Mo/HZSM-5催化剂上甲烷无氧芳构化反应——HZSM-5分子筛脱铝的影响

采用两种不同的脱铝方法对HZSM-5分子筛进行了预处理,并利用MAS NMR和吸附吡啶的FT-IR对分子筛的结构和酸性质进行了表征,考察了分子筛的脱铝程度对Mo基催化剂上甲烷芳构化反应性能的影响.结果表明,HZSM-5分子筛的酸性过强或B酸量不足,均会导致催化剂严重积炭,但积炭成因不同.母体HZSM-5分子筛上的强B酸中心的存在可促使催化剂上反应中间物种深度脱氢,造成催化剂在反应过程中严重积炭.经水热处理的HZSM-5分子筛,骨架铝脱出严重,造成B酸活性中心不足以及部分微孔阻塞,不利于C2中间物种芳构化,导致芳烃选择性显著降低.经高温N2处理的HZSM-5分子筛,骨架铝脱出相对缓和,在消除母体分子筛上强B酸中心的同时,保留了较多的弱B酸中心,既可满足C2中间物种芳构化反应的需要,又可有效抑制催化剂积炭,导致甲烷芳构化反应性能显著改善.     

Theoretical and Experimental Study on the Adsorption and Desorption of Methane by Granular Activated Carbon at 25 ℃

A theoretical and experimental study was conducted to accurately determine the amount of adsorption and desorption of methane by various Granular Activated Carbon(GAC)under different physical conditions.To carry out the experiments,the volumetric method was used up to 500 psia at constant temperature of 25℃.In these experiments,adsorption as well as desorption capacities of four different GAC in the adsorption of methane,the major constituent of natural gas,at various equilibrium pressures and a constant temperature were studied.Also,various adsorption isotherm models were used to model the experimental data collected from the experiments.The accuracy of the results obtained from the adsorption isotherm models was compared and the values for the regressed parameters were reported.The results shows that the physical characteristics of activated carbons such as BET surface area,micropore volume,packing density,and pore size distribution play an important role in the amount of methane to be adsorbed and desorbed.     

The Effect of Nb Loading on Catalytic Properties of Ni/Ce0.75Zr0.25O2 Catalyst for Methane Partial Oxidation

In this study,the effect of Nb loading on the catalytic activity of Ce_(0.75)Zr_(0.25)O_2-supported Ni catalysts was studied for methane partial oxidation.The catalysts were characterized by BET,H_2 chemisorption,XRD,TPR,TEM and tested for methane partial oxidation to syngas in the temperature range of 400-800℃at atmospheric pressure.The results showed that the activity of methane partial oxidation on the catalysts was apparently dependent on Nb loading.It seemed that the addition of Nb lowered the catalytic activity for methane partial oxidation and increased the extent of carbon deposition. This might be due to the strong interaction between NiO and Nb-modified support and reduction of surface oxygen reducibility.     

CH4, CO2和H2O在非金属原子修饰石墨烯表面的吸附

煤层气(矿井瓦斯)是一种有望替代传统化石燃料，如煤、石油和天然气的非常规气体. 作为可得的清洁能源，它的利用被认为是节能和经济的选择. 在本工作中，非金属原子X(X=H，O，N，S，P，Si，F，Cl)修饰的石墨烯(Gr)被用来代表具有结构异性的煤表面模型. 通过密度泛函理论系统地研究了煤层气组分Y(Y=CH₄，CO₂，H₂O)在非金属原子修饰石墨烯上的吸附作用. 结果表明Y在非金属原子修饰石墨烯上的吸附均为物理吸附. 态密度和差分电荷密度共同表明了这种弱的相互作用.其中，H和Cl对CH₄的作用较大； N、O、F、Cl对CO₂的作用较强； N，Cl对H₂O的影响不容忽视. 总的来说，吸附能大小依次为：H₂O>CO₂>CH₄. 因此，在CH₄富集的煤层里注入H₂O或CO₂可以与CH₄形成竞争吸附，进而提高煤层气采收率. 本工作提供了在分子水平下煤层气与非金属原子修饰石墨烯之间的相互作用的详情，并为煤层瓦斯的开采与分离提供了有用的信息.     

甲烷直接氧化制甲醇Ⅱ．催化膜反应器（CMR）

采用溶胶－凝胶（Ｓｏｌ－Ｇｅｌ）法制备了微孔结构均匀的“ＳｉＯ＿２／陶瓷”膜和“Ｍｏ－Ｃｏ－·Ｏ／ＳｉＯ＿２／陶瓷”催化功能膜，并用ＸＲＤ、ＳＥＭ和孔径测定等技术进行了表征。在常压、５００～７００℃的条件下，在催化膜反应器（ＣＭＲ）中考察了甲烷氧化制甲醇的反应。在相似的反应条件下（转化率为１．０％），用ＣＭＲ（甲醇选择性１１．２％）可获得较固定床反应器（甲醇选择性４．５％）高得多的甲醇选择性。     

Syntheses and structural characterization of heterometallic bis(pyrazolyl)methane complexes of rhenium and platinum

The new heterometallic complex {μ-1,3,5-[CH(pz)₂]₃C₆H₃}[Re(CO)₃Br][Pt(p-tolyl)₂]₂ has been prepared by reaction of 1 equiv. of the dimer [Pt(p-tolyl)₂(μ-SEt₂)]₂ with the monometallic rhenium precursor {1,3,5-[CH(pz)₂]₃C₆H₃}Re(CO)₃Br, where 1,3,5-[CH(pz)₂]₃C₆H₃ is the tritopic, arene-linked bis(pyrazolyl)methane ligand 1,3,5-tris[bis(1-pyrazolyl)methyl]benzene. Similarly, the heterometallic complex {μ-1,3,5-[CH(pz)₂]₃C₆H₃}[Re(CO)₃Br]₂[Pt(p-tolyl)₂] has been made by the reaction of the dirhenium compound {μ-1,3,5-[CH(pz)₂]₃C₆H₃}[Re(CO)₃Br]₂ and one-half of an equivalent of [Pt(p-tolyl)₂(μ-SEt₂)]₂. X-ray crystallographic studies of the new compounds reveal significant noncovalent interactions in their molecular and supramolecular structures.     

Methane production from synthesis gas using a mixed culture ofR. rubrum M. barkeri,and M. formicicum

The components of synthesis gas, CO, H₂, and CO₂, may be converted into CH₄ biologically through either acetate or H₂/CO₂ as intermediates. Of these two routes, conversion through H₂/CO₂ is preferred. This paper presents results of mixed-culture studies employing the photosynthetic bacteriumR. rubrum for converting CO to CO₂ and H₂ by the water gas shift reaction and two methanogens,M. formicicum andM. barkeri, for converting CO₂ and H₂ into CH₄. Results are presented for triculture operation in two types of reactors, the packed bubble column and the trickle-bed reactor.     

NiO/SnO2-ZrO2催化剂的制备及甲烷燃烧催化性能的研究

利用正交分析，通过溶胶凝胶－超临界干燥及复合浸渍的方法制备了NiO/SnO2-ZrO2催化剂，进行了活性评价，考察了前驱物、NiO、SnO2含量及制备方法对催化剂活性及稳定性的影响，并采用XRD、TEM对催化剂进行了表征分析，结果表明：NiO/SnO2-ZrO2催化剂具有良好的甲烷燃烧催化性能（t100%=640 ℃），其活性、稳定性与制备参数密切相关，其中NiO含量是影响催化剂活性、稳定性的最主要参数，它对催化剂稳定性和活性的影响规律正相反； SnO2组分的添加使ZrO2单斜相稳定，对催化剂起到了良好的稳定化作用，发现当SnO2含量在6 mol％左右时，催化剂具有较好的稳定性；对于制备方法，在凝胶前加入活性组分有利于催化剂的高活性，而在凝胶后加入活性组分，则有利于催化剂保持较好的稳定性；活性组分前驱物对催化剂性能影响不大，采用Ni(NO3)2作为前驱物较为合适。     

Mo/MCM-22分子筛碳化钼活性中心结构及甲烷活化机理的密度泛函理论研究

 应用密度泛函理论研究了Mo/MCM-22分子筛上碳化钼活性中心的几何结构和电子结构,以及甲烷在该活性中心上的活化机理. 设计了两种结构的活性中心模型: Mo(CH2)2(模型A)和Mo(CH)CH2(模型B); 它们都嫁接在MCM-22分子筛超笼边缘的T4位的Brnsted-酸性位上,用3T簇模型代替分子筛的骨架,对所设计的模型进行了几何结构优化和电子结构分析. 结构优化结果显示, Mo与CH2端基以双键结合,键长为0.18～0.19 nm, 而Mo与CH端基以叁键结合,键长为0.17 nm. 通过自然键轨道分析,证明中心钼原子以配位键与骨架氧原子结合. 根据前线分子轨道的分析,预测了甲烷活化反应将发生在甲烷分子的HOMO和钼活性中心的LUMO之间,即 C-H 键的电子流向 Mo-C 键的π*轨道. 甲烷 C-H 键发生异裂, H+和H3C-基团分别与 Mo-C 键上的Mo和C成键. 在模型A上,甲烷活化反应的活化能为119.97 kJ/mol; 在模型B上,甲烷的H原子可以分别结合到CH2端基和CH端基上,对应的活化能分别为91.37和79.07 kJ/mol.