含氮ZSM-5分子筛骨架中氮取代位置的密度泛函计算

运用Gaussian 98程序包, 采用密度泛函理论B3LYP方法, 基于ZSM-5分子筛的8T模型, 分别通过6-31G, 6-31G(d)和6-311G(d,p)基组计算了ZSM-5分子筛中氮原子取代前后各O原子和各N原子的能量, 从而得到各O原子与各N原子在骨架中的稳定性及其对氮化取代反应的影响. 计算结果表明, N原子在骨架中的稳定性对氮取代反应的影响较大. ZSM-5分子筛晶体结构中与B酸位处于同一个四面体的O11位置, 为氮原子的最佳取代位置, 因此氮化后分子筛表面的B酸强度得到较大程度的减弱.     

浸渍法制备的Mo/ZSM-5催化剂中Mo的分布状态

 通过多晶XRD利用Rietveld方法测定和精修了浸渍法制备的Mo/ZSM-5催化剂样品的物相和晶体结构. 结果表明,Mo物种在ZSM-5分子筛中以3种形式存在. 一种是以［Mo5O12］6+形式存在于ZSM-5分子筛的孔道内,每个分子筛晶胞中平均含0.4个［Mo5O12］6+单元. 这些单元覆盖了分子筛孔道内的部分B酸中心,使其B酸量及总酸量减少,但使L酸量增加; ［Mo5O12］6+团中Mo的含量约占Mo/ZSM-5催化剂质量的3.03%. 其余的两种Mo物种分别以α-MoO3晶相和无定形氧化钼形式存在,修饰分子筛的外表面.     

HZSM-5分子筛上乙基叔丁基醚合成反应的理论研究

采用ONIOM (B3LYP/6-31G(d,p):UFF)分层计算的方法, 研究了HZSM-5 分子筛上乙醇和异丁烯合成乙基叔丁基醚(ETBE)的反应机理. 通过反应物在HZSM-5 分子筛上吸附性质的研究发现, 乙醇与分子筛酸性位相互作用形成氢键, 而异丁烯则作用在Brönsted 酸位上形成π配位吸附. 确定反应物吸附位置后, 进一步探索反应机理, 结果表明: HZSM-5分子筛上乙醇和异丁烯合成乙基叔丁基醚的反应为协同反应, 并且, 反应物吸附顺序的不同对反应过程存在一定的影响. ETBE合成反应的最优途径以反应物同时吸附形成的复合物作为起点. 在反应过程中, 形成π配位的H原子向异丁烯分子中不饱和双键的端位C原子靠近, 被吸附的乙醇分子中的O原子向异丁烯双键中的另一个C原子靠近, 直到形成C－O键, 生成ETBE. 这一过程中, 原有的质子H加成到异丁烯的端基C上形成C－H键, 而原醇羟基中的H和B酸位附近的O原子作用形成新的酸性位. 相应的协同反应的最低的反应势垒为25.14 kJ·mol^-1.     

H(M)ZSM-5杂原子分子筛的表面酸性和裂解催化行为

用IR和ITPD技术研究了H(Al)ZSM-5、H(Ga)ZSM-5和H(Fe)ZSM-5杂原子分子筛的表面酸性。结果表明,这些分子筛表面既存在B酸中心,也存在L酸中心,但是就两种酸的表面浓度比值C_L/C_B而言,H(Ga)ZSM-5和H(Fe)ZSM-5要比H(Al)ZSM-5高得多。在十五烷裂解时,L酸中心起的作用可能更大。     

B、Al、Ga同晶取代丝光沸石的从头计算

用从头计算Hartree Fock方法研究了B、Al、Ga等同晶取代进入丝光沸石骨架后可能存在的位置,确定了与电荷平衡质子结合的氧位置,考察了B、Ga等杂原子进入骨架对丝光沸石Brnsted酸性的影响.能量分析表明B、Al、Ga在丝光沸石骨架中最容易进入T3和T4位;当Al、Ga在T4位时,质子与O10结合为能量最低即最稳定结构,而当B在T4位时,质子与O2或O10结合比较稳定.质子亲合势分析表明与硅铝丝光沸石相比, B和Ga进入骨架导致丝光沸石分子筛的Brnsted酸性有所减弱,其酸性依次为：B ZSM 5Ga ZSM 5< Al ZSM 5.     

镧改性提高ZSM-5分子筛水热稳定性

基于12T 团簇模型, 利用密度泛函理论(DFT)研究了ZSM-5 分子筛的水解脱铝机理以及镧改性提高ZSM-5分子筛水热稳定性的机理. 对未改性分子筛水解脱铝机理的研究表明, 首先是第一个水分子吸附在分子筛表面的酸性位上, 对分子筛的Al—O键起弱化作用, 使Al—O键伸长; 接着第二个水分子吸附到分子筛表面,分别与第一个水分子和分子筛骨架形成氢键, 进一步弱化与其最邻近的Al—O键, 并引致该键断裂. 同样, 其它的三个Al—O键也被削弱并逐一断裂, 从而发生分子筛水解脱铝现象. 引入的镧物种与分子筛骨架的四个O原子成键, 将铝包埋, 增加了分子筛孔壁厚度, 增大了水分子攻击铝的空间位阻, 抑制了水分子对Al—O键的弱化, 从而延缓Al—O键的断裂, 提高分子筛的水热稳定性. 计算的水分子吸附能和水解能进一步证实镧的引入提高了ZSM-5分子筛的水热稳定性.     

无粘结剂ZSM-11催化剂上异丁烯直接胺化生成叔丁胺

叔丁胺是一种重要的化工原料和中间体,广泛应用于制备橡胶促进剂、医药、农药和着色剂等下游产品.异丁烯在分子筛催化剂上直接胺化生产叔丁胺是一个经济环保过程,其中ZSM-5和BEA分子筛的催化性能优于其它系列分子筛.ZSM-11与ZSM-5分子筛具有相似的孔道结构,我们以前的实验结果表明,与ZSM-5相比,ZSM-11表现出更优越的芳构化反应性能,在干气中乙烯低温芳构化方面也有明显优势.在此基础上,我们进行无粘结剂ZSM-11分子筛催化剂合成,并应用于异丁烯直接胺化生产叔丁胺反应.传统水热技术合成的分子筛通常为粉末,机械强度不能达到实际应用的要求,在工业化过程中分子筛粉末一般需要加入粘结剂成型使其具备一定的机械强度和形状,但是粘结剂会降低分子筛催化剂的活性和选择性,有可能会引发一些副反应,因此无粘结剂分子筛催化剂引起人们广泛关注.无粘结剂分子筛是指分子筛颗粒中不含惰性粘结剂或只含有少量粘结剂,主要依靠分子筛晶粒间的相互作用支撑存在,具有一定形状、尺寸和机械强度的催化材料.无粘结剂分子筛催化剂中分子筛含量较高,可利用的有效表面积较大,在离子交换及工业催化等方面具有明显优势.本文采用水热合成的ZSM-11分子筛原粉与二氧化硅机械混合(ZSM-11/SiO2=70/30)挤条后,通过气固相合成法制备了无粘结剂ZSM-11分子筛催化剂(Cat-C).作为对比,还分别制备了ZSM-11和SiO2机械混合(ZSM-11/SiO2=70/30)样品HZSM-11+SiO2及ZSM-11和氧化铝机械混合(ZSM-11/Al2O3=70/30)样品HZSM-11+Al2O3.利用X射线衍射、透射电镜、NH3程序升温脱附和吸附吡啶红外光谱等对分子筛催化剂的物理化学性能进行了表征.同时,以这些分子筛样品为催化剂,在固定床反应装置上进行了异丁烯胺化反应评价,反应条件为270℃,5.0 MPa,氨烯比为4和异丁烯空速0.5 h?1.结果表明,与HZSM-11+SiO2和HZSM-11+Al2O3相比,Cat-C上叔丁胺生成速率最高.关联催化剂物化性能和反应性能发现,催化剂孔道结构与叔丁胺生成并不存在明显的关联性,而较多的Br?nsted酸和较少的Lewis酸才是Cat-C具有良好反应性能的主要原因.具有一定机械强度的无粘结剂ZSM-11分子筛催化剂制备简单,在异丁烯直接胺化过程中叔丁胺生成速率高,具有很好的工业化应用前景.     

第一性原理研究镍改性ZSM-12分子筛的酸性(英文)

分子筛被用作工业催化剂时常需要过渡金属改性,镍是制备加氢/脱氢催化剂常用的过渡金属,本研究采用密度泛函理论研究镍改性的ZSM-12分子筛的结构和酸性。结果表明,分子筛的B酸质子可以被镍原子还原成氢分子,而Ni₂的团簇不能将B酸质子还原生成氢气分子。镍原子在分子筛内会被氧化,并形成Lewis酸性位,这会导致分子筛骨架铝的Lewis酸性变弱,镍改性后,分子筛吸附氢气的能力变强,被吸附的氢分子解离为氢原子,并带负电荷,不再具有B酸的功能。从计算的氨分子的吸附能来判断,由于吸附的氢会从镍原子得到电子,吸附的氢分子会增强镍原子的Lewis酸性。     

含氮FAU分子筛的制备、表征及碱催化反应性能

利用脱水氮化法制备了含氮HY分子筛,氮化后分子筛的结晶度和比表面积均得到较好保持.由于氮原子的电负性低于氧原子,氮原子取代氧原子进入HY分子筛的骨架,使其Lewis碱性得到增强.利用氨气吸附红外光谱、二氧化碳吸附红外光谱与二氧化碳程序升温脱附方法对氮化前后的分子筛进行表征.结果表明氮化后HY分子筛的L酸中心数量有所降低,B酸中心数量有所增加,同时生成新的碱性中心.由于新碱性中心的引入,含氮HY分子筛在Knoevenagel缩合碱性探针反应中表现出优异的活性.     

Cu-ZSM-5型分子筛的合成与结构表征

近年来，杂原子ZSM-5分子筛合成研究发展极为迅速，许多原子例如B、Ge、Fe等取代铝或佳而进入了分子筛骨架[1-4]．特别是1986年Guth等人间报导在弱酸性体系氟离子存在下合成分子筛，为杂原子沸石分子筛的合成开辟了一条新途径．在碱性体系下，Ione等人[6,7]报导过含铜ZSM-5的合成，但铜是否进入分子筛骨架，尚未给出确切的说明．在微酸性介质中合成Cu－ZSM-5还未见报导．本文在弱酸性介质氟离子存在下，应技合成出氨型Cu-ZSM-5分子筛，并运用XRD、IR、SEM、XPS等方法证明了铜进入了分子筛骨架．1实验1．1试剂白炭．t（SIO。，…     

硼和氟掺杂ZSM-5分子筛的制备及其甲醇制丙烯反应性能

采用两步水热晶化法,通过在合成体系中加入硼酸、氟化铵、氟硼酸铵,合成出了硼和氟改性的ZSM-5分子筛。利用X射线衍射、氮气吸附-脱附、29Si固体核磁共振波谱、傅里叶变换红外光谱、扫描电子显微镜以及NH₃程序升温脱附等测试手段对样品进行了表征。结果表明：硼和氟掺杂条件下可以合成具有较高结晶度的ZSM-5分子筛,杂原子掺杂提高了分子筛的硅铝比;硼和氟掺杂可以显著降低ZSM-5分子筛的Lewis酸量,但提高了Brønsted酸量;硼和氟共同作用可以降低ZSM-5分子筛的颗粒尺寸。甲醇制丙烯评价结果显示：较低的Lewis酸量和适宜的Brønsted酸性有利于提高丙烯选择性和催化剂寿命;NH₄BF₄改性的ZSM-5分子筛（Z5-BF2）表现出较高的丙烯选择性和较长的催化剂寿命。     

Study on antimony oxide self-assembled inside HZSM-5

Sb/ZSM-5 was obtained by solid-state reaction with the mixture of Sb₂O₃ and zeolite HZSM-5 under a dry nitrogen flow at 773 K. Characterization of the treated zeolite was undertaken with XRD, ²⁷Al MAS NMR, BET, TGA and FT-IR. The results revealed that part of the antimony oxides migrated into the channels of zeolite, and decreased the Brönsted acid sites in Sb/ZSM-5 remarkably. The other part of antimony oxides together with the amorphous alumino-silicate in the products distributed on the external surface of zeolite ZSM-5 and modified it, while the framework of ZSM-5 in crystal phase was retained. The structure of occluded antimony oxide inside the channels of ZSM-5 was studied by XRD Rietveld method. The result showed that their structure can be described as a chain of non-perfect [Sb₅O₅(H₂O)₂]_n⁵ⁿ⁺, which is parallel to the straight channel of ZSM-5. There is about 0.6 [Sb₅O₅(H₂O)₂]⁵⁺ unit in every cell of the ZSM-5 on an average.     

Investigation of catalytic property in the t-butylation of 1,2-dihydroxybenzene using FT-IR and XPS study

Catalytic properties of HZSM-5s with three different Na⁺ ion-exchange levels and SiO₂ /Al₂O₃ ratios used in tert-butylation of DHB (1,2-dihydroxybenzene) are interpreted through pyridine adsorbed FT-IR and XPS study. The DHB conversion decreases as increment of degree of Na⁺ ion-exchange level and of Si content in HZSM-5. Catalytic properties with respect to Na amount in ZSM-5 are more sensitive than those of HZSM-5s with different SiO₂/Al₂O₃ ratios. But selectivity for 4-TBC (4-t-butylcatechol) is not changed significantly. Acidic properties, i.e. acid strength and acid density are characterized by pyridine adsorbed FT-IR and XPS study. Based on FTIR and XPS analyses, DHB conversion and selectivities for DTBC (3,5-di-t-butylcatechol) and 3-TBC (3-t-butylcatechol) depend on type and strength of acid sites, with the result that strong Brønsted acid rather than weak Brønsted or Lewis acid sites are more closely related to the conversion. Furthermore, t-butyl alcohol is selectively adsorbed on the Brønsted acid site of FT-IR band at 3612 cm^-1, which signifies that the Brønsted acid site is the active site. The mechanism for t-butylation of DHB is suggested based on the FT-IR results of adsorption/desorption of reactants.     

Synthesis of [B,Al]-EWT-Type Zeolite and Its Catalytic Properties

EWT zeolite belongs to ultra-large pore zeolite with the 10MR and 21MR channels, which has good thermal stability, certain acid strength and good application prospects in petroleum refining and petrochemical reactions. However, EWT zeolite has fewer medium/strong acid sites, especially Brönsted acid sites, which makes it difficult to apply to acid-catalyzed reactions. The regulation of acid amount and distribution was achieved by boron and aluminum substitution into the siliceous framework of EWT. The physico-chemical properties of the samples were characterized by XRD, SEM, N₂ adsorption-desorption, XRF, ICP, Py-IR, NH₃-TPD and ¹¹B & ²⁷Al & ²⁹Si MAS NMR. The results show that quantities of boron and aluminum elements can occupy the framework of [B,Al]-EWT to increase the density of medium and strong acid centers, with more acidity and Brönsted acid centers than EWT zeolite. In the reaction of glycerol with cyclohexanone, the conversion of the sample (U-90-08-10/U-90-H-HCl) is significantly higher than that of the EWT sample, approaching or exceeding the Beta zeolite. A catalytic activity study revealed a direct correlation between the Brönsted acidic site concentration and the activity of the catalyst. The U-90-08-10-H catalyst was also considerably stable in the catalytic process. This work shows, for the first time, that extra-large pore zeolites can be used in industrial acid-catalytic conversion processes with excellent catalytic performance.     

Interactions of phosphorous molecules with the acid sites of H-Beta zeolite: Insights from solid-state NMR techniques and theoretical calculations

The local structures of various Brønsted and Lewis acid sites in H-Beta zeolite were resolved with the combined ³¹P MAS NMR, ³¹P–²⁷Al TRAPDOR NMR experiments and theoretical calculations at different levels. In addition, the interacting mechanisms of these acid sites with probe molecules such as trimethylphosphine (TMP) and trimethylphosphine oxide (TMPO) were clarified, which greatly aids the understanding of acid catalysis. Owing to the narrow chemical shift range and close Brønsted acid strengths, only an average resonance at −4.5 ppm was observed in TMP adsorbed H-Beta zeolite, consistent with the calculated data of acidities (substitution energies and proton affinities), geometries, adsorption energies as well as ³¹P chemical shifts. However, two types of Brønsted acids were distinguished by TMPO, and the HF/DZVP2 (MP2/DZVP2) chemical shifts were calculated at 68.1 (69.5) and 69.7–72.1 (71.7–74.9) ppm, respectively. Two types of Lewis acids were identified at −32.0 and −47.0 ppm with the latter exhibiting strong ³¹P–²⁷Al TRAPDOR effects. With theoretical calculations, these two peaks were attributed to the extra-lattice oxo-AlOH²⁺ species and the three-fold coordinated lattice-Al, extra-framework Al(OH)₃, oxo-AlO⁺ species, respectively. The peak at −60.0 ppm was conventionally assigned to the TMP physisorption, but the calculations indicated that the EFAL monovalent Al(OH)₂⁺ species coordinating with two lattice-O atoms near the framework Al atom can contribute to it as well.     

The nature of active sites in high-silica zeolites containing platinum and cobalt nanoparticles

The calculations of interaction of Co₆ and Pt₆ nanoparticles with silicalite ZSM-5 and zeolite HZSM-5 were performed by the density functional theory method. Introduction of cobalt or platinum to silicalite slightly stabilizes the metal cluster and induces a small positive charge on the Co₆ particle and an appreciable negative charge on the Pt₆ particle. In the case of cobalt, the interaction of the metal particle with the acid zeolite is accompanied by a proton transfer from the Brønsted acid site to the surface of the metal cluster, resulting in the formation of a hydride-like structure, whereas in the Pt-zeolite system a complex cation containing adsorbed hydrogen atom is formed.     

ZSM-5分子筛催化1-己烯生成cis-2-己烯的理论研究

基于54T团簇模型, 采用ONIOM分层计算方法, 研究了1-己烯在ZSM-5分子筛上进行顺式双键异构的反应机理. 计算结果表明, 1-己烯的顺式双键异构反应通过只有分子筛Brønsted酸部分起作用的机理进行. 首先, 1-己烯与分子筛的Brønsted酸性位形成π配位复合物. 接着, 酸质子发生迁移使1-己烯的双键端基碳原子被质子化, 同时双键的另一碳原子与失去质子的Brønsted酸羟基的氧原子成键, 形成稳定的烷氧基中间体. 然后, 烷氧基中间体中的C―O共价键被打断, 同时Brønsted酸羟基的氧原子从C₆H₁₃基团提取一个氢原子还原分子筛的酸性位, 并且生成cis-2-己烯. 这一反应路径与借助于分子筛活性位的酸-碱双功能性质的反应路径是相互竞争的. 计算得到的表观活化能是59.37 kJ·mol^-1, 该值与实验值非常接近. 这一结果合理解释了双键异构过程中的能量特征, 并且扩展了对分子筛活性位本质的理解.     

Surface Structure and Catalytic Performance of CuCl/SiO2-Al2O3 Catalysts for Methanol Oxidative Carbonylation

Aluminum was doped into amorphous silica gel to modify its surface structure. The obtained SiO₂-Al₂O₃ support was used to prepare the CuCl/SiO₂-Al₂O₃ catalyst by solid-state ion exchange, and the catalyst activity for liquid-phase oxidative carbonylation of methanol to dimethyl carbonate was investigated. The results showed that the prepared SiO₂-Al₂O₃ support kept the amorphous structure of the silica gel. The BET specific surface area of the silica gel was decreased to 200 m²/g, and the surface acid sites (including Brønsted acid sites) were increased. In the CuCl/SiO₂-Al₂O₃ catalyst, CuCl was not only dispersed on surface but also was ion exchanged with surface Brønsted acid sites of the SiO₂-Al₂O₃ support to form Cu⁺ species, which resulted in a decrease in BET specific surface area to 148 m²/g. These two kinds of Cu⁺ species on the catalyst surface were both active centers for the oxidative carbonylation of methanol to dimethyl carbonate. When the catalyst was prepared with Si/Al molar ratio of 5 and was calcined at 500 °C, the selectivity and space-time yield of dimethyl carbonate reached 74% and 1.27 g/(g·h), respectively.     

The formation mechanism of Mo-methylidene species over Mo/HBeta catalysts for heterogeneous olefin metathesis: A density functional theory study

Density Functional Theory (DFT) calculations were performed to optimize the Mo active sites in HBeta zeolite catalysts as well as to locate the reaction pathways to form the Mo-methylidene species. Two different Mo active sites, i.e., the oxidized Mo^VIO₂ and its reduced form Mo^VO(OH), were developed and incorporated into HBeta zeolites by replacing a pair of Brønsted acidic sites. The Mo-methylidene species were found to be produced through two elementary reaction steps, and the Mo-oxametallacyclobutanes were identified as the intermediates. The activation barriers of the decompositions of the oxametallacyclobutane intermediates (Step 2) were estimated to be higher than those of the ethene addition on the Mo active sites (Step 1). The oxidation states of the Mo centers exerted marked influences on the stabilities of the intermediates as well as on the activation barriers and reaction heats of Steps 1 and 2, which were elucidated by the electronic properties of the O_b-ligands directly bonded to the Mo centers. Both free energy barriers and reaction heats have indicated that the whole processes of generating the Mo-methylidene species were preferred over the Mo(VI) rather than Mo(V) active site. Accordingly, the Mo(VI) active site was more efficient in catalyzing the formation of Mo-methylidene species in the heterogeneous Mo/HBeta catalytic systems.