宏观均相多孔电极电化学阻抗谱基础

电化学阻抗谱可用于诊断多孔电极内电荷转移反应,即界面电荷集聚和电荷传导,以及反应物质输运。本文采用复相量方法,在同态假设条件下,重新推演多孔电极阻抗谱模型,厘清传统多孔电极阻抗谱模型中的模糊性表述。(1) 定义多孔电极表征输入参数,包括电极基体电子电导率σ₁ 、电解质离子电导率σ₂、界面电荷传递电导率g_ct、单位面积界面电容C、固相扩散系数D、速度常数k、电极厚度d、特征孔深L_p 和单位体积表面积S_c;(2) 解析阻抗谱特征输出参数,包括场扩散常数K,特征频率ω₀、ω₁、ω₂、ω₃和 ω_max,它们分别相关于界面传导反应、有限场扩散、氧化还原反应、孔内扩散和最小特征孔尺寸,以及分别对应于从传导到扩散和从扩散到饱和的转折频率f_k1 和f_k2;(3) 当参数X和Z同时变化时(X = σ₁和Z = d,S_c,L_p,C,g_ct,D,k),通过阻抗谱特征参数的演变规律,分析了电荷转移反应中X和Ζ参数耦合竞争;(4)为深入分析电荷转移反应中参数X和Z的耦合竞争,引入了分叉频率f_XZ和f_ZX 。f_XZ和f_ZX所处位置可以用于表征参数X和Z影响电荷转移反应的深度和广度。当分叉频率f_XZ和f_ZX不存在时,表明电荷转移反应中参数X和Z在全频率范围内存在耦合竞争。总之,借助于特征频率和分叉频率,本文一方面研究了动力学参数和微观结构参数对多孔电极中电荷转移反应的影响,另一方面分析谱图的变化及其背后的阻抗谱特征演化规律。本文研究结果可为阻抗谱的系统仿真和辨识提供理论基础,可为多孔电极内电荷转移反应的竞争分析提供技术支撑,还可为电化学储能系统的优化设计提供诊断工具。     

Gemini表面活性剂/C12En混合体系的界面吸附、扩张粘弹与泡沫稳定性

用表面张力法研究了阳离子gemini表面活性剂乙基-1, 2-双(十二烷基二甲基溴化铵)(简写为12-2-12)和非离子表面活性剂十二烷基聚氧乙烯醚(C₁₂E_n,其中n = 4, 10, 23)混合体系在气液界面上的吸附行为;用扩张流变技术研究了吸附膜的扩张粘弹行为,实验数据用Lucassen-van den Tempel (LVT)模型进行拟合并根据模型得到了极限弹性值.最后研究了混合体系的泡沫行为,用泡沫塌陷到初始高度一半所对应的时间(t_1/2)来表征泡沫的稳定性.结果表明,所有的非离子表面活性剂C₁₂E_n均与12-2-12产生了吸引作用.在12-2-12浓度相同的情况下,混合吸附层中吸附分子的最小分子占据面积的顺序为12-2-12/C₁₂E₂₃ > 12-2-12/C₁₂E₁₀ > 12-2-12/C₁₂E₄,而极限弹性的顺序为ε_{0, fit}(12-2-12/C₁₂E₄) > ε_{0, fit}(12-2-12/C₁₂E₁₀) > ε_{0, fit}(12-2-12/C₁₂E₂₃).与单组分12-2-12形成的吸附膜相比,只有12-2-12/C₁₂E₄形成更加紧密的结构.具有较小亲水头基的非离子表面活性剂C₁₂E₄的加入,可增强12-2-12吸附膜的弹性,进而增强了对应体系泡沫的稳定性.     

碱土金属Ben (n=1~3)对B12团簇结构的调控研究

基于第一性原理, 系统地研究了Be_n (n=1~3)对B₁₂团簇结构的调控. 结果表明: 团簇BeB₁₂全局极小结构为C_s对称性准平面结构, 而Be₂B₁₂和Be₃B₁₂最稳定的结构均为笼状结构, 对称性分别为C_s和C_2v. 随着Be_n (n=1~3)原子数的增加, 团簇B₁₂由准平面结构过渡到笼状结构, 且Be倾向内嵌在B₁₂笼状结构表面的B₇或B₈单元环中, 通过离子和共价作用形成稳定Be&B₇和Be&B₈单元, 从而稳定笼状结构. 自然键轨道(NBO)分析表明, 团簇C_s BeB₁₂, C_s Be₂B₁₂, C_2v Be₃B₁₂内部存在电子转移情况, Be原子2s轨道上失去电子, Be—B键主要以离子作用为主, 同时也存在共价作用. 成键分析显示C_s Be₂B₁₂和C_2v Be₃B₁₂的π键遵循球状芳香性2(n+1)² (n=1)电子计数规则, 表明该团簇具有球状芳香性. 预测了三个结构的红外和拉曼光谱, 为以后的合成实验和数据表征提供了理论基础.     

CeO2负载的PdO与Ce1‒x Pd x O2‒δ 物种的甲烷催化燃烧性能

通过调控Pd前驱物在CeO₂上的沉积方式, 分别制备了以PdO和离子态的Ce_1?x Pd _x O_2?δ 物种为主的 Pd/CeO₂催化剂, 并采用X射线光电子能谱(XPS)和拉曼(Raman)光谱确证了这两种Pd物种的存在. 氧气程序升温脱附(O₂-TPD)和氢气程序升温还原(H₂-TPR)的表征结果显示, 相比于与载体相互作用较弱的PdO物种, 与CeO₂相互作用较强的Ce_1?x Pd _x O_2?δ 物种具有更加稳定的Pd—O键. 催化剂的甲烷燃烧反应起燃活性测试结果显示, 以PdO物种为主的催化剂表现出了良好的低温催化性能, 在原料气配比为1%CH₄/4%O₂-Ar, 空速为60000 mL·{\mathrm{g}}_{\mathrm{c}\mathrm{a}\mathrm{t}}^{-\mathrm{1}}·h^?1的条件下, T₁₀和T₉₀分别为275和367 ℃, 而两种以Ce_1?x Pd _x O_2?δ 物种为主的催化剂的T₁₀均超过420 ℃. 催化剂的甲烷程序升温还原(CH₄-TPR)表征结果表明, 在升温过程中只有当PdO或Ce_1?x Pd _x O_2?δ 物种被CH₄还原后, 催化活性才开始上升. 由于PdO物种的Pd—O键强度较弱, 有利于Pd物种上的晶格氧在较低温度下参与CH₄的氧化过程. 而Ce_1?x Pd _x O_2?δ 物种的Pd—O键较稳定, 且在反应条件下离子态Pd²⁺与反应体系中氧物种的作用较强, 进而抑制了其与CH₄的反应, 因此反应的起燃温度较高. 以γ-Al₂O₃为载体采用相同的方法制备了Pd/γ-Al₂O₃催化剂, 相关的表征结果进一步证实, 与载体相互作用较弱的PdO物种更容易被CH₄还原, 进而具有较高的催化活性. 据此可以认为Pd/CeO₂上氧化态的Pd物种被CH₄的还原性能是决定其甲烷催化燃烧反应活性的重要因素之一.     

(2-羧基苯氧基)苯-1,2-二羧酸构筑的镧系配合物对苯甲醛和阳离子的荧光传感

采用水热法合成了5个稀土配合物[Sm₂(bdbc)₂(phen)₄](1)和[Ln(bdbc)(phen)(H₂O)][Ln=Eu(2), Gd(3), Tb(4), Dy(5), bdbc=(2-羧基苯氧基)苯-1,2-二羧酸根, phen=1,10-邻菲啰啉]. 配合物1是双核分子, 通过氢键和C—H…π作用进一步构筑成一维超分子结构; 配合物2~5是同构的一维双螺旋结构, 通过氢键和C—H…π作用进一步构筑成三维超分子结构. 配合物1, 2, 4和5呈现了Sm³⁺, Eu³⁺, Tb³⁺和Dy³⁺离子的特征发射, 分别对应于Sm³⁺离子的⁴G_5/2→⁶H_J/2(J=5, 7, 9)、 Eu³⁺离子的⁵D₀→⁷F_J(J=1—4)、 Tb³⁺离子的⁵D₄→⁷F_J(J=6, 5, 4, 3)和Dy³⁺离子的⁴F_5/2→⁶H_J/2(J=15, 13)跃迁. 对配合物4的荧光性质进行了表征, 结果表明, 配合物4可用作荧光探针以检测阳离子和苯甲醛.     

用量子化学参数研究烯烃聚合物定量构效关系

以密度泛函理论(DFT)方法所得的烯烃聚合物结构单元的物性参数如总能量E_t、内能E_in、等容比热C_V、熵S、四极矩Q_ii、偶极矩 µ、平均极化率α及原子最大负电荷q^－等8个量子化学参数, 用逐步回归法分别建立了这些参数与摩尔体积V_{298 K}, 摩尔等张体积P_s、摩尔吸收常数色散分量F_d、摩尔折射率R_LL、摩尔抗磁磁化率χ、摩尔粘度温度函数H_vsum、摩尔Rao函数U_R及摩尔Hartmann函数U_H的结构-性能定量关系 (QSPR) 模型, 其测试集的决定系数R²分别是: V_{298 K} 为0.989, P_s为0.982, F_d为0.975, R_LL为0.997, χ为0.988, H_vsum为0.914, U_R为0.988及U_H为0.972. 结果表明, 用这些量子化学参数所建立的聚合物QSPR模型能用于聚合物性能的预测.     

基于Keggin型杂多酸的无机-有机杂化物的合成和光催化活性

采用水热合成方法制备了2个基于Keggin型杂多酸的无机-有机杂化物, 化学式分别为{[Cu₂(4,4′- bipy)₄(H₂O)₄](SiMo₁₂O₄₀)·18H₂O}_n(1)和{[Cu₂(4,4′-bipy)₄(H₂O)₄](PMo₆W₆O₄₀)·18H₂O}_n(2)(bipy=bipyridine). 结构分析 表明2个化合物同构, Cu²⁺是六配位, 分别与4个4,4′-bipy上的N原子和2个水分子上的O原子结合, 形成 [Cu(4,4′-bipy)₂(H₂O)₂]_n²ⁿ⁺二维层状结构. 杂多阴离子通过静电与配位阳离子[Cu(4,4′-bipy)₂(H₂O)₂]_n²ⁿ⁺作用交叉排列在层间. 通过红外光谱、 粉末X射线衍射和固体紫外-可见漫反射光谱等对化合物的性质进行了表征. 研究了所合成化合物对水溶性染料亚甲基蓝的降解活性, 发现2种化合物对于亚甲基蓝均表现出显著的光降解活性, 并对它们的催化机理进行了讨论.     

蓝光引发丙烯酸水凝胶的聚合交联动力学

研究了聚丙烯酸(PAAc)水凝胶的蓝光聚合性能及实时光流变行为, 并提出了力学性能相关的经验模型. 以樟脑醌/二苯基碘鎓六氟磷酸盐(CQ/DPI)为蓝光引发体系, 丙烯酸(AA)为单体, 聚乙二醇二丙烯酸酯(PEGDA)为交联剂, 450 nm蓝光为辐照光源, 通过光差示扫描量热法(Photo-DSC)和实时光流变法(Photo-rheology)对不同CQ, DPI, AA浓度及光照强度(I)条件下水凝胶聚合前驱液的蓝光聚合性能及交联特性进行了研究. 结果表明, 水凝胶聚合前驱液的聚合速率(R_p)与CQ, DPI和AA的质量分数(w_CQ, w_DPI和w_AA)以及光照强度(I)的平方根均呈线性关系, 由于量子产率的下降及自由体积效应, 在高浓度CQ及DPI条件下, 聚合速率和双键转化率均出现偏离线性的现象. 通过光流变系统对水凝胶前驱液光聚合交联过程中的凝胶特性及交联动力学进行了研究. 经数据拟合发现, 凝胶时间(t_gel)和弹性模量(G')与相关影响因素(w_CQ, w_DPI和w_AA)分别呈现指数和幂律函数关系, 延迟时间(t_d)及交联速率(R_c)与w_CQ, w_DPI, I和w_AA均呈线性函数关系. 根据上述函数关系提出了描述蓝光聚合交联丙烯酸水凝胶力学性能的经验模型.     

荧光粉Ba5-3x/2B4O11∶xEu3+的制备及发光性能

采用高温固相烧结法成功制备了Ba_5-3x/2B₄O₁₁∶xEu³⁺(x=0.02~0.22)荧光粉,利用XRD和SEM等对荧光粉进行了结构和形貌表征。 在激发波长为393 nm的条件下,发射峰(596、621、657和706 nm)与Eu³⁺的⁵D₀-⁷F_J(J=1,2,3,4)电子跃迁相对应,其中621 nm最强发射峰由Eu³⁺离子⁵D₀→⁷F₂电偶极跃迁造成。 文章还研究了Eu³⁺掺杂浓度对Ba_5-3x/2B₄O₁₁∶xEu³⁺发光性能的影响,结果表明,荧光粉的发光强度随着Eu³⁺掺杂量的增加呈现先增大后减小的趋势,Eu³⁺最佳掺杂量为0.16。     

十二烷基聚氧乙烯(n)醚与牛血清白蛋白的团簇化热力学模型

用表面张力和稳态荧光猝灭技术研究非离子表面活性剂十二烷基聚氧乙烯(n)醚(AEO_n)与牛血清白蛋白(BSA)的团簇化体系,根据质量作用定律建立AEO_n与BSA的团簇化热力学模型.从ΔH°>0,ΔS°>0及ΔG°＜0可以推知,AEO_n束缚胶束与BSA形成软物质团簇是熵驱动的超分子自组装过程,其间的超分子作用力以疏水作用为主.团簇化过程的(ΔG°)_clu与表面活性剂自由胶束化过程的(ΔG°)_mic皆小于零,且c₁＜cmc,可以圆满解释在团簇化体系中表面活性剂形成束缚胶束并与大分子经超分子自组装形成软团簇在先,而表面活性剂分子自组装形成自由胶束在后的实验事实.     

Stochastic diffusion interactions and coarsening in a system of droplets growing from a supersaturated gas mixture

In this work we study diffusion interactions among liquid droplets growing in stochastic population by condensation from supersaturated binary gas mixture. During the postnucleation transient regime collective growth of liquid droplets competing for the available water vapor decreases local supersaturation leading to the increase of critical radius and the onset of coarsening process. In coarsening regime the growth of larger droplets is prevailing noticeably broadening the droplet size-distribution function when the condensation process becomes more intensive than the supersaturation yield. Modifications in the kinetic equation are discussed and formulated for a stochastic population of liquid droplets when diffusional interactions among droplets become noteworthy. The kinetic equation for the droplet size-distribution function is solved together with field equations for the mass fraction of disperse liquid phase, mass fraction of water vapor component of moist air, and temperature during diffusion-dominated regime of droplet coarsening. The droplet size and mass distributions are found as functions of the liquid volume fraction, showing considerable broadening of droplet spectra. It is demonstrated that the effect of latent heat of condensation considerably changes coarsening process. The coarsening rate constant, the droplet density (number of droplets per unit volume), the screening length, the mean droplet size, and mass are determined as functions of the temperature, pressure, and liquid volume fraction.     

不同底物体系下漆酶的失活动力学研究

本文对三种体系的漆酶热失活动力学进行了研究,并对动力学参数进行了相应的分析。结果显示,漆酶在纯水溶液中的失活符合一级动力学模型,其失活方程为lnA=-0. 1353t-2. 2522。在有毒有机物体系(2,4-二氯酚和吲哚溶液)中漆酶的失活仍符合一级失活动力学模型,失活速率常数减小,但半衰期增大。在极性溶液(乙醇)中,漆酶的反应速率常数最小,可能是因为漆酶分子内部作用力的变化导致了漆酶反应变缓;在非极性体系(异辛烷溶液)中,水-疏水体系减少了对酶的伤害,利于酶的稳定,延长了漆酶半衰期;极性或非极性体系中的漆酶失活均符合一级动力学失活模型。     

Ligand bonding and dynamics on colloidal nanocrystals at room temperature: the case of alkylamines on CdSe nanocrystals

With CdSe nanocrystals stabilized with very weak ligands (pyridine) as the starting materials, NMR techniques were applied to distinguish the bonded and free alkylamine ligands in an equilibrated adsorption/desorption system for the CdSe-amine nanocrystal-ligand pair. NMR and photoluminescence (PL) measurements were further correlated to identify the linear relationship between PL intensity and the surface ligand coverage of the amine-coated CdSe nanocrystals. For 3.5 nm CdSe nanocrystals and octylamine ligands, the chemical equilibrium constant (K) of the CdSe-amine nanocrystal-ligand adsorption/desorption process was found to be around 50-100, and the corresponding Delta(r)G(o) was calculated as 9.8-11.5 kJ/mol. With a proposed mathematic method, the corresponding chemical kinetic constants for the desorption (kd) and adsorption (ka) processes were measured to be 0.01 s(-1) and 0.5 L mol(-1) s(-1), respectively. K, kd, and ka obtained here are generally 2-4 magnitudes different from those estimated in literature. Analysis indicates that these constants are well consistent with the existing experimental observations.     

Numerical simulation of the chromatographic process for direct ligand-macromolecule binding studies

A numerical simulation of the direct zonal liquid chromatographic method is described for studying the binding of a ligand to a macromolecule by quantification of the interacting species present in a sample at equilibrium. The algorithm accounts for both the kinetic exchanges in solution and the dispersion effects depicted by the Fick law. Dimensionless variables are used for the concentrations which are expressed as a function of the equilibrium constant, KD. The free ligand concentration was varied in the injected samples from 0.1 to 20 KD, while that of the macromolecule was kept constant. An apparent binding isotherm was obtained from the total ligand chromatogram generated by the simulation run, when the amount emerging at almost column dead volume is plotted against that eluting at the free ligand retention time. As a continuous dissociation of the complex may occur during its migration, the apparent binding curve and the theoretical binding isotherm coincide at extremely low dissociating rates. At larger dissociation rates (0.001 s(-1) < kd <0.1 s(-1), for a first peak eluting in 1 min) the simulations were used to test various chromatographic conditions. The flow rate (or column volume) is the major effect which influences the on-column dissociation process as an exponential decay was found when the apparently bound fraction is plotted against the analysis time. The apparent equilibrium coefficient is close to the theoretical one for a binding curve generated with an initial solution containing a relatively low total concentration of binding sites (< or = KD). The apparent stoichiometric term is largely underestimated as its value decreases exponentially at increasing dissociation rates. An extrapolation at extremely short analysis times could be used to determine the stoichiometric coefficient characterizing the binding interaction.     

双金属催化环氧化物聚合动力学研究

研究了双金属氰化络合催化剂DMC催化环氧丙烷聚合的动力学 .用测定反应过程体系压力变化来决定聚合的起始速率 ,发现聚合反应速率正比于催化剂用量C ,单体浓度M的平方 .该实验规律可以从单体参与链引发的动力学特点解释 .考察了温度对聚合反应速率的影响并求得了表观活化能为 5 9 1kJ·mol- 1 ,该值与环氧聚合的卟啉铝、稀土络合物等催化体系接近 .     

Kinetics of Na+-dependent D-glucose transport

The kinetic parameters of the Na+-dependent glucose transport system have been determined in isolated membrane vesicles for D-glucose, Na+, and phlorhizin. The D-glucose flux measurements were carried out by the equilibrium exchange procedure at constant external and internal Na+ concentrations and zero potential. Equations were developed to extract information about Km and Vmax from uptake measurements into a vesicle population that is heterogeneous with respect to size (surface to volume ratio). The Km for D-glucose was 14 mM and independent of the Na+-concentration, while the Vmax was strongly Na+-dependent and increased 15-fold between 1 and 100 mM Na+. The Km of Na+ for activation of the Vmax was 18 mM. The calculated KI values for phlorhizin were 2.7 and 1.9 micrometer when determined under active and equilibrating D-glucose flux conditions, respectively.     

负离子引发丙烯腈沉淀聚合动力学研究

从负离子引发丙烯腈沉淀聚合的亚微观过程出发,建立了动力学模型,并通过初生态沉淀聚集体联结方法数的叠加,推导出了动力学方程.在不同条件下(单体浓度、引发剂浓度、时间)对丙烯腈沉淀聚合进行了研究,用推导的动力学方程处理数据后发现实验数据与理论相吻合.丙烯腈负离子沉淀聚合的聚合反应为对单体浓度的一级反应,对引发剂浓度的一级反应,反应速率方程为Rp=k0[M]1.0[I]1.0.     

Kinetic substrate quantification by fitting the enzyme reaction curve to the integrated Michaelis–Menten equation

The reliability of kinetic substrate quantification by nonlinear fitting of the enzyme reaction curve to the integrated Michaelis-Menten equation was investigated by both simulation and preliminary experimentation. For simulation, product absorptivity epsilon was 3.00 mmol(-1) L cm(-1) and K(m) was 0.10 mmol L(-1), and uniform absorbance error sigma was randomly inserted into the error-free reaction curve of product absorbance A(i) versus reaction time t(i) calculated according to the integrated Michaelis-Menten equation. The experimental reaction curve of arylesterase acting on phenyl acetate was monitored by phenol absorbance at 270 nm. Maximal product absorbance A(m) was predicted by nonlinear fitting of the reaction curve to Eq. (1) with K(m) as constant. There were unique A(m) for best fitting of both the simulated and experimental reaction curves. Neither the error in reaction origin nor the variation of enzyme activity changed the background-corrected value of A(m). But the range of data under analysis, the background absorbance, and absorbance error sigma had an effect. By simulation, A(m) from 0.150 to 3.600 was predicted with reliability and linear response to substrate concentration when there was 80% consumption of substrate at sigma of 0.001. Restriction of absorbance to 0.700 enabled A(m) up to 1.800 to be predicted at sigma of 0.001. Detection limit reached A(m) of 0.090 at sigma of 0.001. By experimentation, the reproducibility was 4.6% at substrate concentration twice the K(m), and A(m) linearly responded to phenyl acetate with consistent absorptivity for phenol, and upper limit about twice the maximum of experimental absorbance. These results supported the reliability of this new kinetic method for enzymatic analysis with enhanced upper limit and precision.     

单一非离子表面活性剂制备胶质气体泡沫的稳定性

用单一的十二烷基醇聚氧乙烯醚(C12EOn)非离子表面活性剂制备了稳定的胶质气体泡沫(CGA). 采用偏光显微镜和流变仪对其表面活性剂溶液相态和泡沫体系的微观结构及流变行为进行研究, 以探索CGA的稳定化机理. 实验结果表明, 分别由C12EO3和C12EO5制备的CGA分散体系中均存在层状液晶相, 层状液晶吸附在气泡的界面上. CGA稳定性可达20 h以上, 没有明显的相分离发生. 而分别由C12EO7和C12EO9制备的CGA呈现由胶束组成的连续相, 不存在液晶相结构, 因而其稳定性较差, 仅能维持数分钟. 实验结果表明, 层状液晶相结构可以显著提高CGA的稳定性. 其稳定作用的机理是通过影响泡沫排液过程, 增强Gibbs-Marangoni效应, 从而提高气泡液膜强度和减缓气相扩散速率.     

A simplified method to estimate kinetic and thermodynamic parameters on the solid-liquid separation of pollutants

The aim of the present study was to propose a simplified experimental-theoretical method for estimating the kinetic and thermodynamic parameters for the solid-liquid separation of pollutants by using kinetic studies with batch reactors, i.e., the removed quantity of dissolved ion as a function of time at different initial concentration. This method was applied to the removal of uranyl ion (UO(2+)(2)) from aqueous solutions onto synthetic manganese oxide (birnessite). The pseudo-second-order kinetics and one-site saturation models were proposed to fit the experimental and calculated data, the fitting parameters being estimated by nonlinear regression, using the least-squares method. For initial concentration range 0.2-11.8 microM, the results showed that the uranyl removal process in dispersed batch reactors can be efficiently modeled by the proposed models. Then, several kinetic and thermodynamic parameters were calculated, such as maximal removed quantity of uranyl, q(r,max), half-removal time, t(1/2), initial rate of uranyl-ion removal, v(0), initial uranyl-removal coefficient, K, maximal rate of uranyl removal, v(0,max), mass transfer coefficient, D(transfer), equilibrium Langmuir constant, K(L), and constant separation factor, K(s). These parameters make it possible to demonstrate that the removal of U onto birnessite is favorable, and that the maximum surface coverage of the uranyl ions represents about 3% of vacant sites in the Mn layer.