无机体系合成纳米丝光沸石组装体及其优异的二甲醚羰基化催化性能

乙醇是一种重要的有机化工原料和燃料/燃料添加剂.二甲醚(DME)羰基化制乙酸甲酯(MAc)并进一步加氢制备乙醇提供了一条乙醇生产新途径.作为该路线的核心过程,DME羰基化制备MAc反应具有原子经济性高和反应条件温和等特点,近年来备受关注.在DME羰基化制备MAc的多相催化剂中,丝光沸石(MOR)是迄今为止最为高效的催化剂之一,表现出优异的羰基化反应活性和高MAc选择性.但传统的无机体系合成方法只能得到Si/Al比(SAR)介于5～7的MOR沸石,且晶体尺寸通常较大.本文设计了低碱度凝胶体系和晶种法相结合的合成策略,在无有机模板条件下绿色高效合成了SAR最高为9.4的MOR沸石纳米组装体.选取三个具有不同SAR(I-5.3,I-7.4和I-9.4)的样品进一步表征并与其催化性能相关联.实验发现,催化剂的酸强度随着SAR的提高而明显增强,但是三个样品的总酸量以及Br?nsted酸在主孔道和侧口袋的分布比例接近.利用傅里叶变换红外和钠核磁技术分别对H-MOR及其Na-MOR母体样品中的酸羟基和Na+的空间分布进行分析,发现质子在主孔道与侧口袋的分布比例与Na+的分布并不一致,表明质子和Na+可以落位于同一T位的不同氧位.通过对催化剂扩散性质以及酸性位的可接触性的表征,发现低硅样品I-5.3和I-7.4尽管晶粒尺寸较小,但由于孔道中骨架外铝的含量较高,严重阻碍内扩散,并且导致吡啶对12元环主孔道中酸中心的可接触性降低.相对于低硅样品,高硅样品I-9.4由于其相对较低的骨架铝密度和较低的脱铝程度,表现出最优的传质性能以及吡啶对12元环主孔道中酸中心的可接触性,催化剂主通道中的所有酸性位都能被吡啶所覆盖.相应地,样品I-9.4(吡啶修饰催化剂)在DME羰基化反应中表现出较高的催化活性与MAc选择性(接近100％),MAc产率高达6.8 mmol/g/h.综上,本文发展的无有机模板策略合成MOR沸石纳米组装体具有良好应用前景.     

Gas Phase Selective Catalytic Oxidation of Toluene to Benzaldehyde on V2O5-Ag2O／η-Al2O3 Catalyst

Gas phase selective catalytic oxidation of toluene to benzaldehyde was studied on V2O5-Ag2O/η-Al2O3 catalyst prepared by impregnation. The catalyst was characterized by XRD, XPS, TEM,and FT-IR. The catalytic results showed that toluene conversion and selectivity for benzaldehyde on catalyst sample No.4 (V/(V Ag)=0.68) was higher than other catalysts with different V/Ag ratios. This was attributed to the higher surface area, larger pore volume and pore diameter of the catalyst sample No.4 than the other catalysts. The XRD patterns recorded from the catalyst before and after the oxidation reaction revealed that the new phases were developed, and this suggested that silver had entered the vanadium lattice. XPS results showed that the vanadium on the surface of No.4 and No.5 sample was more than that in the bulk, thus forming a vanadium rich layer on the surface. It was noted that when the catalyst was doped by potassium promoter, the toluene conversion and selectivity for benzalde hydewere higher than those on the undoped catalyst. This was attributed to the disordered structure of V2O5 lattice of the K-doped catalyst and a better interfacial contact between the particles.     

Gas Phase Selective Catalytic Oxidation of Toluene to Benzaldehyde on V2O5-Ag2O/η-Al2O3 Catalyst

Gas phase selective catalytic oxidation of toluene to benzaldehyde was studied on V2O5-Ag2O/η-Al2O3 catalyst prepared by impregnation. The catalyst was characterized by XRD, XPS, TEM,and FT-IR. The catalytic results showed that toluene conversion and selectivity for benzaldehyde on catalyst sample No.4 (V/(V Ag)=0.68) was higher than other catalysts with different V/Ag ratios. This was attributed to the higher surface area, larger pore volume and pore diameter of the catalyst sample No.4 than the other catalysts. The XRD patterns recorded from the catalyst before and after the oxidation reaction revealed that the new phases were developed, and this suggested that silver had entered the vanadium lattice. XPS results showed that the vanadium on the surface of No.4 and No.5 sample was more than that in the bulk, thus forming a vanadium rich layer on the surface. It was noted that when the catalyst was doped by potassium promoter, the toluene conversion and selectivity for benzaldehyde were higher than those on the undoped catalyst. This was attributed to the disordered structure of V2O5 lattice of the K-doped catalyst and a better interfacial contact between the particles.     

ZSM-5／MOR复合分子筛催化剂对混合C4烃转化反应的催化性能

以ZSM-5/丝光沸石(MOR)复合分子筛为催化剂,对混合C4烃的催化转化反应进行了评价,并采用程序升温脱附和原位红外光谱技术对ZSM-5/MOR的酸性进行了表征. 结果表明,与ZSM-5相比, MOR具有很低的催化活性,但ZSM-5/MOR复合分子筛具有较高的催化活性,随着ZSM-5/MOR复合分子筛中ZSM-5含量的增加, C4烃转化率稍有升高;在C4烃转化率大致相同的情况下,乙烯和丙烯的总选择性比较接近,但苯和甲苯的总收率却快速升高. 随着ZSM-5/MOR复合分子筛中ZSM-5含量的增加,弱酸和中强酸的酸量逐渐减少,强酸的酸量有所增加. 由于ZSM-5/MOR复合分子筛中MOR对ZSM-5起到分散作用而产生更多的L酸中心,且此L酸中心处于分子筛的外表面而具有较高的能量,导致苯和甲苯的总收率升高.     

NaBr/KY催化剂在甲苯氧化甲基化反应中的稳定性

考察了NaBr/KY催化剂的甲苯氧化甲基化(OMT)反应的稳定性，经过50 h的OMT反应结果表明，在反应初期，甲苯转化率、总C8选择性均有不同程度的下降，之后趋于稳定.在总C8产物中，苯乙烯的选择性随着反应的进行呈下降趋势，而乙苯的选择性与苯乙烯相比呈相反的变化趋势.此外，利用XRD、骨架IR、XPS对反应前后的催化剂结构进行了研究，发现催化剂经过50 h的OMT反应，分子筛的结构遭到了部分破坏，但其基本骨架仍保留.     

Influence of platinum and hydrogen on n-butane isomerization on H-Mordenite

Hydrogen inhibits n-butane isomerization of H-MOR and improves catalyst stability and selectivity. Similarly, when Pt is present, hydrogen inhibits the reaction which is always controlled by the acid function.     

大孔沸石催化剂上苯与丙烯液相烷基化反应行为的研究

围绕具有工业实用价值的苯与丙烯液相烷基化制取异丙苯这一课题,对比考察了不同硅铝组成的ＨＹ型和Ｈβ型沸石的催化性能,利用烧炭试验、结炭前驱物萃取方法及色－质谱表征手段探索了沸石催化剂在烷基化反应中的结炭行为。烷基化试验结果表明,β沸石对异丙苯的选择性和催化剂稳定性都明显优于Ｙ型,其异丙苯选择性可达９６ｍｏｌ％以上。同时,提高原料苯烯比、降低反应温度或保持适当高的进料空速能够提高异丙苯的选择性。结炭催化剂的烧炭结果显示,在烷基化反应中Ｈβ比ＨＹ具有较强的抗结炭能力。结炭催化剂的溶剂萃取结果表明,反应中的液相苯能够有效地使催化剂孔道中的结炭前驱物种脱离催化剂表面,从而抑制结炭,提高催化剂的稳定性     

晶种数量对MOR分子筛上烷基转移反应的影响及反应机理研究

以丝光沸石(MOR)分子筛为催化剂,甲苯与三甲苯烷基转移反应为探针反应,系统考察了晶种数量变化对分子筛物化性能和催化性能的影响。研究表明,合成过程中晶种添加量的不同会显著影响催化剂的酸性、比表面积和孔体积,进而影响其催化剂活性和稳定性。当晶种添加量为8%时,MOR分子筛具有最多的B酸含量、最大的比表面积和孔体积,同时对应的催化剂活性和稳定性也最好。本研究还对甲苯和三甲苯烷基转移反应机理进行了深入研究,结果表明,发生在MOR分子筛上的烷基转移反应通过双分子中间体机理进行,并应用实验手段捕捉到了中间体的存在,证实了双分子中间体机理的合理性,同时推导出可能的反应机理路线图。     

High benzene selectivity of mesoporous silicate for BTX gas sensing microfluidic devices

The gas selectivities of highly ordered mesoporous silicates and commercially-obtained porous silicates with respect to benzene, toluene and xylene were studied. After studying the porosities, pore uniformities, and surface silanol structures of the silicates and their relationships to gas selectivity in detail, we found that we could achieve high benzene selectivity by controlling the micropore size (less than 1 nm). Concluding that mesoporous silicate has a suitable micropore size and structure for benzene selectivity, we also observed that mesoporous silicate SBA-16 exhibited a high (>6) benzene selectivity from toluene and xylene even in a pseudo-atmospheric environment. A benzene detection limit of about 100 ppb was achieved by introducing SBA-16 into a microfluidic device originally developed for the separate detection of benzene, toluene, and xylene gases.     

Na-W-Mn/SiO2催化剂表面甲烷脉冲反应Ⅱ. 多组分Na、 W、 Mn/SiO2催化剂

制备了多组分Na,W,Mn/SiO2催化剂，在ITD（Ion Trap Detector)装置上进行了催化剂表面晶格氧脱附前后的甲烷恒温脉冲反应（CH4－CTPR）。研究结果表明，Na-W/SiO2催化剂表面晶格氧，具有较高的CH4转化率和C2烃选择性，并对C2H6的生成起着重要的作用，Na-Mn/SiO2催化剂表面晶格氧，也具有较高的CH4转化率和C2烃选择性，但对C2H6的形成有一定的诱导期；W－Mn/SiO2催化剂表面晶格氧，对CH4的转化和CO2的生成具有很高初活性，但对C2烃的选择性较低；Na-W-Mn/SiO2催化剂表面晶格氧，具有很高的CH4转化率和C2烃定向选择性，这是由于Na,W,Mn各组分协同作用的结果。     

磷改性Cr2O3/Al2O3催化4-乙基酚转化制轻质芳烃

以烷基酚转化为轻质芳烃（苯和甲苯）为目标，制备了Cr₂O₃/Al₂O₃催化剂，并以4-乙基酚为模型化合物研究了其加氢反应性能。体积空速、氢油比、反应压力和温度升高时，脱烷基率、芳烃总选择性、轻质芳烃选择性呈先增大后减小的趋势，反应温度对转化率影响较大。以不同浓度磷酸对Cr₂O₃/Al₂O₃进行改性，随着磷酸用量的增大，催化剂酸量总体增大，主要是弱酸和中强酸，酸强度先增加后降低，磷酸用量较高时，弱酸增加幅度较大。与未改性相比，质量分数8%磷酸改性Cr₂O₃/Al₂O₃上4-乙基酚转化率99.5%，脱烷基率提升9.4%，达74.4%，轻质芳烃选择性提高4.0%，达到57.0%，以较高选择性实现了转化制轻质芳烃，同时，芳烃总选择性高达80.4%，较高程度保持了芳环不被破坏。提出了Cr₂O₃/Al₂O₃上4-乙基酚加氢反应的路径并对反应机理进行了研究。     

A Novel Non-phosgene Process for the Synthesis of Methyl N-Phenyl Carbamate from Methanol and Phenylurea： Effect of Solvent and Catalyst

A novel environmentally benign process for the synthesis of methyl N-phenyl carbamate (MPC) from methanol and phenylurea was studied. Effect of solvent and catalyst on the reaction behavior was investigated. The IR spectra of methanol and phenylurea dissolved in different solvents were also recorded. Compared with use of methanol as both a reactant and a solvent, phenylurea conversion and selectivity to MPC increased by using toluene, benzene or anisole as a solvent, while phenylurea conversion decreased slightly by using n-octane as a solvent. The phenylurea conversion declined nearly 50% when dimethyl sulfoxide (DMSO) was used as a reaction media, and MPC selectivity decreased as well. The catalytic reaction tests showed that a basic catalyst enhanced the selectivity to MPC while an acidic catalyst promoted the formation of methyl carbamate and aniline. Moderate degree of basicity showed the best catalytic performance in the cases studied.     

新型苯选择加氢制环己烯非晶态催化剂Ru-Fe-B/ZrO2的制备及其可调变性

采用化学还原法制备了一种新型高活性和高选择性苯选择加氢制环己烯的Ru-Fe-B/ZrO2纳米非晶态合金催化剂,并利用透射电镜、选区电子衍射、X射线衍射和N2物理吸附仪等手段对催化剂进行了表征.重点研究了Ru-Fe-B/ZrO2催化剂活性和选择性的可调变性,及还原剂NaBH4浓度和洗涤后滤液的pH值对其催化性能的影响.结果表明,在新型Ru-Fe-B/ZrO2催化剂上,当苯转化54%时,环己烯选择性高达80%,同时环己烯选择性随苯转化率升高而缓慢下降.向反应浆液中添加酸性或碱性物质可以调变催化剂的活性和选择性,同时催化剂制备工艺和性能具有很好的可重复性.Ru-Fe-B/ZrO2催化剂融合了纳米和非晶材料的特性,这是其对苯选择加氢制环己烯表现出高活性和高选择性的主要原因.     

近临界下HZSM-5催化的甲苯歧化反应

用高压观测池通过可视观测确定了苯、甲苯和对二甲苯等二元系及三元系的临界性质以及甲苯歧化反应混合物临界性质随着反应进程的变化规律；在此基础上，分别研究了近临界区以及高温下以HZSM-5为催化剂的甲苯歧化反应。结果发现，在近临界区甲苯歧化反应的对二甲苯选择性最高，随温度的升高甲苯转化率明显增加，对二甲苯选择性下降。高温下压力对对二甲苯选择性没有影响，转化率随压力升高而提高。     

Cr2O3-Al2O3催化剂半导性对催化性能的影响

在剖析Cr_2O_3-Al_2O_3系催化剂微观结构的基础上,通过对Cr_2O_3 Al_2O_3的电导测定、热磁分析研究了Cr_20_3-Al_2O_3催化剂的半导性及它对临氢脱烷基催化过程的影响。实验结果表明,氧化态Cr_2O_3为p型半导体,在还原气氛中,将转化为n型。其转变温度随Cr_2O_3含量的增加而提高。催化甲苯临氢脱烷基的活性中心为Cr(Ⅱ)。具有尖晶石结构的γ-Cr_2O_3比α-Cr_2O_3的活性更好。在甲苯气氛中,载流子Cr(Ⅱ)越多,活性越高;在苯气氛中,载流子Cr(Ⅱ)相对越少,其对苯的选择性越好。     

Ni‐W Catalysts Supported on HZSM‐5/HMS for the Hydrogenation Reaction of Aromatic Compounds: Effect of Ni/W Ratio on Activity,Stability, and Kinetics

Ni‐W/HZSM5‐HMS catalysts were evaluated for the benzene hydrogenation reaction at 130–190°C. To study the catalyst characterization, X‐ray diffraction, X‐ray fluorescence, Fourier transform infrared, UV–vis, diffuse reflectance spectra, temperature‐programmed desorption of NH₃, FT‐IR of adsorbed pyridine measurements (Py‐IR), H₂ chemisorption, nitrogen adsorption–desorption, and TGA techniques were used. Kinetics of benzene hydrogenation was investigated under various hydrogen and benzene pressures, and the effect of reaction conditions on catalytic performance was studied. The results showed that bimetallic catalysts have better ability than a monometallic catalyst (Ni/HZSM5‐HMS) for this reaction, such as maximum benzene conversion (100%), minimum toluene conversion (1.76–40%), very low converted xylene, benzene selectivity (100%), good catalytic stability against coke deposition, and appropriate kinetic parameters.     

Synergistic effect of dealumination and ceria impregnation to the catalytic properties of MOR zeolite

MOR zeolite has been extensively employed as a catalyst in industries. However, high Brønsted acidity in MOR leads to rapid deactivation due to coke deposition on the pore mouths; thus, the surface acidity of MOR needs to be moderated. Herein, we report a modification of MOR chemical composition via acid treatment and deposition of ceria nanoparticles using a wet impregnation method. The acid treatment successfully increases the Si/Al ratio of MOR from 8.39 to 11.58 and reduces the total acid site concentration of MOR from 990 μmol/g to 752 μmol/g. The acidity of MOR is decreased when the Si/Al ratio is increased since the quantity of Brønsted acid sites is proportional to the number of Al framework. In addition, the acid treatment also improves the external surface area of MOR. Furthermore, ceria particles were successfully deposited on the MOR surface using wet impregnation method. The ceria content of parent MOR sample is lower compared to that of preceded by the acid treatment, which may be attributed to the formation of more terminal silanol groups. Finally, catalytic test on Friedel–Crafts alkylation of toluene with benzyl alcohol shows that the synergy between dealumination and the impregnation of ceria significantly improves the activity of MOR zeolite.     

Liquid-phase oxidation of ethylamine to acetaldehyde oximes over tungsten-doped zeolites

The liquid-phase oxidation of ethylamine with hydrogen peroxide was studied over tungsten-doped zeolites to develop a clean and simple route for producing acetaldehyde oxime. The investigations were firstly performed over W/MOR, where the coordinated state as well as the acidity of the W species were characterized. The reaction parameters, including H_2O_2 amount, solvent,temperature, tungsten content as well as catalyst amount, governed the activity and oxime selectivity. Under optimized reaction conditions, W/MOR showed an ethylamine conversion and corresponding oxime selectivity of 18.3% and 88.9%. W/MOR showed a superior performance in comparison to other tungsten-containing zeolites of W/Beta, W/MWW and W/Y. Although W/MOR exhibited lower amine conversion than titanosilicates of TS-1 and Ti-MWW, it gave higher selectivity to the main product of oxime. Moreover, W/MOR proved to be a robust catalyst, exhibiting a stable catalytic performance after being reused at least for 5 times.     

镧-钼复合氧化物超细微粒催化剂结构和甲苯选择氧化催化性能

镧－钼复合氧化物超细微粒催化剂结构和甲苯选择氧化催化性能匡文兴范以宁陈开东邱金恒王镇浦＊陈懿（南京大学化学系，南京２１００９３；＊南京化工大学应化系，南京２１０００９）关键词：镧－钼复合氧化物超细微粒结构甲苯选择氧化近年来，有关甲苯选择氧化方面的文献...     

Hydrogen Effect on Coke Removal and Catalytic Performance in Pre-Carburization and Methane Dehydro-Aromatization Reaction on Mo/HZSM-5

1. Introduction As an effective utilization of methane, the methane dehydro-aromatization was focused in the last decade [1-28]. Over the Mo/HZSM-5 bi- functional catalyst at high reaction temperature, methane can be converted into light aromatics (ben- zene and naphthalene) and hydrogen. Mo active species can activate the C—H bond of methane; and HZSM-5 supplies the acid sites for the oligomeriza- tion and cyclization of hydrocarbons to form aromat- ics, and suppresses the deeper condens…