA-co-PBz MA)三嵌段共聚物在聚合诱导自组装过程中组装体结构的转变过程.     

聚乙二醇-接枝-聚(γ-苄基L-谷氨酸酯)刚-柔接枝共聚物的合成及其自组装行为研究

通过负离子开环聚合,合成了以柔性亲水的聚乙二醇(PEG)为主链,刚性疏水的聚(γ-苄基L-谷氨酸酯)(PBLG)为侧链的PEG-g-PBLG刚-柔接枝共聚物.运用核磁共振氢谱(1H-NMR)、傅里叶变换红外光谱(FTIR)和凝胶渗透色谱(GPC)等表征了共聚物的结构、分子量及其分布.以共溶剂溶解、选择性溶剂透析的方法制备了自组装聚集体.利用扫描电子显微镜(SEM)、透射电子显微镜(TEM)、原子力显微镜(AFM)和激光光散射(LLS)等表征了共聚物自组装体的形貌和结构.研究发现,基于其特殊的拓扑结构,接枝共聚物的自组装行为表现出与一般规律不同的变化趋势.具有较短疏水PBLG侧链的PEG-g-PBLG可以自组装形成球形复合胶束,随着疏水PBLG侧链的增长,聚集体逐渐由复合胶束转变为囊泡,这种现象在已有的研究中鲜有报道.此外,降低初始聚合物溶液的浓度,共聚物自组装得到的聚集体的尺寸变小而分布变宽;反之,聚集体的尺寸增大而分布变窄.还利用耗散粒子动力学方法,验证了实验中聚集体的形貌变化,并给出了聚集体中的链段分布等在实验中较难得到的信息.     

聚苯乙烯-聚(4-乙烯基吡啶)嵌段共聚物LB膜结构形态的研究

采用氯仿作为铺展溶剂,将嵌段共聚物聚苯乙烯-聚(4-乙烯基吡啶)(PS-b-P4VP)稀溶液铺展于空气与水界面上,利用Langmuir-Blodgett(LB)膜技术转移至固体基底.研究了不同的嵌段比、表面压和小分子1-芘丁酸(PBA)的加入对嵌段共聚物气液界面聚集组装的影响.研究发现随着亲水段(P4VP)的增加,聚集组装结构由纳米片状、带状转变成纳米条状、纳米点状结构.表面压对纯PS-b-P4VP聚集组装产生影响,表面压增大,组装体排列紧密;随着表面压的继续增大,单层聚集结构遭到破坏,发生堆叠.加入PBA小分子后,PBA与PS-b-P4VP形成氢键,形态发生明显变化,原来的片状结构转变为条状或点状结构.     

含侧链盘状苯并菲和棒状偶氮苯的二嵌段液晶共聚物的可控合成及其光物理性质

分别通过可逆加成-断裂链转移（RAFT）聚合和原子转移自由基聚合（ATRP）结合叠氮-端炔基大分子点击反应,制备了一系列不同聚合度和不同嵌段比例的基于侧链苯并菲TP盘状液晶基元和偶氮苯Azo棒状液晶基元的盘棒杂化二嵌段共聚物。采用核磁共振氢谱（¹H NMR）、凝胶渗透色谱（GPC）、差示扫描量热分析（DSC）和正交偏光分析（POM）对盘棒杂化二嵌段共聚物的组成结构、相对分子质量和液晶相行为进行了表征。偶氮苯嵌段较短的共聚物P（TP₆）₄₀-b-P（Azo）₁₀,主要表现出占优势嵌段TP盘状液晶聚合物的热转变温度与相行为。而偶氮苯嵌段较长的共聚物P（TP₆）₁₀-b-P（Azo）₄₀和P（TP₆）₄₀-b-P（Azo）₄₀则更多体现出类似Azo棒状侧链液晶聚合物的相行为和光响应特性。小角/广角X射线散射（SAXS/WAXS）分析证实了Azo嵌段较长的嵌段共聚物薄膜尤其经退火处理后呈现层状结构,倾向于平行基底取向排布的苯并菲诱导偶氮苯平躺沿着平行基底方向排列而显著减少了光吸收,经紫外及可见光的辐照后光吸收显著增大,其中盘状嵌段较长的P（TP₆）₄₀-b-P（Azo）₄₀对比响应增幅尤其明显。这种盘棒杂化二嵌段共聚物薄膜所表现出的特殊光物理性质及其快速光响应-回复特性,加深了对其相互作用的理解,可望为设计合成新的光响应材料提供参考依据。     

H型(PS)2PEG(PS)2嵌段共聚物在旋涂过程中的结晶行为

采用原子力显微镜和X射线衍射等手段研究了H型(PS)₂PEG(PS)2嵌段共聚物在不同溶剂和不同浓度的溶液中旋涂所得薄膜的形貌, 并与聚乙二醇(PEG)均聚物进行了比较. 虽然(PS)₂PEG(PS)₂中PS的链长很短, 但对形貌有很大影响, PS链段的存在改变了聚合物在基底上的稳定性, 使用四氢呋喃为溶剂, 当溶液浓度较小时, 在旋涂过程中发生去润湿, 然后再发生结晶, 膜厚较大时去润湿被抑止, 所得形貌与PEG均聚物类似. 以甲苯为溶剂时, 由于PEG和PS与溶剂的相互作用不同, 共聚物在溶液中形成胶束, 从而改变了聚合物的结晶形貌.     

Palladium-catalyzed Heck coupling reactions using different fluorinated phosphine ligands in compressed carbon dioxide and conventional organic solvents

Palladium-catalyzed Heck reaction of iodobenzene and styrene was investigated in compressed CO₂ using different fluorinated phosphine compounds as ligands at a temperature of 70 °C. The reaction mixture is a single phase at 12 MPa but biphasic at 8 MPa, a little higher than the critical pressure of pure CO₂ under the reaction conditions used. Although the solubility of fluorinated ligands is very high in dense CO₂, they have marginal improvements in Heck conversion in this medium compared with a non-fluorinated ligand of triphenylphosphine. The activity of palladium complexes strongly depends on the kind of phosphine compound used, in the order of bis(pentafluorophenyl)phenylphosphine (III)>triphenylphosphine (I), tris(pentafluorophenyl)phosphine (IV)>diphenyl(pentafluorophenyl)phosphine (II), tris(p-fluorophenyl)phosphine (V)>tris(p-trifluoromethyl phenyl)phosphine (VI), 1,2-bis[bis(pentafluorophenyl)phosphino]ethane (VII), for the homogeneous reaction at 12 MPa. This order of effectiveness of these ligands is different from those obtained in conventional organic solvents. Hexane, toluene, ethanol, and N-methylpyrrolidone (NMP) showed maximum conversions with the ligands VI, IV, V and VII, respectively. The conversion in CO₂ with the ligand III is comparable with those in polar solvents of ethanol and NMP, and larger than those in hexane and toluene in the presence of the best ligands. The dense CO₂ may affect the specific activity of palladium complex catalysts and/or the reactivity of reacting species. Small quantities of fluorinated products were observed to form at high pressure of CO₂ and this is direct evidence of P–C bond cleavage during Heck reaction in dense CO₂. The activity of palladium complexes with those ligands is higher in more polar solvent.     

Gas permeation properties of asymmetric carbon hollow fiber membranes prepared from asymmetric polyimide hollow fiber

Asymmetric carbon hollow fiber membranes were prepared by pyrolysis of an asymmetric polyimide hollow fiber membrane, and their mechanical and permeation properties were investigated. The carbon membrane had higher elastic modulus and lower breaking elongation than the polyimide membrane. Permeation experiments were performed for single gases such as H₂, CO₂, and CH₄, and for mixed gases such as H₂/CH₄ at high feed pressure ranging from 1 to 5 MPa with or without toluene vapor. The permeation properties of the carbon membranes and the polyimide membrane were compared. There was little change in the properties of the carbon membranes with a passage of time. The properties were hardly affected by the feed pressure, whether the feed was accompanied with the toluene vapor or not, because the carbon membranes were not affected by compaction and plasticization.     

Poly(N,N-dimethylaminoethyl methacrylate)–poly(ethylene oxide) copolymer membranes for selective separation of CO2

A series of copolymers containing ether oxygen groups and amino groups were prepared based on N,N-dimethylaminoethyl methacrylate (DMEMA) and polyethylene glycol methyl ether methyl acrylate (PEGMEMA). The effect of PEGMEMA content in the copolymer on density, free volume, mechanical performance, and H₂, CO₂, N₂ and CH₄ gas transport properties of the copolymer was determined. Free volume was characterized using the polymer density and group contribution theory. The permeability of the copolymer to CO₂ is high, and both the CO₂/N₂ and CO₂/H₂ selectivities are high. For example, the permeability coefficient of PDMAEMA–PEGMEMA-90 (“90” represents the weight percent of PEGMEMA) to CO₂ is 112 Barrer and the CO₂/N₂ and CO₂/H₂ selectivity coefficients are 31 and 7, respectively. The effect of the temperature on gas transport properties was also determined. Finally, the potential application of the copolymer membranes for CO₂/light gases separation was explored.     

Gas transport property of polyallylamine–poly(vinyl alcohol)/polysulfone composite membranes

Polyallylamine (PAAm) was synthesized by free radical polymerization and characterized by Fourier transform infrared resonance (FT-IR) spectroscopy, hydrogen nuclear magnetic resonance (¹H NMR) spectroscopy and differential scanning calorimetry (DSC). The composite membranes were prepared by using PAAm–poly(vinyl alcohol) (PVA) blend polymer as the separation layer and polysulfone (PSF) ultrafiltration membranes as the support layer. The surface and cross-section morphology of the membrane was inspected by environmental scanning electron microscopy (ESEM). The gas transport property of the membranes, including gas permeance, flux and selectivity, were investigated by using pure CO₂, N₂, CH₄ gases and CO₂/N₂ gas mixture (20 vol% CO₂ and 80 vol% N₂) and CO₂/CH₄ gas mixture (10 vol% CO₂ and 90 vol% CH₄). The plots of gas permeance or flux versus feed gas pressure imply that CO₂ permeation through the membranes follows facilitated transport mechanism whereas N₂ and CH₄ permeation follows solution–diffusion mechanism. Effect of PAAm content in the separation layer on gas transport property was investigated by measuring the membranes with 0–50 wt% PAAm content. With increasing PAAm content, gas permeance increases initially, reaches a maximum, and then decreases gradually. For CO₂/N₂ gas mixture, the membranes with 10 wt% PAAm content show the highest CO₂ permeance of about 1.80 × 10⁻⁵ cm³ (STP) cm⁻² s⁻¹ KPa⁻¹ and CO₂/N₂ selectivity of 80 at 0.1 MPa feed gas pressure. For CO₂/CH₄ gas mixture, the membranes with 20 wt% PAAm content display the highest CO₂ permeance of about 1.95 × 10⁻⁵ cm³ (STP) cm⁻² s⁻¹ KPa⁻¹ and CO₂/CH₄ selectivity of 58 at 0.1 MPa feed gas pressure. In order to explore the possible reason of gas permeance varying with PAAm content, the crystallinity of PVA and PAAm–PVA blend polymers was measured by X-ray diffraction (XRD) spectra. The experimental results show an inverse relationship between crystallinity and gas permeance, e.g., a minimum crystallinity and a maximum CO₂ permeance are obtained at 20 wt% PAAm content, indicating that the possibility of increasing CO₂ permeance with PAAm content due to the increase of carrier concentration could be weakened by the increase of crystallinity.     

Gas permeation of poly(amide-6-b-ethylene oxide) copolymer

Block copolymers exhibit a different gas permeation behavior from that of homopolymers. In the diffusion process, the fraction of impermeable regions in the block copolymer decreases the diffusivity and the permeability. As the amount of impermeable regions in the block copolymer increases, the flow paths for the gas diffusion are restricted. Poly(amide-6-b-ethylene oxide) (PEBAX^®) copolymer consists of a regular linear chain of rigid polyamide for hard segment interspaced with flexible polyether for soft segment. PEBAX^® copolymer shows a typical permeation behavior of rubbery polymers. The permeability of CO₂ increases with the pressure originating from the increment of the sorbed CO₂ amounts. PEBAX^® copolymer shows the high permeability and the high selectivity for polarizable/nonpolar gas pairs. Particularly, the selectivity of CO₂ over N₂ is 61 and that of SO₂ over N₂ is 500. For small and nonpolar gases (i.e. He, H₂, O₂ and N₂), the permeability decreases with increasing the molecular size or volume of gases. On the other hand, for polarizable and larger gases (i.e. CO₂ and SO₂), it shows the high permeability. The high permeability and permselectivity of PEBAX^® copolymer are attributed of polarizable gases to polyether segment in PEBAX^®.     

二氧化碳/甲烷/氮气二元混合物在有序介孔碳材料CMK-3 中的吸附和分离

采用分子模拟与吸附理论研究了天然气成分在有序介孔碳材料CMK-3上的吸附和分离.巨正则系综蒙特卡罗(GCMC)模拟表明,CH4和CO2气体的较优存储条件分别为208 K、4 MPa和298 K、6 MPa,其最大超额吸附量分别为10.07和14.85 mmol· g-1.基于双位Langmuir-Freundlich (DSLF)模型,使用理想吸附溶液理论(IAST)预测了不同二元混合物在CMK-3中的分离行为,发现吸附选择性Sco2/CH4与ScH4/N2比较接近,在298 K和4 MPa下约等于3,而N2-CO2体系中的CO2吸附选择性较高,可达到7.5,说明CMK-3是一种适合吸附和分离天然气组分的碳材料.     

改性橄榄石对C_7H_8/CO_2催化重整的影响

在固定床反应器中,以甲苯作为生物质气化焦油模型化合物,橄榄石作为甲苯裂解催化剂,结合XRD、SEM、BET、H2-TPR等表征手段,考察了不同重整反应温度、CO_2浓度、橄榄石煅烧温度以及载镍量对甲苯催化重整性能的影响。结果表明,甲苯转化率随着重整反应温度的升高而增加,橄榄石对甲苯具有较高的催化活性,经900℃煅烧后的橄榄石活性最高。相比于橄榄石直接催化裂解甲苯,CO_2的加入能够显著降低催化剂表面的积炭率,当CO_2/C_7H_8物质的量比为4时,橄榄石催化剂表面的积炭率降低至17.0%。橄榄石载镍后,对C_7H_8/CO_2的催化重整性能进一步提高,甲苯转化率最高达到99.4%,但是积炭率也会随之增加。