Conversion of acids to benzimidazoles with transition metal/zeolites

Transition metal/Y zeolites were prepared using microwave solid state and aqueous solution ion exchange methods. The activity of these zeolites was investigated in a conversion of acids to benzimidazoles reaction between 4-methyl-1, 2-phenylenediamine and 3-nitrobenzoic acid. The yield of these reactions increased in order of CuY < Fe²⁺Y < NiY < CoY < NaY < CrY < MnY < ZnY for both methods. The solid state ion-exchanged zeolites showed higher activity in comparison to the aqueous solution exchange. Yields of products in the presence of the ZnY zeolite were of the order of 69–83%. It seems that the Lewis sites are better sites compared to the Bronsted sites for this reaction.     

β沸石的铝化

β沸石自1988年结构被确定以来受到普遍重视,由干结构上的特殊性,G沸石既具有较强酸性又具有明显的碱性［‘,‘］．但q佛石的高硅铝比使其在化学组成上对碱性的贡献甚微,如果能降低其硅铝比,则有可能获得具有较强碱性的佛石分子筛．直接合成的o佛石,硅铝比一般在10以上．     

分子筛模型中非骨架离子位置的研究

从理论上研究了非骨架阳离子可能的分布位置．计算了分子筛晶体基本结构单元在整个空间的静电势分布，找出空间中静电势的各个极小点．在静电势最低点逐个放置钠离子，优化，重新计算模型分子筛的电势分布．研究了阳离子放置过程中静电势变化的趋势．     

杂原子Y分子筛的二次合成及其吸附脱硫性能

采用液-固相同晶取代反应制备了骨架含Ga的Y型分子筛, 并对其吸附脱硫性能进行了研究. 在室温, 空速为7 h−1的条件下, 镓化Y型分子筛([Ga]AlY)处理噻吩、四氢噻吩、4,6-二甲基二苯并噻吩(4,6-DMDBT)正壬烷溶液(硫含量500 μg•g−1), 每克吸附剂吸附硫的量分别为7.7、17.4、14.5 mg. 采用密度泛函理论(DFT)中的广义梯度近似方法(GGA)计算各分子中硫原子上的电荷数, 噻吩中硫原子的电荷数为−0.159, 而4,6-DMDBT和四氢噻吩分别为−0.214、0.298. 四氢噻吩和4, 6-DMDBT中硫原子上的电子密度大于噻吩中硫原子上的电子密度, 这就使得四氢噻吩和4,6-DMDBT中的硫原子与吸附位间的作用会远大于噻吩中的硫原子与吸附位间的作用, 吸附容量必然会大很多. 采用[Ga]AlY处理抚顺石油二厂的催化裂化汽油(硫含量：299 μg•g−1), 每克吸附剂处理2.1 mL汽油时, 处理后汽油的硫含量为54.8 μg•g−1, 说明[Ga]AlY对汽油脱硫有一定的效果.     

探针反应和FTIR法研究Pt与L型沸石的相互作用

探针反应和ＦＴＩＲ法研究Ｐｔ与Ｌ型沸石的相互作用董家禄,朱建华,须沁华,张婕,刘大壮（南京大学化学系,南京,２１０００８）（郑州工学院化工系,郑州,４５０００２）关键词Ｐｔ／Ｌ沸石,沸石催化剂,异丙醇分解反应,Ｐｔ－载体相互作用Ｐｔ的分散度和电子状态...     

Synthesis and complexing properties of a double-calix[4]arene crown ether

The template synthesis of copper(II) phthalocyanine by the condensation of dicyanobenzene within the supercages of Cu(II) exchanged X and Y type zeolites was studied using differential scanning calorimetry. The exotherms for intrazeolite and surface complexation have been resolved. These thermal events exhibit a dependence on the copper loading and hydration level which has been interpreted as a pressure effect.     

载镍沸石上NH3-TPD脱附峰的非酸性探讨

NH_3-TPD技术表征固体催化剂的酸性似乎已很成熟,其实不然。如该技术表征HZSM-5沸石时,有作者观察到773K左右的高温脱氨峰,而有些作者则检测不到。诚然,各作者间所用试样及预处理条件等存在差异,但实验装置和实验操作条件不同带来的影响也不可忽视。此外,该技术在用于表征一些新的较复杂的催化剂时,其程脱谱也会呈现出新现象,这些现象有时是不能通过酸性来解释的,这是因为NH_3作为探针分子不仅具有碱性,同时还有还原性和配位性。本文对载镍沸石上NH_3-TPD谱图中出现的某些新峰进行了剖析和归属。     

非碱性介质中分子筛的合成

分子筛的合成通常是采用含碱金属离子的强碱性体系,通过水热晶化法实现~[1,2]的.得到的分子筛原粉不但必须通过铵离子交换和焙烧才能转变为氢型催化剂,而且在该体系中晶体的粒度也较小.Guth等人~[3]首次报道了在非碱性介质F-离子存在下直接合成铵型ZSM-5的工作.除用四丙基溴化铵合成ZSM-5及其杂原子分子筛外~[4],尚未见到在非碱性介质中合     

Dimethyl carbonate as a novel methylating reagent for fatty acids in analytical pyrolysis

Dimethyl carbonate (DMC) was investigated as a mild, harmless and odorless reagent for pyrolytic methylation of fatty acids. Soybean oil was selected as test material for its high content of (poly)unsaturated fatty acids. Pyrolyses were performed at 500, 700 and 900 degrees C by means of a heated platinum filament pyrolyser on-line and off-line to the GC-MS apparatus. Methyl esters of palmitic, linoleic, oleic and stearic acid were formed as prominent products from off-line pyrolysis of soybean oil in the presence of DMC and zeolite 13X. Fatty acid methyl esters (FAMEs) were not observed at important levels in the absence of zeolite, while on-line Py-GC-MS experiments resulted principally in the formation of free fatty acids and hydrocarbons. The FAME profiles obtained from the DMC/zeolite off-line pyrolysis were compared to those resulting from tetramethylammonium hydroxide (TMAH) thermochemolysis and BF3-methanol procedure. The observed differences between pyrolysis and methanolysis methods were principally attributed to the thermal degradation of unsaturated fatty acids. The effectiveness of the DMC/zeolite pyrolytic methylation was further demonstrated by the analysis of tripalmitine and soybean seeds.     

Monte Carlo simulation of adsorption of binary and quaternary alkane isomers mixtures in zeolites: Effect of pore size and structure

Grand canonical Monte Carlo and configurational bias Monte Carlo techniques were employed to simulate the adsorption of binary mixtures of butane isomers and quaternary mixtures in nine zeolites at 300 K. For binary mixtures the results show there is a critical pore size, which is 10-membered-ring about 5.6 Å. The channel sizes of BEA, ISV, MOR and CFI are larger than this critical pore size, they prefer i-butane than n-butane, whereas TON with smaller channel size than critical pore size prefers n-butane than i-butane, but its selectivity decreases with pressure increasing. MFI, MEL and TER prefer i-butane than n-butane at low pressure, but with pressure increasing, the selectivity is reversed. BOG prefers i-butane than n-butane but the selectivity decreased with pressure increasing. It demonstrates that the adsorption and selectivity are controlled by both pore size and pore structure. The n-butane–i-butane–n-pentane–2-methylbutane quaternary mixtures adsorbed in these nine zeolites were studied, and the results show alkane chain length dependence at low pressure, but the adsorption is controlled by pore size and structure with pressure increasing in all the zeolites except for TON and BOG.