合成甲基叔丁基醚的分子筛催化剂研究

通过对ＨＺＳＭ－５,ＨＺＲＰ－１和Ｈβ三种类型分子筛催化剂上合成甲基叔丁基醚的活性测定和结构表征,初步考察了分子筛孔结构对催化活性的影响。在此基础上,对适宜孔结构的分子筛进行了水热改性,考察了改性条件对分子筛催化剂的性质及其合成甲基叔丁基醚反应催化活性的影响,得到了催化活性较好的分子筛催化剂。     

β分子筛的物化性质对其催化活性的影响

研究了β分子筛的物化性质对其催化活性的影响。实验发现,β分子筛对甲基叔丁基醚(MTBE)反应的催化活性是各类酸中心共同作用的结果,但强Lewis酸密度对其活性的影响较大;比表面积、二次孔体积及微孔比表面积等因素与异丁烯转化率无明显的相关性;C4原料中的惰性组分对MTBE反应的影响较小,但以混合C4为原料时MTBE反应的初始反应速率较低。     

Efficient Synthesis of Dimethyl Ether from Methanol in a Bifunctional Zeolite Membrane Reactor

A sandwich FAU–LTA zeolite dual‐layer membrane has been developed and used as a catalytic membrane reactor for the synthesis of dimethyl ether (DME). In the top H‐FAU layer with mild acidity, methanol is dehydrated to DME. The other reaction product, water, is removed in situ through a hydrophilic Na‐LTA layer, which is located between the porous alumina support and the H‐FAU top layer. The combination of mild acidity with the continuous removal of water results in high methanol conversion (90.9 % at 310 °C) and essentially 100 % DME selectivity. Furthermore, owing to the selective and continuous removal of water through the Na‐LTA membrane, catalyst deactivation can be effectively suppressed.     

HY Zeolite Modified by Liquid Silane Deposition and Its Catalytic Activity in Selective tert-Butylation of Naphthalene

HY zeolites were modified by chemical liquid deposition with i-C₄H₉Si(OC₂H₅)₃, followed by hydrothermal treatment. The samples were characterized by X-ray diffraction, N₂ adsorption and pulse mass analysis to investigate the influence on framework structure, specific surface area, pore diameter and adsorption behaviors. The catalytic performances of HY zeolite and the modified samples in the alkylation of naphthalene with tert-butyl alcohol were also evaluated. The results showed the modification of HY zeolite did not change framework structure but increased specific surface area, decreased average pore diameter, and reduced the size of pore opening. Catalytic activity of the modified HY zeolite catalyst for tert-butylation of naphthalene was decreased compared with that of HY zeolite catalyst while shape-selectivity of 2,6-di-tert-butylnaphthalene (2,6-DTBN) was increased obviously, the highest 2,6-DTBN/2,7-DTBN ratio of 6.62 obtained.     

Effect of Spectrum of Acidity of Zeolites of Various Structural Types on Their Catalytic Characteristics in the Synthesis of Ethyl tert-Butyl Ether

The catalytic properties of zeolites of various structural types in the liquid phase synthesis of ethyl tert-butyl ether from isobutylene and ethanol have been studied. The activity and selectivity of the catalysts depend on the concentration and strength of the acid centers. A possible mechanism for the synthesis of ethyl tert-butyl ether is proposed, suggesting that isobutylene and ethanol are activated on the weak and strong acid centers respectively.     

Synthesis of Oxynitrided Beta Zeolite and Its Application in Knoevenagel Reactions as Solid Base Catalysts

It is a challenge to explore the possibility of developing various novel oxynitrided zeolites,in which oxygen bridging atoms are substituted to some levels by isoelectronic groups     

Kinetics of the Vapor-Phase Decomposition of Mtbe (Methyl Tert-Butyl Ether) over h3pw12o40/sio2

A kinetic study on the vapor-phase MTBE decomposition over H₃PW₁₂O₄₀/SiO₂ was carried out. Possible kinetic mechanisms are proposed and discussed. Rate expressions were ultimately developed after several verification processes.     

改性H-MOR沸石催化甲醇转化(英文)

The conversion of methanol was carried out over various mordenite zeolite catalysts to evaluate their catalytic performance. A post-preparation treatment of the H-MOR catalyst by halogenation with NH4Cl or NH4F and by hydrohalogenation with HCl or HF was carried out and its effect on methanol conversion reactions at 100–300 °C in a continuous flow reactor was investigated. The as-synthesized Hmordenite (H-MOR) is generally more active during dimethyl ether (DME) production than the NH4-MOR and Na-MOR. Fluor...     

甲醇及合成气制二甲醚中不同粒径的 HY 分子筛及复合 Cu-Mn-Zn/HY 催化剂

 通过改变导向剂的老化时间, 制备了一系列不同粒径的 HY 分子筛作为脱水催化剂, 考察了甲醇脱水反应性能; 将其与铜基甲醇合成活性组分 Cu-Zn-Mn 组成双功能催化剂, 考察了催化剂对合成气直接制二甲醚反应的催化性能. 结果表明, 粒径为 820 nm 的 HY 分子筛在甲醇脱水中表现出较高的催化活性; 以其作为脱水组分的双功能 Cu-Zn-Mn/HY 催化剂也表现出较高的催化活性和良好的稳定性.     

轻质烃类中微量甲醇、甲基叔丁基醚等含氧化合物的测定

在乙烯厂生产中微量含氧化合物的测定非常重要,含氧化合物的存在可引起催化剂中毒,致使生产不能长周期运行。对乙烯、丁烯-1中含氧化合物的测定已有报道。但随着仪器和数据处理设备的更新有些缺陷就显现出来。近年来,毛细管色谱柱在含氧化合物的测定上也得到应用,但所使用的极性柱对甲醇、甲基叔丁基醚（MTBE）等含氧化合物分析时常有C3,C4和C5等烃类的干扰,在分析实际样品时会有合峰出现,无法得到准确结果。本文采用超强极性的LOWOX色谱柱,可以排除轻质烃类的干扰,降低检出限。     

Isomerization of n-Hexane Over Platinum Ion-Exchanged Zeolite Beta

Zeolite Beta was synthesized from appropriate gels and crystallized under the controlled temperature and pressurized conditions. For isomerization of n-hexane, platinum ion-exchanged zeolite Beta exhibited high activity and selectivity for 2,2-dimethylbutane (2,2-DMB), 2,3-dimethylbutane (2,3-DMB), 2-methylpentane (2-MP) and 3-methylpentane (3-MP). As high as 72% of n-hexane conversion and 98% of product selectivity were obtained at 250°C, 1600 h^–1 for 20 min on stream. The influences of reaction temperature and space velocity were also studied. Pt/H-Beta zeolite was recommended as one of the promising catalyst for n-hexane isomerization due to its high activity and stability. The combined effect of the stronger acidity possessed by H-Beta and the dehydrogenation role played by Pt was believed to be responsible for the good catalytic performance of Pt/H-Beta.     

磷酸盐辅助一步合成介孔Beta分子筛

在合成纳米Beta分子筛的体系中添加磷酸二氢钠等无机盐,通过一步晶化制备介孔Beta分子筛.纳米分子筛组装形成的二次粒子克服了传统纳米粒子难以过滤分离的问题,同时所形成的粒间介孔改善了分子在催化剂内的扩散从而提高催化反应效率.采用X射线衍射、扫描电镜、氮吸附-脱附和氨程序升温脱附等表征方法对材料进行表征,结果表明磷酸二氢钠的用量对介孔体积有很大影响.当NaH2PO4/SiO2摩尔比为0.1时,合成的材料具有较好的孔结构和酸性,并在叔丁醇与苯酚的液相烷基化反应中表现出最好的催化活性.     

Electrotreatment of Wastewaters from High-Octane Fuel Production To Remove Methyl tert-Butyl Ether and Methanol

The possibility is examined of removing methyl tert-butyl ether from wastewaters by electrotreatment.     

多级孔无铝Beta分子筛的合成与表征

研究了氟介质条件下,合成参数对前驱体黏度和无铝Beta分子筛晶化过程的影响.X射线衍射结果表明,高水硅比可降低前驱体的黏度,但抑制分子筛的晶化.当合成体系中加入成核促进剂(二氧化锗)和晶化促进剂(高氯酸根或磷酸根)后,即使水硅摩尔比高达20~30,在150℃水热合成4 d,仍可获得高结晶性、微米级球形或多面体形无铝Beta分子筛.热重和能谱分析结果表明,极少量高氯酸根和磷酸根可进入分子筛孔道,并影响模板剂四乙基铵根离子的热分解过程.氮气吸附-脱附、扫描电子显微镜、透射电子显微镜和选区电子衍射分析结果表明,所得无铝Beta分子筛具有多级孔结构,介孔尺寸在3.4~3.8 nm之间,由纳米晶体或纳米棒堆积而成.     

Alkylation of acetylene by tert-butyl alcohol

A reaction of acetylene with tert-butyl alcohol in the presence of sulfuric acid leads to tert-butylacetylene.     

Catalytic Performances of Binder-free ZSM-5 Catalysts for Dehydration of Crude Methanol to Dimethyl Ether

A series of binder‐free ZSM‐5 catalysts and a binder‐containing catalyst were prepared and characterized with X‐ray diffraction (XRD), X‐ray fluorescence (XRF), ²⁷Al magic‐angle spinning (MAS) nuclear magnetic resonance (NMR), N₂ sorption and ammonia temperature‐programmed deposition (TPD) methods. The catalytic activity and selectivity in the dehydration of crude methanol to dimethyl ether (DME) were evaluated in a fixed‐bed reactor for the catalysts. The outstanding structural characters such as high zeolite contents, sufficiently open channels and richness in mesopores have been proved on these binder‐free catalysts. The influence of the solid‐acidity, which is closely related to the framework silica alumina ratio (SAR) of the catalysts, on the catalytic properties has been discussed. A binder‐free catalyst with a better potential in application has been selected for its high activity and selectivity, long life‐time and non‐sensitivity to water contents in the feed. The reason for its excellent performance of the catalyst was discussed.     

甲醇脱水制二甲醚的杂多酸/纳米HZSM-5复合固体酸催化剂

开发低温、高活性和良好稳定性的催化剂成为甲醇气相脱水制二甲醚乃至合成气一步法制二甲醚反应的核心.在氧化铝挤条成型的纳米HZSM-5沸石上负载Keggin结构12-磷钨酸制备了复合固体酸催化剂, 通过FT-IR、UV-Raman、³¹P MAS-NMR和XRD对所制备的样品进行表征. 以甲醇气相脱水制二甲醚为探针反应的研究结果表明, 在选定的操作条件下连续运转超过300 h, 甲醇摩尔转化率大于87%(理论转化率90.9%), 二甲醚摩尔选择性高于99.0%, 是目前该反应非常有效的催化剂之一.     

Method for determination of methyl tert-butyl ether in gasoline by gas chromatography

A simple method for the determination of methyl tert-butyl ether (MTBE) in gasoline has been developed. The separation of MTBE from other analytes was controlled by the use of gas chromatography–mass spectrometry in the full scan mode using the characteristic primary, secondary and tertiary ions m/z 73, 57 and 43. The sample mass spectrum did not show any superimposition of other analytes. The separation from the common gasoline component 2-methylpentane was sufficient for reliable quantitation. An application of the developed conditions using gas chromatography with flame ionization detection was performed by the analysis of regular, euro super, super premium unleaded and ‘Optimax’ gasoline from petrol stations in the area of Frankfurt/Main, Germany. Regular unleaded gasoline shows an average MTBE content of 0.4% (w/w), whereas the MTBE content in euro super gasoline varies between 0.4 and 4.2% (w/w). The blending of MTBE to super premium has increased from 8.2% (w/w) in 1998 to 9.8% (w/w) on average in 1999. The recently introduced gasoline ‘Optimax’ shows an average MTBE content of 11.9% (w/w). The presented method might also be used for the analysis of other ethers, such as ethyl tert-butyl ether, which requires the use of another internal standard.     

磷改性HZSM-5分子筛的制备及其在合成气一步法制二甲醚反应中的应用

 以磷酸为前驱体,采用浸渍法制备了一系列不同P2O5含量(分别为5%, 10%和15%)的磷改性HZSM-5分子筛(P2O5/HZSM-5), 并采用氨程序升温脱附和吡啶吸附红外光谱法研究了其酸性. 结果表明,随着P2O5含量的增大, P2O5/HZSM-5样品的酸量尤其是强Brnsted酸位的酸量逐渐减少. 以上述P2O5/HZSM-5分子筛为甲醇脱水催化剂与工业甲醇合成催化剂(Cu-ZnO-Al2O3)组成双功能催化剂,在连续流动加压固定床反应器上考察了其对合成气一步法制二甲醚反应的催化性能. 结果表明,以适量磷(10%P2O5)改性的HZSM-5分子筛作为甲醇脱水催化剂,可使产物中二氧化碳和烃类副产物的选择性分别由改性前的43.3%和3.0%下降至低于33%和0.1%, 从而使二甲醚的选择性由49.7%提高到63%以上. 当P2O5/HZSM-5中的磷含量(15%P2O5)过高时,产物中甲醇的选择性高达30%以上,表明反应所生成的中间产物甲醇无法有效地转化,从而使二甲醚的选择性和一氧化碳的转化率均大大降低.     

Selective alkylation of xylenes by alcohols on zeolite catalysts

The peculiarities of catalytic performance of crystalline aluminosilicates of different types and compositions (X, Y including dealuminated Y, mordenite, pentasil ZSM-5), as well as of amorphous aluminosilicate catalyst in conversion of xylene + alcohol mixtures were studied. New data were obtained for alkylation ofo-xylene withtert-butyl alcohol, concerning controlling the selectivity and stability of the zeolite catalysts in reactions proceeding with the participation of water, including the water evolved during the reaction, in particular by controlling the acidic properties and hydrophobycity of the zeolites. A catalyst ensuring production of 1,2-dimethyl-4-tert-butylbenzene (DMTBB) with a 94% yield and selectivity of alcohol conversion to the target product of 94–97% was developed. The catalyst can be used as the basis for a high-performance and environmentally safe method for the synthesis of DMTBB. The catalysts developed can be also used for selective alkylation ofo-xylene by C₃-C₅ alcohols and for alkylation ofm-xylene bytert-butyl alcohol.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No, 12, pp, 2912–2917, December, 1996.