水汽和空气焙烧制备LaY沸石的SiCl4气相超稳研究

为了考察不同焙烧条件制备的LaY沸石在SiCl₄气相超稳后性能的差异，采用离子交换和氨水沉淀相结合的方法将La离子负载到NaY沸石上，经水蒸汽焙烧或空气焙烧得到不同La负载量的LaYS和LaYB沸石，再经过SiCl₄气相超稳改性得到DLaYS和DLaYB沸石.XRD数据表明水蒸汽焙烧能使沸石发生更为明显的骨架脱铝；不同La负载量的LaY沸石经SiCl₄气相超稳改性都能顺利实现晶胞收缩.XRF数据表明气相超稳和洗涤过程伴随着稀土La的大量流失，DLaYB沸石中的La流失量相对较小.NH₃-TPD和Py-IR数据表明La负载量相同时，DLaYS沸石的总酸量少于DLaYB沸石的总酸量.固定流化床重油催化裂化评价结果显示，与参比催化剂相比，DLaYS催化剂和DLaYB催化剂都具有汽油收率高、柴油收率低，及总轻质油收率高的特点.La负载量相同时，DLaYS催化剂的汽油收率低于DLaYB催化剂.     

硅烷化对NH3选择性催化还原NOx催化剂CuCe/BEA水热稳定性的促进作用

采用硅烷化改性NH₃选择性催化还原NO_x催化剂CuCe/BEA,以提高催化剂的水热稳定性。X射线衍射、扫描电子显微镜和²⁷Al核磁共振谱图等研究证实,硅烷化改性明显抑制BEA分子筛骨架中Si-O-Al键的水解,保持其结构完整,从而有效提高水热处理后CuCe/BEA的催化活性。氨气-程序升温脱附和原位漫反射傅里叶变换红外光谱研究结果表明,硅烷化改性的催化剂由于保持更完整的骨架结构能够形成更多的酸性位点。此外,氢气-程序升温还原和X射线光电子能谱测试表明,硅烷化改性有利于提高活性铜物种的分散性。因此,相比于CuCe/BEA催化剂,硅烷化改性的CuCeSi/BEA催化剂具有更多的酸性位点和高度分散的Cu物种,共同促进了催化剂的水热稳定性。     

La 或 Ce 增强 Y型分子筛结构稳定性的机制

 采用 X 射线粉末衍射、²⁹Si 固体核磁共振、X 射线光电子能谱和扫描电镜及能谱等方法研究了 La, Ce 增强 Y 分子筛结构稳定性的差异. 结果表明, La 和 Ce 的引入均可稳定 Y 分子筛的骨架结构, 但 La 离子比含量相当的 Ce 离子更容易进入分子筛内部和抑制骨架铝的脱除, 因而对分子筛结构的稳定作用更优. 结合量子力学密度泛函计算方法, 从理论上阐述了这种增强机制, 即La 或 Ce 的引入能显著增加分子筛骨架 Al 和相邻 O 原子的作用力, 有效稳定分子筛骨架 Al 位, 并且稀土离子与分子筛间存在较强的作用力; 与 Ce 相比, La 与分子筛的相互作用更大, Al–O 作用力更强, 因此, La 比 Ce 更有利于稳定分子筛的骨架结构.     

低硅铝比ZSM-5分子筛的合成及其正庚烷裂化反应性能

以氨水为矿化剂,通过添加NH₄⁺离子水热合成了具有较低骨架硅铝比的ZSM-5分子筛。通过X射线衍射(XRD)、扫描电镜(SEM)、固体核磁共振(MAS-NMR)等表征手段,研究了硅源、铝源、矿化剂、阳离子等对ZSM-5分子筛的结晶度、形貌尺寸和骨架硅铝比等的影响,研究了ZSM-5分子筛的骨架硅铝比对正庚烷催化裂化反应的影响。研究表明,投料硅铝比越低,铝原子越难进入到分子筛骨架中;当氨水为矿化剂、正硅酸四乙酯为硅源时可以合成骨架硅铝比较低的氢型ZSM-5分子筛,添加NH₄⁺离子可以增强骨架铝的嵌入,进一步降低分子筛的骨架硅铝比(24.2)。正庚烷裂化反应结果表明,降低分子筛的骨架硅铝比可以提高正庚烷裂化反应的活性,但会降低低碳烯烃的选择性。     

FCC催化剂中REHY分子筛的结构与酸性

 用XRD,N2吸附,NH3-TPD和Py-IR等手段对REHY分子筛进行了表征,并通过多晶XRD法测定了稀土离子在Y分子筛骨架外的分布. 结果表明,在含水条件下,定位于Y型分子筛β笼SⅠ′ 位的RE3+与骨架氧及定位于SⅡ′ 位的H2O配位,稳定了分子筛的骨架,减少了分子筛酸性中的最强酸部分;定位的RE3+通过极化定位的配位水,增加了分子筛的中强酸,减缓了RE3+取代H+所引起的酸量下降. 从结构测定可推测出,在FCC催化剂中Y型分子筛上RE3+的最佳量应为每个晶胞含11个稀土离子,并完全定位于β笼的SⅠ′ 位.     

MnO2的晶相结构和表面性质对低温NH3-SCR反应的影响

采用水热法合成了两种具有相同形貌但是不同物相结构的MnO₂纳米棒, 分别为隧道状和层状结构, 考察其低温NH₃选择性催化还原NO_x (NH₃-SCR)的性能. 结果表明MnO₂纳米棒的比表面积不是影响活性的主要因素, 催化剂的晶相结构和表面性质对催化活性有很大影响, 隧道状α-MnO₂纳米棒的低温NH₃-SCR活性明显高于层状δ-MnO₂纳米棒. 结构分析和NH₃程序升温脱附(NH₃-TPD)实验表明, α-MnO₂纳米棒的暴露晶面(110)面存在大量的配位不饱和Mn离子, 形成较多的Lewis 酸性位点, 而且α-MnO₂较弱的Mn―O键和隧道结构都有利于NH₃的吸附; 而δ-MnO₂纳米棒的暴露晶面(001)面上的Mn离子已达到配位饱和, 所以其表面Lewis 酸性位点较少. X射线光电子能谱(XPS)和热重(TG)分析表明α-MnO₂纳米棒的表面更有利于NH₃和NO_x的活化. 具有有利于吸附NH₃和活化NH₃和NO_x的表面性质和晶型结构, 是α-MnO₂纳米棒活性高的主要原因.     

焙烧温度对MnOx-CeO2-WO3-ZrO2催化剂上NH3选择性还原NO的影响

采用共沉淀法制备了MnO_x-CeO₂-WO₃-ZrO₂催化剂,考察了催化剂焙烧温度对O₂和H₂O存在下NH₃选择性催化还原（NH₃-SCR） NO的影响,并利用低温N₂吸附、X射线衍射（XRD）、透射电镜（TEM）、X射线光电子能谱（XPS）、NH₃程序升温脱附（NH₃-TPD）和CO脉冲反应对催化剂进行了表征. 结果表明在NH₃-SCR反应中,催化剂的低温活性随焙烧温度的提高而降低,这是由于催化剂表面化学吸附氧和酸性位减少引起的;催化剂的高温活性随焙烧温度的提高先增加后减小,这与催化剂表面最易释放氧数量的变化趋势相反. 700 ℃焙烧的催化剂具有良好的低温活性和最宽的反应温度窗口,在空速为90000 h^-1的条件下,该催化剂的起燃温度（50% NO转化率）为189 ℃,且反应温度在218-431 ℃范围内,NO转化率可达到80%-100%.     

NH3-SCR反应过程中NH3和NOx在Cu/SAPO-34分子筛催化剂上的吸附特性和作用

通过离子交换法制得Cu/SAPO-34菱沸石分子筛催化剂, 同时研究了NH₃和NO_x (NO和NO₂)在该催化剂上的吸附位、吸附强度、吸附量和吸附速率, 得到了不同反应气氛在Cu/SAPO-34 上的吸附性能及其在NH₃选择性催化还原(NH₃-SCR)反应中的作用. 研究采用瞬态实验、程序升温脱附(TPD)和漫反射傅里叶变换红外光谱(DRIFTS)等方法进行表征实验. 瞬态实验结果表明NH₃是吸附性气体. 程序升温脱附实验和红外漫反射实验结果表明NH₃可以吸附在布朗斯特和路易斯酸性位上形成不同的NH₃物种, 它们显示不同的SCR活性. NH₃在Cu²⁺上的吸附速率最快, 且键强最强. NO_x可以氧化并以硝酸盐/亚硝酸盐的形式吸附在Cu物种上. 最后, 本文讨论了NH₃选择性催化还原反应过程中在Cu物种上的中间物种并推测反应机理.     

酸处理对CuY催化剂孔结构及氧化羰基化性能的影响

对NaY分子筛(n_Si/n_Al=2.65)进行了草酸脱铝处理并作为载体采用液相离子交换法制备CuY催化剂, 应用于常压甲醇氧化羰基化合成碳酸二甲酯(DMC)反应。NaY分子筛及其CuY催化剂通过N₂低温吸附-脱附、透射电子显微镜、X射线衍射、²⁹Si固体核磁共振、NH₃吸附程序升温脱附、吡啶吸附红外光谱、H₂程序升温还原、原子吸收等方法进行表征。研究结果表明, 酸处理NaY分子筛后, 骨架铝被脱除, 导致骨架n_Si/n_Al比增加、相对结晶度降低并产生介孔, 有利于产物分子的扩散, 从而影响催化活性。采用4 h、2 mol·L^-1草酸处理NaY分子筛作为载体制备的CuY催化剂显示出较高的催化性能, DMC时空收率和甲醇转化率分别从103.6 mg·g^-1·h^-1和6.3%增加到184.9 mg·g^-1·h^-1和10.2%。产生的介孔能够促进催化剂中铜活性位的可接近性及反应物分子和产物分子的扩散。     

氟硅酸铵改性纳米HZSM-5分子筛催化甲醇制丙烯

在静态条件下, 采用不同浓度的氟硅酸铵溶液对纳米ZSM-5分子筛进行了改性处理. 利用粉末X射线衍射(XRD)、²⁷Al 魔角旋转固体核磁共振(²⁷Al MAS NMR)、X射线荧光光谱(XRF)、X射线光电子能谱(XPS)、N₂ 吸附、透射电镜(TEM)、NH₃程序升温脱附(NH₃-TPD)、吡啶吸附红外光谱(Py-IR)等技术对改性前后纳米ZSM-5分子筛的骨架结构、织构性质、酸性质进行了表征. 并在常压、反应温度为450℃、甲醇质量空速(WHSV)为1 h^-1的条件下, 研究了改性前后纳米HZSM- 的甲醇制丙烯(MTP)催化性能. 结果表明, 合适浓度的氟硅酸铵处 理能够选择性地脱除纳米ZSM-5 分子筛的外表面铝, 从而使得HZSM-5 的酸密度降低, 比表面积和孔容增大, MTP催化性能显著提高. 氟硅酸铵改性后纳米HZSM-5 的丙烯选择性和丙烯/乙烯(P/E)质量比分别由原来的 28.8%和2.6提高到45.1%和8.0, 催化剂寿命增加了近2倍.     

Influence of chemical dealumination on the properties of USY zeolite

Three series of dealuminated Y zeolites have been prepared by chemical extraction ofhydrothermally dealuminated Y zeolite(USY)with H_2Na_2EDTA,HCl and H_4EDTA.The unitcell constant,mesopore distribution,acidity and extraframework aluminum(EFAL)of thezeolites were studied with XRD,chemical analyses,adsorption,IR and NH_3-TPD techniques.It was shown that H_2Na_2EDTA only removed EFAL species deposited in the pores of USY,by contrast,HCl and H_4EDTA extract both extraframework and framework aluminum,andmake the zeolite framework further dealuminated.Adsorption tests gave evidence that a second-ary pore system exists in these dealuminated zeolites.H_2Na_2EDTA extraction increased bothmicropore and mesopore volumes,but after HCl and H_4EDTA treatments,new mesopores formedand the micropore volume was decreased.The pyridine-IR and NH_3-TPD measurements demon-strated that EFAL had no evident contribution to the zeolite acidity.     

Extraction of rare-earth nitrates by phosphoryl podands

The distribution of trace amounts of rare-earth nitrates between aqueous solutions of NH₄NO₃ and organic solutions of phosphoryl podands is studied for Ln = La, Ce, Pr, Nd, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu, and Y. The stoichiometry of the extraction complexes is determined. The effect of the structure of the extractant and the nature of the organic solvent on the efficiency of rare-earth recovery to the organic phase is considered.     

Author index for volume 52

Dehydrated samples of zeolite Y containing alkali-metal cations have been reacted with alkali-metal vapor in sealed silica tubes, and the products studied by electron-spin resonance (ESR) spectroscopy. Two distinct species were detected following the reaction of sodium-exchanged zeolite Y with sodium, potassium, or rubidium vapor. Exposure to a low concentration of metal vapor resulted in brightly colored samples with ESR signals characteristic of a stable ionic cluster species Na³⁺₄, in which an unpaired electron is trapped on four equivalent sodium cations in the sodalite cages of the zeolite. Exposure to higher concentrations of metal vapor resulted in dark-colored samples with ESR signals characteristic of small metallic particles located inside the zeolite cavities. A similar ionic cluster species K³⁺₄ was detected following the reaction of potassium-exchanged zeolite Y with sodium or potassium vapor although the potassium cluster was less stable than its sodium counterpart and an ESR signal from small metallic particles was observed at the same time. The corresponding Rb³⁺₄ ionic cluster species was not detected following the reaction of rubidium-exchanged zeolite Y with rubidium vapor; only an ESR signal from small metallic particles was observed. The narrow linewidths of the ESR signals from the small metallic particles suggest an inhibition of the spin-relaxation mechanisms in the bulk metals.     

Formation of Mesopores in USY Zeolites: A Case Revisited

Steaming of NH₄Y zeolite at 723 K and 873 K is accompanied by the formation of extra‐framework amorphous aluminosilicate and silica gel in addition to earlier observed extra‐framework aluminum species. Their occurrence is directly associated with the formation of mesopores. Bulk (intracrystalline) mesopores occur inside the crystallite nuclei and surface (intercrystalline) mesopores are located nearby the crystallite surface. Corrosion of the zeolite framework results in a loss of crystallinity and, consequently, decreased catalytic activity of the USY catalysts synthesized. Analysis of the reasons of mesopore formation may help to reduce these disadvantages.     

Evaluation of Co/SSZ-13 Zeolite Catalysts Prepared by Solid-Phase Reaction for NO-SCR by Methane

Co/SSZ-13 zeolites were prepared by heating the finely dispersed mixture of NH₄-SSZ-13 and different cobalt salts up to 550 °C. Investigations by thermogravimetry – differential scanning calorimetry – mass spectrometry provided new insight into details of the solid-state reaction. Formation of Co carrying hydrate melt or volatile species was shown to proceed from chloride, nitrate, or acetylacetonate Co precursor salts upon thermal treatment. This phase change allows the transport of the Co species into the zeolite pores. The reaction of the NH₄⁺ or H⁺ zeolite cations and the mobile Co precursors generates vapor or gas products, readily leaving the zeolite pores, and cobalt ions in lattice positions suggesting that solid-state ion-exchange is the prevailing process. The obtained catalysts are of good activity and N₂ selectivity in the CH₄/NO-SCR reaction. The thermal treatment of acetate or formate salts give solid intermediates that are unable to get in contact and react with the cations in the zeolite micropores. These catalysts contain mainly Co-oxide clusters located on the outer surface of the zeolite crystallites and have poor catalytic performance.     

甲基噻吩在HY分子筛上的吸附、脱附及转化行为

由NH₄Y分子筛制备了HY分子筛,运用N₂吸附、NH₃-TPD和Py-FTIR等手段表征HY分子筛的物化性能;采用智能重量分析仪(IGA)方法研究了甲基噻吩(2-甲基噻吩、3-甲基噻吩)在HY分子筛上的吸附-脱附行为;采用程序升温脱附-质谱(TPD-MS)联用手段研究了甲基噻吩在HY分子筛上的转化行为。结果表明,在200 ℃下 2-甲基噻吩和3-甲基噻吩在HY分子筛中的强B酸上发生强化学吸附作用,与B酸结合后生成了甲基噻吩的碳正离子结构进而发生了歧化反应、脱烷基反应以及裂化反应;与2-甲基噻吩不同的是,3-甲基噻吩与HY通过一定的氢转移反应生成了3-甲基四氢噻吩,且200 ℃吸附条件下3-甲基噻吩比2-甲基噻吩更容易发生裂化反应。     

Phase Transitions,Prominent Dielectric Anomalies,and Negative Thermal Expansion in Three High Thermally Stable Ammonium Magnesium–Formate Frameworks

We present three Mg–formate frameworks, incorporating three different ammoniums: [NH₄][Mg(HCOO)₃] ( 1 ), [CH₃CH₂NH₃][Mg(HCOO)₃] ( 2 ) and [NH₃(CH₂)₄NH₃][Mg₂(HCOO)₆] ( 3 ). They display structural phase transitions accompanied by prominent dielectric anomalies and anisotropic and negative thermal expansion. The temperature‐dependent structures, covering the whole temperature region in which the phase transitions occur, reveal detailed structural changes, and structure–property relationships are established. Compound 1 is a chiral Mg–formate framework with the NH₄⁺ cations located in the channels. Above 255 K, the NH₄⁺ cation vibrates quickly between two positions of shallow energy minima. Below 255 K, the cations undergo two steps of freezing of their vibrations, caused by the different inner profiles of the channels, producing non‐compensated antipolarization. These lead to significant negative thermal expansion and a relaxor‐like dielectric response. In perovskite 2 , the orthorhombic phase below 374 K possesses ordered CH₃CH₂NH₃⁺ cations in the cubic cavities of the Mg–formate framework. Above 374 K, the structure becomes trigonal, with trigonally disordered cations, and above 426 K, another phase transition occurs and the cation changes to a two‐fold disordered state. The two transitions are accompanied by prominent dielectric anomalies and negative and positive thermal expansion, contributing to the large regulation of the framework coupled the order–disorder transition of CH₃CH₂NH₃⁺. For niccolite 3 , the gradually enhanced flipping movement of the middle ethylene of [NH₃(CH₂)₄NH₃]²⁺ in the elongated framework cavity finally leads to the phase transition with a critical temperature of 412 K, and the trigonally disordered cations and relevant framework change, providing the basis for the very strong dielectric dispersion, high dielectric constant (comparable to inorganic oxides), and large negative thermal expansion. The spontaneous polarizations for the low‐temperature polar phases are 1.15, 3.43 and 1.51 μC cm^?2 for 1 , 2 and 3 , respectively, as estimated by the shifts of the cations related to the anionic frameworks. Thermal and variable‐temperature powder X‐ray diffraction studies confirm the phase transitions, and the materials are all found to be thermally stable up to 470 K.     

Thermoanalytical investigations on ion-exchanged Y-zeolites

NH₄Y and NH₄LaY-type zeolite catalysts were prepared by cyclic ion-exchange of a synthetic Linde Y-zeolite. The release of ammonia and water were followed by evolved gas analysis (automatic thermogastitrimetric equipment) as well as with a continuous selective water detector. The ion-exchangeability of NH ₄ ⁺ for La³⁺ on the zeolite was also investigated. The capacity of the NH₄Y-zeolite was found to be 3.60 mequiv./g calcined zeolite. After a three times repeated ion-exchange process, 88.9 % of the ammonia was replaced by lanthanum.     

Mesopores in USY Zeolites II

Microporous zeolites Na‐Y and K‐Y were converted into the NaNH₄‐Y and KNH₄‐Y modifications by ion exchange being active in dealumination. Removal of framework aluminium and silicon is accompanied by formation of secondary mesopores. Internal mesopores are formed in the centre of zeolite crystals and external pores at their surface. Formation of mesopores changes the sorption behaviour.Residual alkali metal cations as Na⁺ or K⁺ stabilise, however, the framework ≡Si‐O‐Al≡ bonds. Because of inhomogeneous distribution of sodium ions, in NaNH₄‐Y less internal but more external mesopores are formed. Potassium ions of KNH₄‐Y are more homogeneous distributed over the framework why a more balanced formation of secondary pores takes place.     

Halide abstraction reactions of tin(IV) chloride and the group 3 chlorides MCl3 (M = Sc,Y, La) in thf: crystal and molecular structure of [ScCl2(thf)4][SnCl5(thf)]

Direct treatment (1:1) of MCl₃ (M = Sc, Y or La) with SnCl4 in thf provides colourless compounds of the type ScSnCl₇(thf)₅ and MSnCl₇(thf)₆ (M = Y, La), which have been characterised by elemental analysis and spectroscopic studies. An X-ray determination of ScSnCl₇(thf)₅ reveals an ionic structure comprising individual six-coordinate [ScCl₂(thf)₄]⁺ cations and [SnCl₅(thf)]^-anions. The cations feature an octahedral metal geometry in which a linear Cl-Sc-Cl unit is surrounded by an equatorial girdle of four solvent (thf) molecules.