流化床煤气化炉内脱硫的研究 Ⅱ．脱硫剂焙烧反应动力学与脱硫反应动力学初步研究

钙质脱硫剂的焙烧反应是炉内脱硫的关键过程，本文研究了影响石灰石和白云石焙烧速率的因素。操作温度７５０℃以上时，焙烧速率很快。ＣＯ_２分压显著地影响焙烧过程，Ｐ_（ＣＯ）２高于平衡分压时，石灰几乎不分解。在本实验的粒度范围内，脱硫剂粒度对焙烧速率影响不大。采用未反应核收缩模型模拟焙烧过程的结果和实验结果基本一致。脱硫反应速率对气相Ｈ_２Ｓ浓度呈一级反应，操作温度特别在６００～７００℃的低温时显著地影响反应速率。     

微波有机合成化学最新进展

从反应装置、合成实例、反应机理以及发展趋势等方面概述了微波技术近年来在有机合成中的应用。参考文献67篇。     

Phebalosin的全合成

以间苯二酚和D,L-苹果酸为原料,经Pechmann反应、Reimer-Tiemann反应、Darzens缩合反应及Wittig反应合成了Phebalosin,总收率1.3%,其结构经~1H NMR和~(13)C NMR表征.     

异腈参与的多组分反应研究进展

多组分反应由于反应本身的经济性和生态价值,越来越受到人们的重视。异腈的亲电和亲核反应均发生在碳原子上,因此在多组分反应中具有重要作用。本文就近年来有异腈参与的多组分反应进行了综述,主要阐述了Ugi反应和Passerini反应及其他含异腈参与的多组分反应的机理、研究开展及应用情况。     

钯催化合成嘧啶核苷衍生物的研究进展

嘧啶核苷衍生物在药物化学、生物探针和核酸化学的研究中具有重要的作用, 金属催化碳碳的形成广泛应用于嘧啶核苷衍生物的合成. 综述了钯催化的Sonogashira反应、Stille反应、Heck反应以及Hiyama反应在嘧啶类核苷衍生物合成中的应用.     

有机反应的竞争性

有机反应的竞争性胡秀贞（南京师范大学化学系，２１００２４）竞争反应是有机化学中一个相当普遍的反应，所以我们研究有机反应机理时，必须具有有关这个反应的热力学和动力学的基本知识。大家知道热力学研究的一个重要内容是反应的起始状态和终止状态的能量变化，而动力...     

Mannich型环肽的液相及固相合成比较

为了改善肽化合物的抗酶解能力，首次介绍了3肽Pro-Pro-Tyr分子的非天然环 化反应，其中分别采用液相及固相两种合成方式组装直链肽，再经过分子内 Mannich缩合，得到以Mannich碱为桥连结构的环肽5（产率5.38%)及10（产率72. 7%)。产物结构经氨基酸组分及质谱分析证明。结果表明，固相法环合可以避免分 子间反应，因此产物收率明显高于液相法。     

Ugi/Diels-Alder串联反应在构建杂环化合物中的应用

杂环化合物广泛存在于天然产物和药物分子中,许多杂环化合物还具有潜在生物活性和药理作用。因此,如何快速高效地构建小分子杂环化合物库成为当今有机合成和药物化学领域的研究热点。Ugi反应在多样性导向合成方面具有得天独厚的优势,能够解决待合成化合物数量庞大、结构复杂的难题;同时,Diels-Alder [4+2]环加成反应能够高效构建碳-碳键,以较高的立体选择性和区域选择性合成六元环系。目前,集二者于一身的Ugi/Diels-Alder串联反应在构建杂环化合物方面展现出了巨大优势和无穷潜能。本文以不同类型的DA反应分类:按照呋喃作为双烯体、吡咯作为双烯体、噻吩为双烯体、口恶唑作为双烯体、 1,2,4-三嗪作为双烯体、苯作为双烯体、不饱和键和芳环共同作为双烯体等对UDA串联反应的研究进行了综述。     

Friedel-Crafts反应的发现史

介绍Ｆｒｉｅｄｅｌ和Ｃｒａｆｔｓ在进行Ｇｕｓｔａｖｓｏｎ反应的实验过程中如何发现了Ｚｉｎｃｋｅ反应的本质,从而创立了以无水三氯化铝等金属卤化物为催化剂的烷基化和酰基化反应。     

低浓度三分子双曲型反应-扩散方程的非线性理论

建立了低浓度三分子模型双曲型反应-扩散的波动方程，研究了定态的稳定性，重点研究了Turing不稳定问题，指出双曲型方程的Turing不稳定不受扩散系数不相等（Dx≠Dy）这一条件的约束，进而对方程作近似的分支分析，讨论了出现极限环的条件，最后对极限环和定态不稳定作了数值研究．     

On the permeation time lag for different transport equations by Frisch method

A constructive application of Frisch method for deriving permeation time lags for different transport equations is shown. Two main classes, i.e. parabolic and hyperbolic diffusional mass transport equations, are presented and compared. An influence of drift and chemical reaction terms on the time lag is discussed.     

Low-dimensional manifolds in reaction-diffusion equations. 1. Fundamental aspects

The approach to equilibrium for systems of reaction-diffusion equations on bounded domains is studied geometrically. It is shown that equilibrium is approached via low-dimensional manifolds in the infinite-dimensional function space for these dissipative, parabolic systems. The fundamental aspects of this process are mapped out in some detail for single species cases and for two-species cases where there is an exact solution. It is shown how the manifolds reduce the dimensionality of the system from infinite dimensions to only a few dimensions.     

Complex wave patterns in an effective reaction-diffusion model for chemical reactions in microemulsions

An effective medium theory is employed to derive a simple qualitative model of a pattern forming chemical reaction in a microemulsion. This spatially heterogeneous system is composed of water nanodroplets randomly distributed in oil. While some steps of the reaction are performed only inside the droplets, the transport through the extended medium occurs by diffusion of intermediate chemical reactants as well as by collisions of the droplets. We start to model the system with heterogeneous reaction-diffusion equations and then derive an equivalent effective spatially homogeneous reaction-diffusion model by using earlier results on homogenization in heterogeneous reaction-diffusion systems [S.Alonso, M.Ba?r, and R.Kapral, J. Chem. Phys. 134, 214102 (2009)]. We study the linear stability of the spatially homogeneous state in the resulting effective model and obtain a phase diagram of pattern formation, that is qualitatively similar to earlier experimental results for the Belousov-Zhabotinsky reaction in an aerosol OT (AOT)-water-in-oil microemulsion [V.K.Vanag and I.R.Epstein, Phys. Rev. Lett. 87, 228301 (2001)]. Moreover, we reproduce many patterns that have been observed in experiments with the Belousov-Zhabotinsky reaction in an AOT oil-in-water microemulsion by direct numerical simulations.     

Locally implicit solution of a reaction-diffusion system with stiff kinetics

The Tyson-Fife reaction-diffusion equations are solved numerically using a locally implicit approach. Since the variables evolve at very different time scales, the resulting system of equations is stiff. The reaction term is responsible for the stiffness and the time step is increased by using an implicit method. The diffusion operator is evaluated explicitly and the system of implicit nonlinear equations is decoupled. The method is particularly useful for parameter values in which the equations are very stiff, such as the values obtained directly from the experimental reaction rate constants. Previous efforts modified the parameters on the equations to avoid stiffness. The equations then become a simplified model of excitable media and, for those cases, the locally implicit method gives a faster although less accurate solution. Nevertheless, since the modified equations no longer represent a particular chemical system an accurate solution is not as important. The algorithm is applied to observe the transition from simple motion to compound motion of a spiral tip.     

Catalytic conversion reactions mediated by single-file diffusion in linear nanopores: hydrodynamic versus stochastic behavior

We analyze the spatiotemporal behavior of species concentrations in a diffusion-mediated conversion reaction which occurs at catalytic sites within linear pores of nanometer diameter. Diffusion within the pores is subject to a strict single-file (no passing) constraint. Both transient and steady-state behavior is precisely characterized by kinetic Monte Carlo simulations of a spatially discrete lattice-gas model for this reaction-diffusion process considering various distributions of catalytic sites. Exact hierarchical master equations can also be developed for this model. Their analysis, after application of mean-field type truncation approximations, produces discrete reaction-diffusion type equations (mf-RDE). For slowly varying concentrations, we further develop coarse-grained continuum hydrodynamic reaction-diffusion equations (h-RDE) incorporating a precise treatment of single-file diffusion in this multispecies system. The h-RDE successfully describe nontrivial aspects of transient behavior, in contrast to the mf-RDE, and also correctly capture unreactive steady-state behavior in the pore interior. However, steady-state reactivity, which is localized near the pore ends when those regions are catalytic, is controlled by fluctuations not incorporated into the hydrodynamic treatment. The mf-RDE partly capture these fluctuation effects, but cannot describe scaling behavior of the reactivity.     

Three-variable reversible Gray-Scott model

Even though the field of nonequilibrium thermodynamics has been popular and its importance has been suggested by Demirel and Sandler [J. Phys. Chem. B 108, 31 (2004)], there are only a few investigations of reaction-diffusion systems from the aspect of thermodynamics. A possible reason is that model equations are complicated and difficult to analyze because the corresponding chemical reactions need to be reversible for thermodynamical calculations. Here, we introduce a simple model for calculation of entropy production rate: a three-variable reversible Gray-Scott model. The rate of entropy production in self-replicating pattern formation is calculated, and the results are compared with those reported based on the Brusselator model in the context of biological cell division.