2-氟-6-三氟甲基苄胺的合成新方法

以2-甲基-3-三氟甲基苯胺（1）为原料,经Balz-Schiemann反应制得3-氟-2-甲基三氟甲苯（3）;3经溴代制得2-氟-6-三氟甲基苄溴(4）,最后经Gabriel反应合成2-氟-6-三氟甲基苄胺,总收率53.4%,其结构经¹H NMR和MS(ESI)确证。     

2-氰基-2,3-二甲基-3-甲基羰甲基-5-硫酮-吡咯烷的合成

2-氰基-2;3-二甲基-3-甲基羰甲基-5-硫酮-吡咯烷的合成;双甲基环并内酯;双甲基环并内酰胺-内酯;氰基吡咯烷酮;氰基吡咯烷硫酮     

5-甲基-3-硝甲基己酸乙酯的合成

以异戊醛和膦酰乙酸三乙酯为原料,1,8-二氮杂二环［5,4,0］十一碳-7-烯(DBU)为催化剂,碘化钠为磷酸酯碳负离子稳定助剂,经Horner-Wadsworth Emmons反应合成了5-甲基-2-己烯酸乙酯(3),收率90%;仍以DBU为催化剂,3与硝基甲烷经Michael加成反应合成5-甲基-3-硝甲基己酸乙酯,收率98%,两步总收率88.2%,其结构经¹H NMR和IR确证。     

5-二氰亚甲基-4-二环丙亚甲基-3-[1-(2, 5-二甲基-3-呋喃基)亚乙基]四氢呋喃-2-酮的合成

报道俘精酸酐类化合物(E/Z)4-二环丙亚甲基-3-[1-(2, 5-二甲基-3-呋喃基)亚乙基]四氢呋喃-2, 5-酮的拆分, 及(E)和(Z)-5-二氰亚甲基-4-二环丙亚甲基-3-[1-(2, 5-二甲基-3-呋喃基)亚乙基]四氢呋喃-2-酮 4(E)和4(Z)的合成, 并对它们的光致变色特性进行了初步研究。     

4-甲基-4-氮杂-21E-苯亚甲基-5-孕烯-3,20-二酮类化合物的合成

报道了一种以KF/Al_2O_3催化合成4-甲基-4-氮杂-21E-苯亚甲基-5-孕烯-3,20-二酮类化合物的方法。以黄体酮为原料,经NaIO_4/KMnO_4氧化裂解、胺解关环得到重要中间体4-甲基-4-氮杂-5-孕烯-3,20-二酮,后者在KF/Al_2O_3催化下经克莱森缩合得到目标产物。考察了不同的催化剂、反应温度、催化剂用量对目标产物的影响。条件优化的结果为:n(3)∶n(KF/Al_2O_3)=1∶1,回流状态下反应4 h,产率为56%~68%。此方法适用性好,为4-氮杂甾体苯亚甲基衍生物的合成提供了一种方便而有效的方法。     

2甲基-3-羥甲基-5-硝基酚的合成

1.从2一甲基-5-硝基氯化苄(Ⅵ)合成2-甲基-3羟甲基-5-硝基酚(Ⅴ)。此化合物对肉瘤180无抑制作用。 2.以铬酸氧化乙酸(2-甲基-5-硝基)苄酣(Ⅺ)时,得2-甲基-5-硝基苯甲醛(ⅩⅥ)甲基未氧化而取代的甲基氧化为醛基。     

2-甲基-6-(3-甲基-2-丁烯基)对苯二醌的合成

以邻甲基苯酚为原料,与1-氯-2-甲基-2-丁烯反应生成2-甲基-6-(3-甲基-2-丁烯基)苯酚,然后催化氧化得到目标产物2-甲基-6-(3-甲基-2-丁烯基)对苯二醌。该合成路线简单,易于操作,最终收率51%。     

5-二氰亚甲基-4-二环丙亚甲基-3-[1-(2,5-二甲基-3-呋喃基)亚乙基]四氢呋喃-2-酮的合成

报道俘精酸酐类化合物(E/Z)4-二环丙亚甲基-3-[1-(2,5-二甲基-3-呋喃基)亚乙基]四氢呋喃-2,5-酮的拆分,及(E)和(Z)-5-二氰亚甲基-4-二环丙亚甲基-3-[1-(2,5-二甲基-3-呋喃基)亚乙基]四氢呋喃-2-酮4(E)和4(Z)的合成,并对它们的光致变色特性进行了初步研究。     

甲苯、2-甲基噻吩和3-甲基噻吩的化学分离方法研究

报道了一种分离甲苯、2-甲基噻吩和3-甲基噻吩的方法。通过氯化反应将沸点非常接近的甲苯、2-甲基噻吩和3-甲基噻吩转化为沸点相差较大的甲苯(111℃)、2-氯-5-甲基噻吩(155℃)和2,5-二氯-3-甲基噻吩(185℃),通过对比实验获得氯代反应的最佳条件为:2-甲基噻吩和3-甲基噻吩与磺酰氯的投料比1∶1. 75,反应温度65℃,反应时间2 h。通过精馏将三者分离并提纯,得到甲苯、高附加值的2-氯-5-甲基噻吩和2,5-二氯-3-甲基噻吩产品;通过催化还原反应将2-氯-5-甲基噻吩和2,5-二氯-3-甲基噻吩分别还原为2-甲基噻吩和3-甲基噻吩,达到完全分离、提纯的目的。     

Ni/Al2O3催化2-甲基呋喃加氢制2-甲基四氢呋喃性能的研究

采用浸渍法制备了不同NiO含量的Ni/Al₂O₃催化剂,并进行了2-甲基呋喃加氢制2-甲基四氢呋喃性能的考察。结果表明,在制备的NiO负载量为10%、20%、25%、30%和40%的Ni/Al₂O₃催化剂中,随着NiO负载量增加,加氢反应的选择性与2-甲基呋喃的转化率均呈现出先增加后减小的趋势。其原因是由于适当增加NiO负载量有利于催化剂表面活性中心的形成,有利于加氢反应的进行;但是过度负载的NiO容易堵塞Al₂O₃载体中的介孔通道,降低反应的转化率与选择性。在釜式反应器中进行反应,对加氢反应条件进行了优化,发现在反应压力为3 MPa、反应温度150℃、机械搅拌速率为1000 r/min时,Ni/Al₂O₃催化2-甲基呋喃加氢制2-甲基四氢呋喃具有较高的选择性。当NiO负载量为25%时,2-甲基四氢呋喃的选择性最高为97.1%,2-甲基呋喃的转化率达到99.4%。     

Selective Oxidation of CO in Excess H2 over Ru/Al2O3 Catalysts Modified with Metal Oxide

The Ru/Al_2O_3 catalysts modified with metal oxide(K_2O and La_2O_3)were prepared via incipient wetness impregnation method from RuCl_3·nH_2O mixed with nitrate loading on Al_2O3 support. The activity of catalysts was evaluated under simulative conditions for the preferential oxidation of CO (CO-PROX)from the hydrogen-rich gas streams produced by reforming gas,and the performances of catalysts were investigated by XRD and TPR.The results showed that the activity temperature of the modified catalysts Ru-K_2O/Al_2O3 and Ru-La_2O_3/Al_2O_3 were lowered approximately 30℃compared with pure Ru/Al_2O_3,and the activity temperature range was widened.The conversion of CO on Ru-K_2O/Al_2O_3 and Ru-La_2O_3/Al_2O_3 was above 99% at 140-160℃,suitable to remove CO in a hydrogen-rich gas and the selectivity of Ru-La_2O_3/Al_2O_3 was higher than that of Ru-K_2O/Al_2O_3 in the active temperature range. Slight methanation reaction was detected at 220℃and above.     

还原态WO_3/Al_2O_3,NiO/Al_2O_3和NiO-WO_3/Al_2O_3催化剂上H_2,CO,O_2的吸附特性

在加氢精制和许多其它催化过程中,Mo,W是主要的活性组分,Co,Ni通常作为助剂,有关Co-Mo体系的研究文献报导很多~[1.2], 但由于钨较难还原和硫化,关于     

α-Fe_2O_3 immobilized benzimidazolium tribromide as novel magnetically retrievable catalyst for one-pot synthesis of highly functionalized piperidines

Nanostructured α-Fe_2O_3 were prepared by precipitation followed by calcination method.Cetyltrimethylammonium bromide(CTAB) was used as surfactant.The nano α-Fe_2O_3 was then silanized with(3-chloropropyl)-triethoxysilane(CPTES) by room temperature mixing of α-Fe_2O_3 and CPTES to produce silane coated α-Fe_2O_3(ClPr-Si@Fe_2O_3).As-synthesized ClPr-Si@Fe_2O_3 was functionalized via covalent grafting of benzimidazole to produce 3-(l-benzimidazole)Pr-Si@Fe_2O_3.This was further reacted with bromine to afford α-Fe_2O_3 immobilized benzimidazolium tribromide(α-Fe_2O_3-BIM tribromide).This ionic liquid(IL)α-Fe_2O_3 BIM tribromide was characterized by FT-IR,XRD,TEM,SEM,TGA,VSM,EDX and BET analysis.The as-synthesized IL tribromide was used as catalyst for one-pot synthesis of highly substituted piperidines.The method is greener in terms of solvent selection,recovery of the catalyst and efficiency.     

Promotion of hydrocarbon selectivity in CO2 hydrogenation by Ru component

We investigated catalytic behavior of iron in CO₂ hydrogenation with and without a ruthenium component. Calcined iron-based catalysts were reduced by H₂ and characterized by XRD, BET surface area and CO₂, CO and C₂H₄ temperature-programmed desorption (TPD), and tested for CO₂ hydrogenation. When Fe-K/γ-Al₂O₃ was used as a catalyst, CO₂ conversion was 36%, but when Fe-Ru-K/γ-Al₂O₃ was used, CO₂ conversion was 41%. The product selectivities for catalysts with and without the ruthenium component were also compared. Fe-K/γ-Al₂O₃ exhibited higher methane (16 mol%) and C₂–C₄ selectivity (39.6 mol%) than Fe-Ru-K/γ-Al₂O₃. The main products obtained with Fe-Ru-K/γ-Al₂O₃ were higher hydrocarbons such as C₅⁺ hydrocarbons. For Fe-Ru-K/γ-Al₂O_3, the product distribution followed the Anderson–Schultz–Flory (ASF) distribution. However, in the case of Fe-Ru-K/γ-Al₂O₃, the hydrocarbon distribution deviates from the ideal ASF distribution. It is concluded that the readsorption rates of the primary hydrocarbon product increase exponentially with chain length in the ruthenium promoted catalytic system. The behavior of catalysts with and without the ruthenium will be explained by the CO₂-, CO- and C₂H₄– profiles. In this study, it was confirmed that ruthenium component promoted the readsorption ability of -olefin, and then the chain length of hydrocarbon is higher. In addition, the microcrystalline wax produced in CO₂ hydrogenation was a high-crystalline and olefin-rich hydrocarbon.     

Surface modification of γ-alumina membranes by silane coupling for CO2 separation

Top layers of γ-Al₂O₃ composite membranes have been modified by the silane coupling technique using phenyltriethoxysilane for improving the separation factor of CO₂ to N₂. The separation efficiency of the modified membranes was strongly dependent upon the hydroxylation tendency of the support materials and the amount of the special functional group (i.e. phenyl radical) which was coupled onto a top layer. The separation factor through the TiO₂ supported γ-Al₂O₃ membrane was found to be fairly enhanced by silane coupling, but in case of the -Al₂O₃ supported membrane was not. The CO₂/N₂ separation factor through the modified γ-Al₂O₃/TiO₂ composite membrane is 1.7 at 90°C and ΔP = 2 × 10⁵ Pa for the binary mixture containing 50 vol% CO₂. The separation factor is proportional to the CO₂ concentration in the gas mixture, and the modified membrane is stable up to 100°C. The main mechanism of the CO₂ transport through the modified γ-Al₂O₃ layer is known to be a surface diffusion.     

ZrO2修饰Al2O3纳米片负载钴催化剂的制备及其费托反应性能研究

通过水热法合成了Al₂O₃纳米片（Al₂O₃-CN）,采用浸渍法制备20%（质量分数）钴基催化剂,并应用于费托合成反应。制备的Al₂O₃-CN（226 m²/g）与商业氧化铝（Al₂O₃-C,249 m²/g）具有相近的比表面积,但Al₂O₃-CN孔尺寸分布更加集中。浸渍钴后,与Co/Al₂O₃-C催化剂相比,Co/Al₂O₃-CN催化剂表现出较高的还原度及更均匀的钴颗粒粒径分布。因此,Co/Al₂O₃-CN催化剂表现出更高的CO转化率和低的甲烷选择性。为了进一步提高Co/Al₂O₃-CN的催化性能,采用不同含量ZrO₂对Al₂O₃-CN进行修饰。表征结果表明,随着ZrO₂修饰量的增加,Al₂O₃-CN载体比表面积变化不明显,孔体积和孔径增大;相对应催化剂的钴颗粒粒径减小,活性位点数目增加。在相同反应条件下,经ZrO₂修饰催化剂CO转化率进一步提高,甲烷选择性降低。     

吸附剂修饰铁基氧载体的氧化动力学研究

研究了吸附剂修饰合成Fe_2O_3/Al_2O_3的氧化动力学。其中,吸附剂(K_2O、Na_2O、CaO)用于控制化学链燃烧过程中有毒氯化物、硫化物以及重金属的排放。首先在热重分析仪(TGA)上利用合成气作为还原气氛使氧载体呈还原态(FeO/Al_2O_3),在空气气氛下进行了原FeO/Al_2O_3以及三种吸附剂修饰FeO/Al_2O_3的氧化实验,实验温度分别为850、875、900和925℃。通过八种等温动力学模型对900℃下原FeO/Al_2O_3的氧化过程进行了分析。结果表明,phase boundary-controlled(contracting cylinder)模型能够很好地描述其氧化过程(FeO向Fe_2O_3转化过程)。利用该模型分别计算了原FeO/Al_2O_3、K_2O修饰FeO/Al_2O_3、Na_2O修饰FeO/Al_2O_3和CaO修饰FeO/Al_2O_3的氧化动力学参数,其表观活化能分别为13.71、20.21、21.62和24.20 k J/mol。通过进行比较依据动力学参数计算得到的转化率随时间的函数以及实验获得的转化率随时间的函数,进一步证实了phase boundary-controlled(contracting cylinder)模型的可靠性以及相应动力学参数的准确性。     

CuO/ZnO/Y2O3/γ-Al2O3双功能催化剂上二甲醚水蒸气重整制氢

将沉积-沉淀法制备的CuO/ZnO/Y2O3催化剂同γ-Al2O3进行机械混合, 制备了CuO/ZnO/Y2O3/γ-Al2O3双功能催化剂, 用于二甲醚水蒸气重整制氢反应, 实验结果表明其活性、稳定性等均优于常用的CuO/ZnO/Al2O3/γ-Al2O3催化剂. 结合N2吸附-脱附(BET)、N2O化学吸附(N2O chemisorption)、NH3程序升温脱附(NH3-TPD)、X射线衍射(XRD)、H2程序升温还原(H2-TPR)等表征手段研究了两种催化剂在表面酸性及微观结构上的差异, 发现CuO/ZnO/Y2O3催化剂具有相对较高的铜分散度, 铜晶粒更加细小化, 并且具有高温稳定性的Y2O3可能起到隔离铜的作用, 在一定程度上防止了铜晶粒的团聚, 从而改善了重整组分的性能, 提高了双功能催化剂的重整制氢活性及稳定性.     

沉淀法制备Bi2O3的晶相转变过程及其光催化性能

以硝酸铋为原料,氨水为沉淀剂,通过液相沉淀法制得前驱体Bi(OH)₃,并将Bi(OH)₃分别在不同温度和时间下焙烧。利用X射线衍射(XRD)、拉曼光谱、热重(TG)、扫描电子显微镜(SEM)、X射线光电子能谱(XPS)及紫外-可见漫反射光谱(UV-Vis DRS)详细研究了Bi(OH)₃转变为Bi₂O₃的过程及相变过程中粒子形貌、大小、光吸收性质等。结果表明,前驱体Bi(OH)₃经过焙烧之后,发生了如下的转变过程:Bi(OH)₃→Bi₅O₇NO₃→β-Bi₂O₃/Bi₅O₇NO₃→β-Bi₂O₃/Bi₅O₇NO₃/α-Bi₂O₃→α-Bi₂O₃,而且转变过程伴随着粒子长大。在上述转变过程中,与Bi₅O₇NO₃向β-Bi₂O₃转变的过程相比,从β-Bi₂O₃到α-Bi₂O₃相变过程更为迅速。此外,以光催化降解罗丹明B(RhB)为模型反应,考察了不同晶相的Bi₂O₃光催化活性,结果表明Bi₅O₇NO₃和β-Bi₂O₃材料具有优异的光催化性能,而α-Bi₂O₃具有较低的光催化活性。     

Y2O3包覆LiCo1/3Ni1/3Mn1/3O2的电化学性能

通过在硝酸钇水溶液浸渍并焙烧的简单工艺, 在LiCo1/3Ni1/3Mn1/3O2材料表面包覆了一层Y2O3. 采用X射线衍射(XRD), 扫描电子显微镜(SEM), 透射电子显微镜(TEM), 循环伏安(CV)和恒流充放电对包覆和未包覆的LiCo1/3Ni1/3Mn1/3O2进行了测试分析. 结果表明, Y2O3包覆并没有改变LiCo1/3Ni1/3Mn1/3O2的晶体结构, 只存在于LiCo1/3Ni1/3Mn1/3O2的表面; 与未包覆的材料相比, Y2O3包覆后的材料在高电位下具有更好的容量保持率和放电容量. CV测试表明, 包覆层的存在有效抑制了材料层状结构的转变及电极与电解液的负反应.