合成了2种含硅二胺单体3,3'-(1,3-二甲基-1,3-二乙烯基-1,3-二硅氧烷)二苯胺(S1)和4,4'-(1,3-二甲基-1,3-二乙烯基-1,3-二硅氧烷)二苯胺(S2),并对其作为环氧树脂的新型固化剂进行了研究.采用非等温示差扫描量热技术(DSC)研究了其与双酚A型环氧树脂E51体系的固化反应动力学,根据不同升温速率下E51/S1和E51/S2体系的特征温度的变化,分别确定了该两体系的固化反应工艺条件,即:E51/S1体系为100℃/1h+160℃/2h+190℃/3h;E51/S2体系为110℃/1h+170℃/2h+190℃/3h.通过Kissinger方程、Crane方程以及Arrheninus方程对固化反应进行了固化动力学行为研究,得到了两个反应体系的表观活化能ΔE、Arrhenius因子A以及反应级数n等动力学参数.E51/S1体系的ΔE为50.65 k J/mol、A为1.83×105,n为0.87;E51/S2体系的ΔE为51.39 k J/mol,A为1.44×105,n为0.87,由ΔE和A表明,E51和S2的反应活性高于E51和S1的反应活性,即,氨基位于苯环的间位时与环氧基团更容易反应.二者的反应级数相同并且小于1,说明E51与S1和S2之间的反应是复杂反应.在动力学参数的基础上,得到了n级固化动力学模型. 相似文献
Electrochemically initiated polymerization at a planar electrode is treated theoretically and an approximate solution to the full time-dependent problem is found assuming the electrode process to be reversible (so that the Nernst relation holds). The homogeneous kinetics lead to a second-order coupled non-linear initial-boundary value problem, and the method developed for its solution is general and applicable to other problems. The approximate solution is converted to an equation for the transient current-versus-time curve, for electrode initiated polymerization, which can be used for the experimental determination of the polymerization and termination rate constants. An analysis procedure for such determination is outlined. 相似文献
Expressions for the transient current at the downstream electrode in response to galvanostatic electrolysis at the upstream electrode in the channel flow cell were derived by applying double Laplace transformation when the electrode reaction at the upstream electrode is kinetically controlled. The ratio of the transient current to the steady state current or the transient collection efficiency was calculated as a function of electrode geometry and θ , where Um is the mean flow velocity in the channel cell, D the diffusion coefficient of the electroactive species, b the half height of the channel, x1 the length of the upstream electrode and t the time elapsed since the beginning of the galvanostatic electrolysis at the upstream electrode. Curves for the transient collection efficiency can be applied to evaluating the amount of adsorption at the upstream electrode when metal at the electrode is anodically dissolved in solution. Digital simulation was carried out. Transient curves, obtained analytically, were in good agreement with those evaluated from the digital simulation. In order to allow one to draw transient curves readily, we derived a simple approximate equation. 相似文献
The pulsed galvanostatic method of studying corrosion processes is applied together with the pulsed galvanostatic method of measuring the electrode capacitance, which makes it possible to more rigorously determine the number of components of an equivalent circuit for the electrode. In order to recognize the processes characterized by small time constants, it is advisable to take one more measurement with a polarizing-current pulse whose magnitude is several times greater but the length is shorter. The time interval for calculating still next RC circuit must be selected so that the residual transient, obtained after subtracting the contribution made by this circuit, should have a horizontal portion in the time interval from RC to 3RC. Parameters of the assumed last RC circuit can be calculated in a roundabout way, from the electrode capacitance measured by a pulsed method. It is established that, with an anodic measuring pulse, an equivalent circuit for an Ni electrode in 1 N H2SO4 comprises two RC circuits; for a Cu electrode in 1 N NaCl, a Warburg circuit and two RC circuits; and for an Ni electrode in 1 N NaCl, a Warburg circuit and four RC circuits. 相似文献
A single-line flow-injection system with a straight tube reactor is proposed for investigating the dynamic response behaviour of ion-selective electrodes. The principle of the method is based on the fact that the concentration—time curve at the electrode surface can be described theoretically in the flow-injection system under certain practically realizable conditions. The response of the ion-selective electrode to that input signal can be measured experimentally. Thus, knowing the input and the output signal of an ion-selective electrode, an appropriate model describing its dynamic behaviour can be selected among the relevant models existing in the literature. Theoretical expressions for predicting the transient response of ion-selective electrodes in the flow system when the rate-determining step is an ion-transport process through a diffusion layer or a kinetic process were elaborated. 相似文献
The extraction of electrode kinetic parameters for electrochemical couples in room-temperature ionic liquids (RTILs) is currently an area of considerable interest. Electrochemists typically measure electrode kinetics in the limits of either transient planar or steady-state convergent diffusion for which the voltammetric response is well understood. In this paper we develop a general method allowing the extraction of this kinetic data in the region where the diffusion is intermediate between the planar and convergent limits, such as is often encountered in RTILs using microelectrode voltammetry. A general working surface is derived, allowing the inference of Butler-Volmer standard electrochemical rate constants for the peak-to-peak potential separation in a cyclic voltammogram as a function of voltage scan rate. The method is applied to the case of the ferrocene/ferrocenium couple in [C2mim][N(Tf)2] and [C4mim][N(Tf)2]. 相似文献