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。     

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。     

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.     

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。     

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。     

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。     

Unravelling the Enigma of Nonoxidative Conversion of Methane on Iron Single-Atom Catalysts

The direct, nonoxidative conversion of methane on a silica-confined single-atom iron catalyst is a landmark discovery in catalysis, but the proposed gas-phase reaction mechanism is still open to discussion. Here, we report a surface reaction mechanism by computational modeling and simulations. The activation of methane occurs at the single iron site, whereas the dissociated methyl disfavors desorption into gas phase under the reactive conditions. In contrast, the dissociated methyl prefers transferring to adjacent carbon sites of the active center (Fe₁©SiC₂), followed by C−C coupling and hydrogen transfer to produce the main product (ethylene) via a key −CH−CH₂ intermediate. We find a quasi Mars–van Krevelen (quasi-MvK) surface reaction mechanism involving extracting and refilling the surface carbon atoms for the nonoxidative conversion of methane on Fe₁©SiO₂ and this surface process is identified to be more plausible than the alternative gas-phase reaction mechanism.     

添加气对非平衡等离子体转化低碳烷烃的影响

在常压下, 研究了添加气的种类(N₂, He, Ar, H₂, NH₃, CO和CO₂)对介质阻挡放电低碳烷烃(甲烷、 乙烷和丙烷)转化制低碳烯烃的影响. 结果表明, 以甲烷或乙烷为原料时, N₂, He, Ar和CO的引入有利于提高原料的转化率和总烯烃的选择性; 而CO₂, H₂和NH₃的引入对甲烷、 乙烷的转化率无明显影响, 但H₂和NH₃的引入会使总烯烃的选择性显著降低. 以丙烷为原料时, 所研究的添加气均可提高丙烷的转化率, 而只有CO的引入可提高总烯烃选择性. 综上所述, 80%(摩尔分数) CO添加量最有利于低碳烷烃转化成低碳烯烃, 对应的甲烷、 乙烷和丙烷的转化率分别提高了14.4%, 17.6%和42.8%, 总烯烃的选择性分别提高了19.9%, 25.0%和11.9%. 以CH₄为例, 通过对放电电流波形和等离子体区物种的发射光谱(OES)研究发现, 引入CO能显著增加等离子体的电子密度, 并且体系中出现激发态O^*物种(777.5和844.7 nm), 这种O^*物种能够促进C-H键的断裂, 有利于烯烃的生成. 因此, 等离子体区电子密度的增加和激发态O^*物种的出现可能是CH₄-CO体系中CH₄有效转化的主要原因.     

Ni/TiO2 Catalyst for Partial Oxidation of Methane to Syngas

Ni/TiO₂ catalyst was firstly used for the partial oxidation of methane to produce synthesis gas. The reaction was carried out in a fixed-bed continuous flow quartz reactor at atmospheric pressure. The flow rate was regulated by a mass controller with a space velocity of 1.5×10⁵ h^-1 and a CH₄/O₂ molar ratio of 2/1. Prior to the introduction of feed gas, the Ni/TiO₂ catalyst was activated in flowing H₂ at 700℃ for 30 min. TiO₂ is known to be a poor support for partial oxidation because which can easily result in complete oxidation. But at 700℃, Ni/TiO₂ catalyst exhibited a better performance than Ni/SiO₂ and Ni/ZrO₂. The conversion of methane was 81.5, and the selectivity of hydrogen and carbon monoxide were 93.4 and 89.4 respectively. After 6h of continuous reaction, the conversion of methane descended a little and then remained a steady yield on the whole,but the selectivity of H₂ and CO gradually declined, as far as to a constant. The selectivity of H₂ was always higher than that of CO and the ratio of H₂/CO wouldn't change with the increasing of reaction time.     

基于反应力场分子模拟的乙烯燃烧自由基与氮气相互作用研究

采用反应力场分子动力学(ReaxFF-MD)方法, 模拟了富燃料条件下乙烯在空气中的燃烧以及燃烧产生的自由基与氮气的相互作用. 采用ReacNetGenerator程序提取反应网络, 结合自编后处理程序确定反应网络上的相关反应, 分析了乙烯燃烧的反应路径, 以及自由基与N₂的相关反应和NO的生成路径. 结果表明, 乙烯燃烧路径与已报道的通过乙烯燃烧反应机理模拟得到的燃烧路径一致, 说明用ReaxFF-MD方法模拟乙烯高温燃烧有效而可靠; 乙烯在富燃料条件下燃烧产生的CH, C₂H, C₂, C₂O自由基是瞬发型NO生成的重要反应物. 这些自由基与N₂的反应和NO的生成路径, 为构建乙烯和大分子碳氢燃料燃烧氮氧化物排放的反应机理提供了重要参考.     

RCOO-取代的镍(Ⅱ)配合物单组分高效催化乙烯均聚和共聚反应

合成并表征了含RCOO-基团的单核(Ni¹~Ni²)及双核(Ni³)镍配合物[(2,6-R₂-C₆H₃)—N=C(H)—(3-Ph-5-PhCOO-2-O-C₆H₂)-κ²-N,O]Ni(CH₃)(pyridine)](R=iPr;3,5-tBu₂C₆H₃),并用于催化乙烯均聚和共聚反应。 作为单组分催化剂,这些配合物可以有效地催化乙烯聚合得到中等相对分子质量的支化聚乙烯(PE)。 供电性的PhCOO—基团促进了催化剂Ni¹的引发,从而在低温下比Ni⁰活性更高。 引入大位阻的2,6-(3,5-二叔丁基苯基)苯胺基团,催化剂Ni²在5×10⁵ Pa下的活性高达1.8×10⁶ g PE mol^-1·Ni^-1·h^-1,是活性最高的水杨醛亚胺中性镍催化剂之一。 与相应的单核催化剂相比,双核催化剂Ni³对三苯基膦具有更好的耐受性。 这些催化剂可催化乙烯与1,5-己二烯、1,7-辛二烯、6-溴-1-己烯或10-十一烯酸甲酯的共聚合,制备功能化聚乙烯。     

甲烷无氧直接制备芳烃研究进展

甲烷无氧直接制备芳烃和氢气是碳一化学与催化领域中一个极具挑战性的研究课题,具有碳原子利用率高、二氧化碳零排放、工艺流程短和绿色环保等优势,已经成为世界各国研究机构的重要研究方向。本研究基于作者课题组在甲烷无氧芳构化反应的研究工作,结合2013-2017年的相关文献,对目前甲烷无氧芳构化的研究现状进行综合评述。重点讨论甲烷无氧芳构化反应机理与积炭形成、催化剂改性及再生、膜反应器、非钼基催化剂体系等工作,并对甲烷无氧芳构化直接制备芳烃的未来前景进行了展望。     

The multichannel reaction NH2 + NH2 at ambient temperature and low pressures

NH₂ profiles were measured in a discharge flow reactor at ambient temperature by monitoring reactants and products with an electron impact mass spectrometer. At the low pressures used (0.7 and 1.0 mbar) the gas-phase self-reaction is dominated by a ‘bimolecular’ H₂-eliminating exit channel with a rate coefficient of k_3b(300 K) = (1.3 ± 0.5) × 10⁻¹² cm³ molecule⁻¹ s⁻¹ and leading to N₂H₂ + H₂ or NNH₂ + H₂. Although the wall loss for NH₂ radicals is relatively small (k_w ≈ 6–14 s⁻¹), the contribution to the overall NH₂ decay is important due to the relatively slow gas-phase reaction. The heterogeneous reaction yields N₂H₄ molecules.     

Photon-induced unimolecular decay of the benzyl radical: first direct identification of the reaction pathway to C7H6

The thermal unimolecular decay of the benzyl radical has been investigated extensively by several groups. However, the reaction products could not be determined unambiguously. In this work the unimolecular bond fission of the benzyl radical is studied in a molecular beam experiment. The precursor molecules toluene and cycloheptatriene are expanded in a molecular beam and photodissociated with two photons at 248 or 193 nm, yielding in each case hot benzyl radicals. Since the internal energies lie above the dissociation limit, the benzyl radicals decay in a subsequent step. The reaction products are detected in a time-resolved manner with a quadrupole mass spectrometer on the molecular beam axis at low electron energies. The measured time-of-flight spectra provide information on the translational energy distribution of the products. In each case it is found that the hot benzyl radicals C₇H₇ fragment under hydrogen loss to C₇H₆.     

Aromatization of methane by using propane as co-reactant over cobalt and zinc-impregnated HZSM-5 catalysts

The activities of the cobalt and zinc-impregnated HZSM-5 catalysts to the non-oxidative conversion of propane (C3) and methane (C1) into aromatic hydrocarbons were evaluated using a fixed-bed microreactor. C1 conversion reached 36.7% and the selectivity of aromatic products reached above 88.7% at atmospheric pressure, weight (hourly) space velocity (WHSV) 1.6 g h⁻¹/(g cat)⁻¹ and 873 K. The influence of the acidity and the ratio of cobalt in the catalyst on the conversion of methane and propane was evaluated. C1 incorporation was conclusively confirmed by the mass spectral analyses of aromatic products produced in a run with ¹³CH₄ which shows a significant ¹³C enrichment in the C₆H₆⁺, C₇H₈⁺ and C₈H₁₀⁺ fragments. The methane activation could result from its hydrogen-transfer reaction with alkenes. These catalysts were thoroughly characterized using XRD, N₂ adsorption measurements, TPD of NH₃, and FT-IR. The results showed that the activation of methane in low temperature was due to existence of propane. The acidic changes and micropore area of the catalyst severely affected aromatization, and resulted in drastic modifications in product distribution. From this work, we found that only a small fraction of tetrahedral framework aluminum, which corresponds to the Bronsted acid sites, is sufficient to accomplish the aromatization of the intermediates in methane and propane aromatic reaction, while the superfluous strong Bronsted acid sites, which can be decreased by adding Co and Zn, are showed to be related with the aromatic carbonaceous deposits on the catalysts. The density of acidic site and the strength of strong acid decreased when the concentration of Co and Zn in the catalyst increased. Therefore, a much higher benzene yield and a longer durability of the catalysts are obtained when compared with the conventional HZSM-5 catalysts.     

CeO2担载Cu纳米粒子电催化CO2还原产乙烯：CeO2不同暴露晶面对催化性能的影响

Fossil fuels are expected to be the major source of energy for the next few decades. However, combustion of nonrenewable resources leads to the release of large quantities of CO₂, the primary greenhouse gas. Notably, the concentration of CO₂ in the atmosphere is increasing annually at an astounding rate. Electrochemical CO₂ reduction (ECR) to value-added fuels and chemicals using electricity from intermittent renewable energy sources is a carbon-neutral method to alleviate anthropogenic CO₂ emissions. Despite the steady progress in the selective generation of C₁ products (CO and formic acid), the production of multi-carbon species still suffers from low selectivity and efficiency. As an ECR product, ethylene (C₂H₄) has a higher energy density than do C₁ species and is an important industrial feedstock in high demand. However, the conversion of CO₂ to C₂H₄ is plagued by low productivity and large overpotential, in addition to the severe competing hydrogen evolution reaction (HER) during the ECR. To address these issues, the design and development of advanced electrocatalysts are critical. Here, we demonstrate fine-tuning of ECR to C₂H₄ by taking advantage of the prominent interaction of Cu with shape-controlled CeO₂ nanocrystals, that is, cubes, rods, and octahedra predominantly covered with (100), (110), and (111) surfaces, respectively. We found that the selectivity and activity of the ECR depended strongly on the exposed crystal facets of CeO₂. The overall ECR Faradaic efficiency (FE) over Cu/CeO₂(110) (FE ≈ 56.7%) surpassed that of both Cu/CeO₂(100) (FE ≈ 51.5%) and Cu/CeO₂(111) (FE ≈ 48.4%) in 0.1 mol·L^-1 KHCO₃ solutions with an H-type cell. This was in stark contrast to the exclusive occurrence of the HER over pure carbon paper, CeO₂(100), CeO₂(110), and CeO₂(111). In particular, the FE toward C₂H₄ formation and the partial current density increased in the sequence Cu/CeO₂(111) < Cu/CeO₂(100) < Cu/CeO₂(110) within applied bias potentials from -1.00 to -1.15 V (vs. the reversible hydrogen electrode), reaching 39.1% over Cu/CeO₂(110) at a mild overpotential (1.13 V). The corresponding values for Cu/CeO₂(100) and Cu/CeO₂(111) were FE_C2H4 ≈ 31.8% and FE_C2H4 ≈ 29.6%, respectively. The C₂H₄ selectivity was comparable to that of many reported Cu-based electrocatalysts at similar overpotentials. Furthermore, the FE for C₂H₄ remained stable even after 6 h of continuous electrolysis. The superior ECR activity of Cu/CeO₂(110) to yield C₂H₄ was attributed to the metastable (110) surface, which not only promoted the effective adsorption of CO₂ but also remarkably stabilized Cu⁺, thereby boosting the ECR to produce C₂H₄. This work offers an alternative strategy to enhance the ECR efficiency by crystal facet engineering.