可见光驱使下有机染料与镍配合物催化放氢芳构化反应研究

在可见光催化下,联合廉价易得的有机染料曙红Y与容易制备的镍催化剂在室温条件下,高效绿色地实现了分子内的脱氢芳构化,此过程中只放出氢气无副产物,无需外在氧化剂,条件温和,产率高,对环境友好.此外,在其他条件相同的情况下,将绝氧条件下的放氢反应跟与有氧条件下的需氧氧化反应进行了对照,发现汉斯酯衍生物及1,4-二氢嘧啶衍生物在放氢条件下得到较高产率;而在需氧氧化条件下3,4-二氢噻吩衍生物、2,5-二氢吡咯衍生物芳构化的转化率更高.     

生物质衍生物γ-戊内酯催化转化制芳烃和2-环戊烯酮的研究

应用浸渍法在ZSM-5沸石分子筛孔道中引入过渡金属Zn物种,制备了具有不同Zn含量的Zn/ZSM-5。考察了反应温度、催化剂用量、催化剂的酸性性质等条件对γ-戊内酯芳构化产物组成(气、液、固产物)及其液体成分含量的影响。实验结果表明,ZSM-5分子筛孔道中引入Zn后,可以有效改变液体产物成分以及影响气体和固体产物收率。当ZSM-5分子筛孔道中引入Zn物种后,能够明显提高液体产物中苯、甲苯、乙苯、萘等芳香类化合物的含量,表明Zn物种能促进γ-戊内酯芳构化反应的进行。     

Propane Aromatization over Mo/HZSM-5 Catalysts

Impregnation, mechanical mixing and hydrothermal treatment methods were used to introduce molybdenum species into the HZSM-5 zeolite. The structure and surface acidity of the catalysts were studied by means of XRD, FT-IR, NH3-TPD, TPR and XPS. The effects of Mo content and reaction time on stream on the aromatization of propane were investigated. It was found that the performance of the Mo/HZSM-5 catalyst prepared by the hydrothermal treatment method was much better than that of the other two catalysts. For example, under the reaction conditions of 823 K and 600 h-1, propane conversion and aromatics selectivity over the catalyst prepared by hydrothermal pretreatment could reach 89.17% and 78.56%, respectively. XRD and XPS results showed that the Mo species in the catalysts prepared by hydrothermal treatment were highly dispersed on the surface of the HZSM-5, and larger amounts of them could penetrate into the HZSM-5 channel, as compared with the other two kinds of catalysts. These factors may be responsi     

1,4-二氢吡啶衍生物合成方法的改进和芳构化研究

改进了Hantzsch合成法,通过一锅煮合成1,4-二氢吡啶衍生物,大大缩短了反应时间,操作简便,发现氯化铁是一个较好的1,4-二氢吡啶衍生物芳构化的氧化剂。     

新型甲烷无氧芳构化催化剂MoO3/MCM-49

自Ｂｅｎｎｅｔｔ[1]等合成出新型分子筛ＭＣＭ 4 9以来 ,有关其结构及性质研究的报道相对较少 .Ｂｅｎ ｎｅｔｔ[1]指出 ,ＭＣＭ 4 9在一些特殊的催化反应上表现出了比ＭＣＭ 2 2更高的活性 (如在丙烯无氧芳构化反应中 ,ＭＣＭ 4 9上丙烯的转化率为 7 1 6% ,远大于ＭＣＭ 2 2的 2 64% ) .ＭＣＭ 4 9的发现时间较晚 ,且合成相对困难 ,在一定程度上限制了对其性质的进一步研究 .对甲烷无氧芳构化催化反应的研究发现 ,酸性适当且具有交叉十元环孔道体系的分子筛载体表现出了较高的催化活性 .ＭＣＭ 4 9与ＭＣＭ 2 2均具有两套互不相通的交叉…     

CH_4在Mo/HZSM-5及其改性催化剂上的无氧芳构化(英文)

运用微型固定床反应器装置,研究了Mo/HZSM-5催化剂的Mo载量、金属助剂改性、载体模数对甲烷无氧芳构化反应性能的影响。结果表明,Ni/Mo摩尔比为0.1的Mo-Ni/HZSM-5(SiO2/Al2O3=25)催化性能最好,其稳定性较好,芳烃收率最高可达15.74%;此时甲烷转化率60.24%,芳烃选择性26.13%。     

Synthesis and characterization of poly(benzazoles) containing the bicyclo[2.2.2]octane moiety

Poly(benzobisoxazoles) (PBOs), poly(benzobisthiazoles) (PBTs) and copolymers thereof containing the 2,5-dihydroxybicyclo[2.2.2]octane moiety have been prepared and studied. The homopolymers were synthesized by the polycondensation of 2,5-dihydroxybicyclo[2.2.2]octane-1,4-dicarboxylic acid with 4,6-diamino-1,3-benzenediol dihydrochloride or 2,5-diamino-1,4-benzenedithiol dihydrochloride in poly(phosphoric acid). Random and block copolymers (PBO–PBT) were also prepared. The polymers were characterized by solubility, X-ray diffraction, spectroscopy (infrared and solid-state ¹³C nuclear magnetic resonance), and thermal analysis such as differential scanning calorimetry and thermogravimetric analysis. Thermogravimetric analysis showed thermal stability of the polymers above 375°C in air and under argon atmosphere. The polymers exhibited high resistance to organic and inorganic solvents. The polymers were converted to the more stable aromatic polymers via dehydration and retro Diels–Alder reactions of the 2,5-dihydroxybicyclo[2.2.2]octyl moiety by pyrolysis. © 1998 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 36: 277–281, 1998     

MoO3/HBZSM-5催化剂上甲烷的无氧芳构化反应

以含硼杂原子分子筛HBZSM-5为载体,考察了其担载MoO3后催化甲烷无氧芳构化反应的性能,并结合XRD,IR,TG和SEM等手段对催化剂进行了表征.实验结果表明,MoO3/HBZSM-5催化剂具有较高的甲烷芳构化活性,但稳定性较差.随着引入分子筛骨架中硼量的增大,甲烷的极值转化率增高;随着反应温度的升高,MoO3/HBZSM-5催化剂的甲烷芳构化活性升高.从产物分布的变化来看,硼的引入对于催化剂上乙烯的选择性影响较大;与MoO3/HZSM-5催化剂相比,MoO3/HBZSM-5催化剂上乙烯选择性大大提高.     

甲烷无氧芳构化反应中钼基分子筛催化剂上积炭的表征

利用化学方法对钼基分子筛催化剂上的CH2Cl2可溶性积炭和不可溶性积炭进行分离，并通过质谱、红外光谱、核磁共振等手段对积炭进行了表征。结果表明，可溶性积炭的主组分为一种非芳烃物质，它的组成不随反应时间、反应温度和催化剂的酸性的变化而变化。可溶性积炭分子对催化剂的活性影响不大。高不饱和度的稠环芳烃型不可溶性积炭分子是催化剂失活的主要原因。     

Zn/H-ZSM-5催化剂上的二甲醚芳构化反应

 考察了 H-ZSM-5 和 Zn/H-ZSM-5 催化剂的二甲醚芳构化性能. 结果表明, H-ZSM-5 分子筛催化剂酸性的增强和酸中心的增多有利于二甲醚芳构化. 当在 H-ZSM-5 催化剂中加入 2% Zn 时, 在 360 oC 下反应时总芳烃收率从 50.0% 增加至 66.2%, C8 芳烃收率从 28.6% 增加到 39.0%. 反应温度升高到 480 oC 时, 总芳烃收率增加至 78.0%.