一组新的光学活性脂肪族β—氨基醇的合成

手性恶唑硼烷催化的前手性酮对映选择性硼烷还原已成为我学活性二级醇的最重要方法之一。此类催化剂可由相应的手性氨基醇得到。为研究这类催化剂结构与性能的关系，我们设计合成了一组新的光学活性脂肪族β－氨基醇。这些氨基醇的结构特点是分子中有一个叔丁基通过若干个亚甲基构成的不同长度“臂”连在手性碳上，本文报道这些氨基醇的合成。     

影响硼烷对酮不对称还原对映选择性的因素研究

手性邻氨基醇催化的硼烷对酮的不对称还原是制备手性二级醇的重要方法之一,特别是Corey等发展的(S)-α,α-二苯基脯氨醇为非常有效的手性配体,也得到了广泛的应用,然而,研究表明,该反应的对映选择性受多种因素,如硼烷的用量、温度、溶剂、底物酮中的杂原子等的影响.最近我们系统研究了在该还原体系中影响产物对映选择性的因素,找到了适合不同类型催化剂和底物酮的最佳还原条件.结果表明催化剂和底物酮中的杂原子、底物酮中的电子效应、还原体系中的阴离子等对还原产物的对映选择性均有明显的影响,其中底物酮的电子效应的影响符合Hammett线性自由能.通过该研究,不仅提高了对该反应的认识,也可以为其他不对称催化反应条件的优化提供借鉴.     

艾拉莫德关键中间体的合成工艺改进

以3-硝基-4-苯氧基苯甲醚(2)为起始原料,甲酸铵为氢源,氢氧化钯碳为催化剂,经还原反应得到3-氨基-4-苯氧基苯甲醚(3),再经过甲磺酰化反应得到3-甲基磺酰氨基-4-苯氧基苯甲醚(4),最后通过盖特曼-科赫反应得到2-氨基-1-(2-甲氧基-4-甲磺酰胺基-5-苯氧基苯基)乙酮盐酸盐(1).目标产物结构均经1H-...     

用芹菜茎生物催化对映选择性还原芳香酮

研究了用芹菜茎薄片在温和与环境友好的条件下催化芳香酮的对映选择性还原反应.制备得到具有光学活性的(S)-1-芳基醇,产物的对映选择性符合Prelog规则.考察了pH值、反应时间、反应温度、底物浓度等因素对底物芳香酮的转化率和产物(S)-1-芳基醇的对映体过量值的影响,并优化了这些反应条件.文中还研究了底物的构效关系,发现羰基两边取代基的空间效应和电子效应明显影响底物的转化率和产物的对映体过量值.在合适的条件下底物苯乙酮的转化率高达100%,产物(S)-1-苯基乙醇的对映体过量值大于99.0%.苯丙酮、对甲基苯乙酮和对氯苯乙酮等其它芳香酮的转化率达到中等程度,但所得(S)-1.芳基醇的最大对映体过量值均大于99.0%.     

3-氨基-2-吲哚酮合成方法的改进

以苯胺为原料,通过传统方法合成靛红,靛红与盐酸羟胺反应生成3-羟基亚氨基-2-吲哚酮,再通过钯碳加氢还原生成3-氨基-2-吲哚酮。合成中,采用钯碳加氢的还原方式,产物收率提高(收率82.76%,较文献提高了11.8%),后处理更简单。该方法可操作性高、成本低、产生三废少,是一条适合大规模生产3-氨基-2-吲哚酮的新合成工艺路线。     

用芹菜茎催化对映选择性还原芳香酮

研究了用芹菜茎薄片在温和与环境友好的条件下催化芳香酮的对映选择性还原反应, 制备得到具有光学活性的(S)-1-芳基醇, 产物的对映选择性符合Prelog规则. 考察了pH值、反应时间、反应温度、底物浓度等因素对底物芳香酮的转化率和产物(S)-1-芳基醇的对映体过量值的影响, 并优化了这些反应条件. 文中还研究了底物的构效关系, 发现羰基两边取代基的空间效应和电子效应明显影响底物的转化率和产物的对映体过量值. 在合适的条件下底物苯乙酮的转化率高达100%, 产物(S)-1-苯基乙醇的对映体过量值大于99.0%. 苯丙酮、对甲基苯乙酮和对氯苯乙酮等其它芳香酮的转化率达到中等程度, 但所得(S)-1-芳基醇的最大对映体过量值均大于99.0%.     

二氧化硅负载聚（丙烯腈—乙烯基三乙氧基硅）钯（Ⅱ）络合物对羰基氢化还…

二氧化硅负载聚（丙烯腈－乙烯基三乙氧基硅）钯（Ⅱ）络合物在温和条件下能将醛酮中羰基高转化率的催化氢化还原成甲基或亚甲基，考察了Ｎ／Ｐｄ对比，反应温度，底物浓度和催化剂用量与起始吸氢速度的关系。     

3-氨基-2-吲哚酮的新合成方法

以苯胺为原料,通过传统方法合成靛红。靛红与盐酸羟胺反应生成3-羟基亚氨基-2-吲哚酮,再通过钯碳加氢还原生成3-氨基-2-吲哚酮。合成中,采用钯碳加氢的还原方式,产物收率提高（收率82.76%,较文献提高了11.8%）,后处理更简单,而且该方法可操作性高,成本低,产生三废少,是一条适合大规模生产3-氨基-2-吲哚酮的新合成工艺路线。     

芳香甲基酮sp~3C-H活化和二聚偶联合成(E)-1,4-二酮

通过芳香甲基酮的sp~3C-H活化和二聚偶联有效地合成了(E)-1,4-二酮。在DMF中用醋酸钯作催化剂,溴化铜为氧化剂,该反应具有广泛的底物范围。     

钯催化烯基苯并噁嗪酮基于内球型机理的线性和不对称烯丙基烷基化反应

烯基苯并噁嗪酮作为底物参与反应受到有机合成工作者的广泛关注.在过渡金属催化作用下,烯基苯并噁嗪酮脱除一分子二氧化碳,生成的两性离子中间体既可以被亲核试剂进攻,得到结构丰富的芳香胺,也可以作为1,4-偶极子与硫叶立德,缺电子烯烃或α,β-不饱和醛参与成环,分别生成相应的五元、六元或七元含氮杂环.后者广泛存在于农药、医药和生物活性分子中.已报道的钯催化烯基苯并噁嗪酮的不对称转化反应中,支链结构是主产物,线性结构产物比较少见.这是因为烯丙基邻位的氨基负离子与亲核试剂存在氢键或者静电作用,诱导亲核试剂进攻位阻更大但是能量更低的苄位.不同于传统的钯催化烯丙基取代反应,产物的结构通常是由亲核试剂的软硬程度决定.除了化学选择性的问题,产物中双键的Z/E构型和立体选择性的控制也同样成为挑战.近期Li课题组(Org.Lett.,2016,18,4392–4395)基于定位基辅助的Rh(Ⅲ)催化C?H活化策略实现了芳烃烯丙基化得到线性产物.Shi课题组(Chem.Commun.,2019,55,1283–1286)利用Ir(Ⅰ)和Br?nsted酸协同催化实现了吖内酯进攻端位烯丙基.但是,这些反应仅能得到消旋产物.发展不对称的线性烯丙基取代反应,不仅可以拓展烯基苯并噁嗪酮的应用前景,还可以合成具有手性的邻乙烯基芳香胺.本文采用α-硫氰基取代的茚酮作亲核试剂,不同于以往文献报道的机理,氨基负离子对烯醇式茚酮没有起到导向作用,意外得到以直链为主的产物.经过优化,最终以联萘二酚骨架亚膦酰胺为配体,钯作为催化剂,成功构建了一系列与硫氰基直接相连的季碳手性产物.所有反应产物均有优秀的化学选择性(线性选择性>20/1),E/Z选择性(>20/1)和立体选择性(最高95%ee).并且该反应适用范围广泛,基团的兼容性良好.为解释实验结果,本文进行相关的控制实验和DFT计算.计算结果表明,由于氨基负离子碱性较强,茚酮α位C?H酸性较强,直接发生了质子转移生成茚酮烯醇负离子,此时氢键作用消失不能起到导向作用.本文还考察了茚酮烯醇负离子与烯丙基钯通过静电作用形成离子复合物.与之前文献报道不同,本文采用了单齿膦配体且钯与配体等量,这意味着钯处于配位不饱和状态,导致离子复合物极其不稳定,烯醇负离子与硫氰基直接与钯配位成键,该过程结合能高达23.47 kcal/mol.最终配合物中间体通过内球型机理,经历环状过渡态得到以线性为主的产物.     

Highly chemoselective hydrogenation with retention of the epoxide function using a heterogeneous Pd/C-ethylenediamine catalyst and THF

In general, palladium-carbon (Pd/C) catalyzed hydrogenation of epoxides affords the corresponding primary and secondary alcohols as a mixture. It has been found that the catalytic activity of a Pd/C -ethylenediamine complex catalyst [Pd/C(en)] in the hydrogenolysis of epoxide functions is drastically reduced. Herein we describe a mild and chemoselective method for the hydrogenation of olefin, nitro, and azide functions with retention of the epoxide function. The chemoselectivity was accomplished by using a combination of 5% Pd/C(en) and THF as solvent. A significant drop in the chemoselectivity of the hydrogenation is observed with 5% Pd/C(en) in MeOH. These results reinforce the utility of epoxides as important precursors of alcohols in synthetic chemistry.     

Selective Hydrogenation of Aromatic Aminoketones by Pd/C Catalysis

We report an alternative hydrogenation of aromatic aminoketones by heterogeneous catalyst of palladium on carbon (Pd/C) in which nitro, in particular carbonyl groups in the ketones, could be selectively transformed to corresponding amino ketone, secondary alcohol, or methylene compound.     

The Stereochemistry of the Reduction of Cyclic Enaminones

Summary.  The stereo- and regiochemistry of di-, tri-, and tetracyclic enaminones upon catalytic hydrogenation on Pd and Pt catalysts seems to be mainly a function of the catalyst and the medium. The highest stereoselectivity was observed for multiflorine on Pd/C in which 99% of equatorial alcohol were formed in this case, the formation of alcohols proceeds via a ketonic intermediate. On platinum, irrespective of the solvent used (EtOH, H₂O, AcOH, HCl), the hydrogenation reaction proceeds through ketonic (piperidone system) and dehydro (pyridone system) intermediates. In EtOH or H₂O solution, the dehydro product remains unchanged, whereas the ketonic intermediate is reduced to a mixture of epimeric alcohols. In HCl and acetic acid, both intermediates are hydrogenolyzed to a product with a methylene group, but the ketonic one is additionally reduced to a mixture of epimeric alcohols. Reductions with complex metal hydrides provide mixtures of epimeric alcohols with a predominance of equatorial orientation. The structures of products were determined by NMR spectroscopy and/or by GC-MS analysis. Received December 28, 2000. Accepted (revised) February 16, 2001     

贵金属催化p-叔丁基-α-甲基肉桂醛加氢

采用傅里叶变换红外光谱仪(FT-IR)、N₂吸脱附、X射线衍射(XRD)、透射电子显微镜(TEM)揭示了微波辅助-KOH处理对活性炭的物理化学性能的影响规律。 结果表明,活性炭表面的含氧基团的种类增加,微孔明显减少,中大孔的比例增大。 通过浸渍-原位还原方法制备了Pt、Pd、Ru、Rh负载微波辅助-KOH处理活性炭催化剂,并对其催化p-叔丁基-α-甲基肉桂醛选择性加氢性能进行了研究。 发现Pt具有优异的C=O加氢选择性,而Pd具有优良的C=C加氢选择性。 进一步研究了Pd-Pt双组分催化剂催化p-叔丁基-α-甲基肉桂醛加氢产物分布,随着Pt含量的增加, C=O选择性逐步提高, C=C选择性逐渐下降,且当m(Pd)∶m(Pt)=4∶1时,其催化剂的催化性能最佳。     

硝基芳烃氢化还原反应中高分子负载催化剂的双金属协同效应

制备了聚Ｎ－乙烯基－２－吡咯烷酮ＰＶＰ负载钯催化剂Ｐｄ／ＰＶＰ及各种双金属催化剂（１－ｍ）Ｐｄ－ｍＭ／ＰＶＰ，并用于硝基芳烃的加氢还原中，其中Ｐｄ／ＰＶＰ中加入Ｈ２ＰｔＣｌ６的效果最佳，碱的用量、溶剂和Ｐｄ、Ｐｔ的比例都对催化剂的活性有明显的影响，双金属催化剂０．８０Ｐｄ－０．２０Ｐｔ／ＰＶＰ在温和条件下能高活性，高选择性地催化硝基芳烃还原，得到相应的芳胺。     

Synthesis,characterization, and application of hollow ceramic microsphere based Pd catalyst for hydrogenation of 2-ethylanthraquinone

Palladium metal has been used extensively in the hydrogenation reactions due to their great affinity towards hydrogen atoms. In the present study, the catalyst preparation attempted with Pd supported Hollow Ceramic Microspheres using wet impregnation method and its use as catalysts is explored in the hydrogenation of 2-ethylanthraquinone studing the effect of the reaction time, temperature, volume of working solution and the catalyst dosages on the conversion of 2-ethylanthraquinone and yield of hydrogen peroxide. The hydrogenation reaction of 2-ethylanthraquinone is the key step in the anthraquinone method for the industrial production of the hydrogen peroxide. The Pd supported catalyst was characterized by XRF, FTIR, and BET to confirm the composition of the prepared catalyst, Pd deposition, and the surface area. The highest catalyst activity was found to be 9.42 ​g/L with the maximum conversion of 96% at 70°C, 0.3 ​MPa. The kinetics of the heterogeneous hydrogenation reaction of 2-ethylanthraquinone with Pd supported on Hollow Ceramic Microspheres as catalyst was also investigated. This paper is in contribution of our earlier publication.     

Hydrogenation of unsaturated compounds in the presence of palladium-containing modified carbon nanofibers

Palladium-containing carboxylated carbon nanofibers were studied as catalysts for hydrogenation of double bond >C=C< in olefins, unsaturated alcohols, and acids, as well as for hydrogenation of nitroarenes. The developed catalyst is 7 times more efficient than the industrial analog (Pd/C).     

Pd/Fe3O4-C催化剂对甲醇、乙醇和丙醇氧化的电催化活性

制备对醇氧化反应具有优异电活性的钯催化剂是醇燃料电池研究的重要内容。本文用硼氢化钠还原法制备了钯纳米颗粒, 然后沉积在Fe3O4/C复合物表面, 得到了不同Fe₃O₄负载量的Pd/Fe₃O₄-C催化剂. 透射电镜（TEM）图显示钯纳米颗粒均匀地分散在Fe₃O₄/C表面. 对制备好的Pd/Fe₃O₄-C催化剂进行了循环伏安法（CV）、计时电流（CA）和电化学阻抗谱（EIS）的测试, 研究了其在碱性介质中对C1-C3醇类（甲醇、乙醇和丙醇）氧化的电催化活性. 结果表明, 所制备的不同Fe₃O₄负载量的Pd/Fe₃O₄(2%)-C,Pd/Fe₃O₄(5%)-C, Pd/Fe₃O₄(10%)-C和Pd/C催化剂中, Pd/Fe₃O₄(5%)-C催化剂表现出最高的醇氧化电流密度. 依据循环伏安（CV）数据,Pd/Fe₃O₄(5%)-C催化剂对甲醇、乙醇、正丙醇和异丙醇氧化的阳极峰电流密度分别是Pd/C催化剂的1.7、1.4、1.7和1.3倍. Pd/Fe₃O₄(5%)-C催化剂对乙醇氧化的电荷传递电阻也远低于Pd/C催化剂. 制备的所有催化剂对C1-C3醇类电氧化的电流密度大小排序如下: 正丙醇﹥乙醇﹥甲醇﹥异丙醇. 此外, 碳粉中Fe₃O₄纳米颗粒的存在提高了钯纳米颗粒的电化学稳定性.     

Liquid-phase hydrogenation of alkenes and aromatic compounds with Pd-loaded oxidized diamond catalyst

Hydrogenation reactions of alkenes (cyclohexene, ethyl acrylate, styrene and 1,5-cyclooctadiene) and aromatic compounds (o-, m- and p-xylene) were carried out in order to examine the activity of palladium-loaded surface-oxidized diamond (Pd/O-Dia) catalyst in liquid-phase hydrogenation. The catalytic performance was compared to commercial palladium-loaded activated carbon (Pd/C) catalyst. The catalyst activities were evaluated by conversions of reactants and H₂ uptake rates in the early stage of the reaction. In all the hydrogenation reactions of alkenes and aromatic compounds, the activity of Pd/O-Dia was almost the same as or slightly higher than that of Pd/C. Dispersion of Pd metal was measured by a CO-pulsed adsorption technique and TEM observations of the catalysts. Pd dispersions were on the same order of magnitude according to the CO-pulsed adsorption technique, although the Pd/C catalyst had a higher surface area (718 m²/g) than that of Pd/O-Dia (23 m²/g). The Pd particle sizes on O-Dia measured by TEM observation were slightly smaller than those on the activated carbon. Such highly dispersed Pd particles on O-Dia would contribute to higher activity for the hydrogenation reaction of alkenes and aromatic compounds.     

Greener Synthesis of Pristane by Flow Dehydrative Hydrogenation of Allylic Alcohol Using a Packed-Bed Reactor Charged by Pd/C as a Single Catalyst

Our previous work established a continuous-flow synthesis of pristane, which is a saturated branched alkane obtained from a Basking Shark. The dehydration of an allylic alcohol that is the key to a tetraene was carried out using a packed-bed reactor charged by an acid–silica catalyst (HO-SAS) and flow hydrogenation using molecular hydrogen via a Pd/C catalyst followed. The present work relies on the additional propensity of Pd/C to serve as an acid catalyst, which allows us to perform a flow synthesis of pristane from the aforementioned key allylic alcohol in the presence of molecular hydrogen using Pd/C as a single catalyst, which is applied to both dehydration and hydrogenation. The present one-column-two-reaction-flow system could eliminate the use of an acid catalyst such as HO-SAS and lead to a significant simplification of the production process.