二氧化硅负载杂多酸对异丁烷与丁烯烷基化的催化作用Ⅰ.催化剂的制备、表征和失活

 采用浸渍法制备了二氧化硅负载的磷钨酸催化剂,系统考察了催化剂的比表面积、结晶水、结构特征和酸性等物化性质. 将在不同条件下制备的不同结构的杂多酸催化剂用于异丁烷与丁烯烷基化反应,考察了催化剂活性组分、制备方法和反应条件对催化剂性能的影响,分析了催化剂的失活过程和失活机理. 结果表明,当负载量不大于50%时,磷钨酸以单分子层形式均匀分散于载体表面,催化剂表面存在大量的强B酸中心,不存在L酸中心; 经160 ℃活化后的催化剂具有最大的酸量和最强的酸性; 催化剂对烷基化反应具有较高的初活性,但随着反应的进行催化剂迅速失活; 反应产物的组成与催化剂失活程度密切相关,反应初期产物以烷烃为主,之后产物则以烯烃为主; 催化剂的失活原因为积碳.     

醋酸仲丁酯加氢反应中Cu/B/Ca/Al_2O_3催化剂的失活及再生

Cu/B/Ca/Al2O3催化剂在长达1 118 h的催化醋酸仲丁酯加氢反应中出现了明显的失活.经过对比分析反应前、后和再生催化剂的组成、形貌和结构,发现金属铜粒子在长时间反应后无明显聚集,醋酸仲丁酯加氢反应中部分氧化钙向醋酸钙转变而引起催化剂结构的改变以及有机物种在催化剂表面的沉积是其失活的根本原因.失活后的催化剂经过350℃空气焙烧再生能够有效消除表面沉积的醋酸钙和有机物种,基本恢复催化剂的结构及其催化醋酸仲丁酯加氢反应的性能.     

PVA-g-PS复合微球的制备与粒径控制研究

由链转移自由基聚合与端基置换反应法,合成了苯乙稀基单封端的聚醋酸乙烯酯(PVAc)大分子单体,使其与苯乙烯在乙醇/水的混合介质中进行自由基分散共聚,得到了表面以PVAc为接枝链的聚苯乙烯(PVAc-g-PSt)微球。将所得微球在碱性条件下醇解,形成了以亲水性聚乙烯醇(PVA)为壳、聚苯乙烯为核的复合微球(PVAc-g-PSt)。用核磁共振对聚合物的结构进行表征,定出了PVAc末端双键的含量;并用激光光散射、扫描电子显微镜对微球的粒径与形态进行了表征。研究结果表明,在共聚反应体系中大分子单体的分子量与浓度、苯乙烯浓度、引发剂浓度及溶剂的组成对微球的形态和粒径大小有明显影响。     

通过远端碳氮双键迁移实现非活化烯烃的三氟甲硫基化反应

利用自由基参与的官能团迁移策略实现了非活化烯烃的三氟甲硫基化反应.通过AgSCF₃和K₂S₂O₈相互作用产生的三氟甲硫基自由基与非活化烯烃反应,继而诱导远端含有碳氮双键官能团（杂芳基、亚胺）的分子内迁移,从而实现非活化烯烃的三氟甲硫基化反应.该转化具有反应条件温和、产物收率高、官能团兼容性广及区域选择性单一等特点,对具有不同电性和位阻的底物具有较好的适用性,高效构建了一系列含有三氟甲硫基的烷烃酮化合物.     

费托合成中Co/ZrO2/SiO2催化剂的失活行为

 采用等体积分步浸渍法制备了费托合成用Co/ZrO2/SiO2催化剂,并用XRD,TPR和N2-吸附等手段对催化剂进行了表征. 考察了催化剂在费托反应过程中的结构变化和失活行为. 结果表明,反应过程中硅酸钴物种的生成是催化剂失活的主要原因,且硅酸钴的生成与产物水的分压有关; 晶粒长大也可能是催化剂失活的原因之一.     

可逆加成-断裂链转移自由基共聚合研究进展

与其它可控/活性自由基聚合相比,可逆加成-断裂链转移(RAFT)自由基聚合具有适用单体范围广、反应条件温和、不受聚合实施方法的限制等优点,因此成为目前高分子合成研究最为活跃的领域之一.通过它不但实现了广泛单体的可控/活性聚合,还合成了嵌段、接枝、梳型、星型、无规及梯度等结构的聚合物.本文综述了RAFT自由基共聚合领域的研究进展,内容主要包括已报道的RAFT自由基共聚合反应体系和RAFT过程对共聚产物组成的影响.     

Ni/SiO2催化剂上甲烷催化裂解制氢

研究了固定床反应器上甲烷在Ni/SiO2催化剂上的裂解反应，并分别用O2、H2O进行催化剂失活/活化循环实验，并对催化剂用XRD进行分析。结果表明,Ni/SiO2催化剂具有良好的催化性能,甲烷转化率～40%，并能在150 min的时间内保持其活性，无论是用空气氧化还是水蒸气汽化，都能有效地活化已失活的催化剂。XRD实验显示，多次裂解－再生循环过程，对催化剂结构没有明显破坏。     

印刷电路板中环氧树脂热解的ReaxFF反应动力学模拟

采用ReaxFF动力学方法模拟了非交联固化环氧树脂在不同温度和升温速率下的热解特性. 结果表明, 含N和含O桥键的断裂是热解的引发反应. 观察到H₂O的4种主要的生成途径, 而这些反应途径都涉及到含羟基的前驱体. 当反应温度较低时, H₂O为热解的主要产物. 而在高温条件下, 热解的主要产物为H₂, 它主要为分子内/分子间脱氢反应和氢自由基的夺氢反应的产物; 高温同时促进了含石墨烯结构且分子量较大的碳团簇的形成. 除此之外, 还观察到了CH₄, HCN, NH₃和CO等小分子产物. 本文用ReaxFF动力学方法模拟所得的气体产物以及含类似石墨烯结构的碳团簇与实际实验结果一致, 说明ReaxFF动力学方法能为从分子水平上研究有机物高温热解反应提供了一种有效的途径.     

沸石分子筛中复杂异构化反应的Monte Carlo模拟研究 Ⅲ．孔口失活对反应行为的影响

用Ｍｏｎｔｅｃａｒｌｏ方法模拟了沸石分子筛中的复杂异构化反应ＡＢＣ，考察了孔口失活对反应性能的影响．发现孔口失活对产物选择性和反应有效因子的影响取决于反应的Ｔｈｉｅｌｅ模数．可分为三种情况：（１）在低Ｔｈｉｅｌｅ模数下，影响不明显；（２）在中等Ｔｈｉｅｌｅ模数下，有一定的影响，且随孔口活性位失活率的增加，某种产物的选择性线性增加而有效因子线性下降，但二者变化幅度均不大；（３）在较高Ｔｈｉｅｌｅ模数下，影响显著．随着孔口活性位失活率的增加，某种产物选择性明显增加，有效因子明显下降．     

电子顺磁共振法研究Fe-Sb-W氧化物催化剂的失活机理

用电子顺磁共振法(ESR)研究了丙烯氨氧化Fe-Sb-W氧化物催化剂的失活机理,记录了沉积在催化剂表面上的焦炭和催化剂结构变化的信息。结果表明:当沉积炭超过一定限度之后,发生反应:,使催化剂表面上的活性结构破坏。这时催化剂严重失活,主要产物是CO₂。     

不同软段结构聚氨酯-酰亚胺嵌段共聚物的合成及热性能研究

用二步法合成了不同软段 (PPO ,PEG ,PEPA)聚氨酯 酰亚胺 (PUI)嵌段共聚物 ,FTIR光谱表征了所有合成PUI分子主链均含有酰亚胺链段 ,并研究了PUI嵌段共聚物的热性能受软段类型及长度的影响 .DSC研究表明聚酯型PUI的软硬段之间的相容性比聚醚型PUI好 ,随相同软段分子量的增加 ,PUI体系的软硬段兼容性变差 ,并显示了相分离的特征 ;热失重 (TGA)研究得出不同软段的PUI样品的热稳定性大小顺序为 :PEPA PUI >PEG PUI>PPO PUI ;动态力学 (DMTA)研究给出了所合成的PUI样品在 5 0～ 2 0 0℃范围内均出现了较长的模量平台显示出有较好的耐热性 ,且随硬段含量的升高其储能模量不断增强     

多嵌段聚醚-酯共混物的微相结构与血液相容性研究

本工作合成了两种性质不同的聚醚-酯多嵌段共聚物,一种是以聚对苯二甲酸乙二酯为硬链段,聚乙二醇(PEGT)为软链段的亲水性多嵌段共聚物,另一种是以聚对苯二甲酸乙二酯为硬链段,聚四亚甲基醚二醇(PTMGT)为软链段的疏水性多嵌段共聚物。将两种共聚物以一定的比例共混,制备多嵌段聚醚-酯共混物。 改变共混物的组成,研究其微相结构与血液相容性的关系。采用动态力学谱(VES)、示差扫描量热(DSC)、透射电镜(TEM)和扫描电镜(SEM)等测定共混物的微观结构,采用微球柱法评价共混物的血液相容性。实验结果表明:材料的微观非均相结构及亲水平衡是决定血液相容性的重要因素。     

Controlling retention, selectivity and magnitude of EOF by segmented monolithic columns consisting of octadecyl and naphthyl monolithic segments--applications to RP-CEC of both neutral and charged solutes

Monolithic capillaries made of two adjoining segments each filled with a different monolith were introduced for the control and manipulation of the electroosmotic flow (EOF), retention and selectivity in reversed phase-capillary electrochromatography (RP-CEC). These columns were called segmented monolithic columns (SMCs) where one segment was filled with a naphthyl methacrylate monolith (NMM) to provide hydrophobic and π-interactions, while the other segment was filled with an octadecyl acrylate monolith (ODM) to provide solely hydrophobic interaction. The ODM segment not only provided hydrophobic interactions but also functioned as the EOF accelerator segment. The average EOF of the SMC increased linearly with increasing the fractional length of the ODM segment. The neutral SMC provided a convenient way for tuning EOF, selectivity and retention in the absence of annoying electrostatic interactions and irreversible solute adsorption. The SMCs allowed the separation of a wide range of neutral solutes including polycyclic aromatic hydrocarbons (PAHs) that are difficult to separate using conventional alkyl-bonded stationary phases. In all cases, the k' of a given solute was a linear function of the fractional length of the ODM or NMM segment in the SMCs, thus facilitating the tailoring of a given SMC to solve a given separation problem. At some ODM fractional length, the fabricated SMC allowed the separation of charged solutes such as peptides and proteins that could not otherwise be achieved on a monolithic column made from NMM as an isotropic stationary phase due to the lower EOF exhibited by this monolith.     

两嵌段共聚高分子在固液界面吸附的Monte Carlo模拟(Ⅰ)——吸附链的构型分布

用MonteCarlo方法对两嵌段共聚高分子在固液界面的吸附进行模拟,获得了固液界面区吸附链节的分布和吸附构型大小分布等微观信息.考察了吸附性链节的吸附能ε_Aa和两嵌段共聚高分子中吸附性链节比例f对固液界面区高分子链节的分布和各种吸附构型大小的影响.结果表明,吸附层厚度主要由两嵌段共聚高分子中非吸附性链段的长度决定.     

The three-dimensional model for helical columns on type-J synchronous counter-current chromatography

Unlike the existing 2-D pseudo-ring model for helical columns undergoing synchronous type-J planetary motion of counter-current chromatograph (CCC), the 3-D "helix" model developed in this work shows that there is a second normal force (i.e. the binormal force) applied virtually in the axial direction of the helical column. This force alternates in the two opposite directions and intensifies phase mixing with increasing the helix angle. On the contrary, the 2-D spiral column operated on the same CCC device lacks this third-dimensional mixing force. The (principal) normal force quantified by this "helix" model has been the same as that by the pseudo-ring model. With β>0.25, this normal centrifugal force has been one-directional and fluctuates cyclically. Different to the spiral column, this "helix" model shows that the centrifugal force (i.e. the hydrostatic force) does not contribute to stationary phase retention in the helical column. Between the popular helical columns and the emerging spiral columns for type-J synchronous CCC, this work has thus illustrated that the former is associated with better phase mixing yet poor retention for the stationary phase whereas the latter has potential for better retention for the stationary phase yet poor phase mixing. The methodology developed in this work may be regarded as a new platform for designing optimised CCC columns for analytical and engineering applications.     

聚乙二醇/聚对苯二甲酸丁二醇酯聚醚酯弹性体的合成与表征——不同硬段长度对材料性能的影响

以熔融缩聚法合成了一系列基于聚乙二醇 (PEG) 聚对苯二甲酸丁二醇酯 (PBT)的聚醚酯热塑性弹性体 ,用NMR、IR、DSC及力学性能测试等方法表征了材料的结构及性能 .讨论了在相同软段长度情况下 ,不同硬段长度对材料结构与性能的影响 .实验表明 ,随着体系中硬段PBT长度的减小 ,弹性模量、抗拉强度降低 ,特性粘度、吸水量及断裂形变量增加 ,材料性能良好可调     

Characters of the Plateau of Methanol Increment in Frontal Analysis in Reversed Phase Liquid Chromatography

With insulin methanol-water,and the ion-pairing agent,hydrochloric acid and trifluroacetic acid(TEA),the character of the first plateau(FP)on the elution curve of frontal analysis in reversed phase liquid chromatography(RPLC)was investigated by on-line UV-spectrometry and identified with nuclear magnetic resonance(NMR) spectrometry and mass spectrometry.The profile of the FP is the same as that of a usual elution curve of methanol in frontal analysis(FA).When the insulin concentration was limited to a certain range,the height of the FP was found to be proportional to the insulin concentration in mobile phase and its length companying to shorten,The FP profile on the intersection of two tangents reflects the components of the microstructure in the depth direction of the bonded stationary phase layer and the desorption dynamics of the displaced components.The displaced methanol was quantitatively determined by NMR and on-line UV spectrometries.TFA with high UV absorbance can not be used as an ionpairing agent for the investigation of the FP in RPLC,but if can be used as a good marker to investigate the complicated transfer process of components in the stationary phase in RPLC.A stoichiometric displacement process between solute and solvent was proved to be valid in both usual and FA in RPLC.From the point of view of dynamics of mass transfer, the solutes can only contact to the surface of stationary phase in usual RPLC,while solute can penetrate into it in FA of RPLC.The solvation of insulin in methanol and water solution as an example indicating the usage of the FP in the FA was also investigated in this paper.     

Density functional theory for inhomogeneous associating chain fluids

We propose a nonlocal density functional theory for associating chain molecules. The chains are modeled as tangent spheres, which interact via Lennard-Jones (12,6) attractive interactions. A selected segment contains additional, short-ranged, highly directional interaction sites. The theory incorporates an accurate treatment of the chain molecules via the intramolecular potential formalism and should accurately describe systems with strongly varying external fields, e.g., attractive walls. Within our approach we investigate the structure of the liquid-vapor interface and capillary condensation of a simple model of associating chains with only one associating site placed on the first segment. In general, the properties of inhomogeneous associating chains depend on the association energy. Similar to the bulk systems we find the behavior of associating chains of a given length to be in between that for the nonassociating chains of the same length and that for the nonassociating chains twice as large.     

Modelling of elution-extrusion counter-current chromatography using perfect replacement approach

Basing on the perfect replacement approach the equilibrium cell model is developed to describe the separation process in elution-extrusion counter-current chromatography (EECCC). As is known, EECCC consists of three steps: classical elution, sweeping elution, and extrusion. The perfect replacement approach means that during sweeping elution step, the mobile phase contained in the column moves and interacts with the "old" stationary phase in the same mode as during the classical elution step; the "new" and "old" stationary phases do not mix; and after the contacting with the mobile phase the concentration of solutes in the "old" stationary phase remains constant and this stationary phase volume is pushed ahead to the exit of the column. Equations are presented allowing the simulation of the chromatogram of solutes eluted from the column with the mobile phase during the elution period and the chromatogram of solutes pushed out of the column with the stationary phase during the extrusion period of EECCC. These equations can help to choose the optimal conditions for conducting elution-extrusion counter-current chromatography.     

Thermal analysis of polyurethane elastomers matrix with different chain extender contents for thermal conductive application

Polyurethane elastomers (PUR) based on polypropylene glycol and 4,4′-diphenylmethane diisocyanate were prepared with various monoethylene glycol (mEG) contents. The aim of this study is to find a reliable polymer matrix for composites of improved thermal conductivity and testing fully in order to collect knowledge about its structure. Thermal conductivity was improved from 0.255 to 0.329 W m^?1 K^?1 when increasing chain extender content. This attributed to a high appearance crystalline ordering level when adding high mEG content. Differential scanning calorimetry revealed a low transition temperature of soft segment at the same temperature around ??64 °C, due to constant polyol content. The enthalpy of melting increases with increasing mEG content. This is due to the increasing crystalline phase and hard segment phase separation within the PUR structure. Dynamic mechanical analysis results show the glass transition temperature of soft segment in the same temperature range between ??57 and ??52 °C and intensity peak of tanδ tends to decrease when mEG content was increased. On the other hand, the glass transition temperature of hard segment tends to increase from 10 to 93 °C and has high intensity peak of tanδ with increasing mEG content. Increasing the chain extender content can be enhancing the hard segment length in PUR structure and affecting both soft segment motion and hard segment motion. Increasing hard segment length might be obstructing soft segment motion and influence hard segment motion which is hard to move at low temperatures. Phase separation of soft and hard segment clearly observed using the DMA technique.