Ti-Si介孔分子筛的转晶与控制

以季铵盐型阳离子Gemini表面活性剂[C16H33(CH3)2N+(CH2)6N+(CH3)2C16H33]•2Br−(GEM16-6-16)为模板剂, 改变n(Ti)/n(Si)比值, 合成了系列Ti-Si介孔分子筛. X射线衍射(XRD)和透射电子显微镜(TEM)等表征结果表明, 在n(Ti)/n(Si)≤0.20时, 分子筛为高度有序六方介孔; 当 n(Ti)/n(Si)为 0.30时, 介孔转晶为立方相; 当n(Ti)/n(Si)为0.50时, 介孔转晶为层状相; n(Ti)/n(Si)为1.0时, 材料失去有序孔道结构. FT-IR分析表明, 在分子筛骨架间形成了Ti—O—Si键, 而且Ti—O—Si键的数目随n(Ti)/n(Si)的增加而增加, 达到一定饱和值后基本保持不变. 乙醇和丁醇对纯硅基介孔分子筛孔结构转晶控制作用呈现六方相→立方相→层状相递变规律, 因而钛酸正丁酯水解生成的丁醇对Ti-Si介孔分子筛转晶具有一定的控制作用.     

高硅分子筛ZSM-23的合成及表征

采用静态水热晶化法以吡咯烷为模板剂,合成出结晶度良好的ZSM-23分子筛晶体.对合成条件的研究结果表明,合成的关键是避免ZSM-35分子筛的生成.当n(Si)/n(Al)=25～110,n(H20)/n(SiO2)=1.3～4.8,n(pyr.)/n(SiO2)=0.12～0.5时,均能稳定生成ZSM-23分子筛晶体.当n(Si)/n(Al)>110时,不能得到分子筛晶体;当n(Si)/n(Al)<25时,生成的是ZSM-35分子筛晶体.采用XRD,SEM,TG-DTA,FTIR等技术,对合成的ZSM-23分子筛晶体的形貌,以及影响分子筛合成的因素进行了详细的研究.     

嫁接Al改性MCM-41介孔分子筛催化合成双酚F

以十六烷基三甲基溴化铵和正硅酸乙酯为原料,合成纯硅MCM-41介孔分子筛。再利用九水硝酸铝为改性剂来嫁接改性纯硅MCM-41介孔分子筛,NH3-TPD结果表明,嫁接后的AlMCM-41产生了中强酸。用改性后不同n(Si)/n(Al)的AlMCM-41催化合成双酚F,在n(苯酚)/n(甲醛)=30、反应时间5 h、反应温度90℃、m(甲醛)/m(AlMCM-41)=7的反应条件下,在一定范围内,双酚F的产率随Al含量增加而增加,但在n(Si)/n(Al)50时,双酚F的产率反而下降,当n(Si)/n(Al)=50时,双酚F的产率最高,为42.28%。     

钛钨改性HMS的合成及催化氧化苯甲醇合成苯甲醛

通过改变硅钛摩尔比和硅钨摩尔比合成了Ti-HMS和Ti/W-HMS型分子筛,并进行了NH3-TPD测试分析. 结果表明,当n(Si)∶ n(Ti)=30∶ 1、n(Si)∶ n(W)=400∶ 1时,分子筛的酸量最大. 利用上述不同HMS为催化剂,ω(H2O2)=30%的H2O2水溶液为氧化剂,在无有机溶剂及相转移催化剂条件下,氧化苯甲醇制备苯甲醛. 结果表明,Ti/W-HMS可选择性氧化苯甲醇制备苯甲醛;催化剂的酸量和酸强度越大,越有利于提高催化活性和选择性. 利用Ti(30)/W(400)-HMS为催化剂,当n(醇)∶ n(H2O2)=1∶ 2、ω(催化剂)=4%、反应时间为5 h时,苯甲醇的转化率和苯甲醛的选择性分别为72.6%、96.9%. 催化剂重复使用4次后,苯甲醇的转化率和苯甲醛的选择性分别为63.2%、89.1%.     

低温晶化对B-ZSM-5和Ti-ZSM-5物化性能的影响

 以改进方法合成的B-ZSM-5分子筛为母体,采用气固相法合成了Ti-ZSM-5分子筛,并以XRD,FT-IR,UV-Vis,XRF,SEM,ICP-AES和MAS NMR等手段对B-ZSM-5和Ti-ZSM-5进行了表征,考察了Ti-ZSM-5对苯酚羟基化反应的催化性能. 结果表明,合成B-ZSM-5时的前期低温晶化有助于晶粒的减小; 以其为母体制备的Ti-ZSM-5对苯酚羟基化反应具有优异的催化性能. 在n(PhOH)/n(H2O2)=3,n(Me2CO)/n(PhOH)=2.7,m(cat)/m(PhOH)=5%,T=353 K和t=6 h的反应条件下,苯酚转化率可达20%以上.     

新型八元环孔结构分子筛Cu/SAPO-35应用于NH_3-SCR的研究

采用六亚甲基亚胺(HMI)为模板剂,合成了新型SAPO-35分子筛,研究发现SAPO-35的酸性随着硅铝摩尔比增加[n(SiO_2)/n(Al_2O_3)=0.3,0.5,0.7]呈现先增加后降低的趋势,当n(Si)/n(Al)=0.7时,部分Si将发生SM3取代,进而降低SAPO-35酸量.进一步采用旋转浸渍法和离子交换法对SAPO-35进行改性,制得Cu/SAPO-35催化剂,并研究了其催化氨气选择性还原(NH3-SCR)反应的性能.催化剂表征结果表明,Cu主要以Cu~(2+)离子形式存在于离子交换法制备的Cu/SAPO-35中,因此其NH3-SCR催化性能更优良.基于液相离子交换法,进一步研究了不同硅铝比[n(SiO_2)/n(Al_2O_3)=0.3,0.5,0.7]SAPO-35原粉酸性对所制备Cu/SAPO-35催化剂NH_3-SCR反应活性的影响,结果表明,分子筛原粉强酸量越大,制得的Cu基催化剂中Cu~(2+)离子含量越高,从而催化剂的SCR活性、N_2选择性更优.     

低硅铝比ZSM-5分子筛上C4烃的催化裂解反应

以低硅铝比(n(SiO2)/n(Al2O2)=20-45)的ZSM-5分子筛为催化剂,研究了混合C4烃的催化裂解反应,并对不同硅铝比的ZSM-5分子筛进行了酸性表征.混合C4烃的催化裂解反应结果表明,低硅铝比的ZSM-5分子筛具有较高的低温催化活性,高硅铝比ZSM-5分子筛催化剂上乙烯和丙烯的收率高于低硅铝比ZSM-5分子筛催化剂,低硅铝比ZSM-5分子筛上苯和甲苯的收率高于高硅铝比ZSM-5分子筛催化剂.在反应温度为625℃时,硅铝比为20的ZSM-5分子筛催化剂上乙烯、丙烯、苯和甲苯的总收率可达79.42%.酸性表征结果表明,硅铝比低的ZSM-5分子筛具有更多的Bronsted(B)酸酸量、Lewis(L)酸酸量及总酸酸量,这是低硅铝比ZSM-5分子筛具有低温高活性及高的苯和甲苯收率的原因.     

低硅铝比ZSM-5分子筛上C4烃的催化裂解反应

以低硅铝比(n(SiO2)/n(Al2O3)=20-45)的ZSM-5分子筛为催化剂, 研究了混合C4烃的催化裂解反应, 并对不同硅铝比的ZSM-5分子筛进行了酸性表征. 混合C4烃的催化裂解反应结果表明, 低硅铝比的ZSM-5分子筛具有较高的低温催化活性, 高硅铝比ZSM-5分子筛催化剂上乙烯和丙烯的收率高于低硅铝比ZSM-5分子筛催化剂, 低硅铝比ZSM-5分子筛上苯和甲苯的收率高于高硅铝比ZSM-5分子筛催化剂. 在反应温度为625 ℃时, 硅铝比为20的ZSM-5分子筛催化剂上乙烯、丙烯、苯和甲苯的总收率可达79.42%. 酸性表征结果表明, 硅铝比低的ZSM-5分子筛具有更多的Bronsted(B)酸酸量、Lewis(L)酸酸量及总酸酸量, 这是低硅铝比ZSM-5分子筛具有低温高活性及高的苯和甲苯收率的原因.     

尿素改性β-分子筛催化苯与煤制油烷基化制重烷基苯

对β-分子筛(n(Si)∶n(Al)=15∶1)分别进行酸洗、碱洗改性,制备出孔结构、酸性等性质不同的分子筛催化剂。通过扫描电子显微镜(SEM)、X射线衍射(XRD)、N2吸附-脱附、NH3-TPD和Py-FTIR等表征手段对分子筛催化剂的结构、性能及其在苯的烷基化反应中的应用进行了研究。结果表明,盐酸浸洗对β-分子筛的孔径、比表面积及孔容均有扩大作用,但在酸性上有所减弱; Na OH溶液浸洗造成了分子筛骨架的崩塌,对其酸性与孔结构均造成了破坏;尿素改性不仅改善了分子筛的孔结构性质,而且对分子筛酸性影响较小,是一种温和、有效的改性方式。尿素改性β-分子筛催化剂催化苯与煤基冷阱油的烷基化反应活性最好,烯烃转化率达91. 2%,且重烷基苯2位异构体(2-HAB)和3位异构体(3-HAB)在产物中含量最高,选择性分别为50. 1%和33. 5%,占整个烷基化产物的84%。     

SAPO-11分子筛合成条件对其结晶度与催化性能的影响

在水热条件下改变合成条件合成一系列SAPO-11分子筛,采用XRD对样品进行结晶度表征,并考察了合成条件对SAPO-11分子筛催化性能的影响.结果表明,合成条件对SAPO-11分子筛的结晶度和催化性能有很大影响.以二正丙胺(DPA)为模板剂,n(DPA)/n(Al2O3)=1.5,n(SiO2)/n(Al2O3)=0.2,晶化时间为24 h和晶化温度为170℃时,合成出的SAPO-11分子筛催化剂最有利于萘和甲醇的甲基化反应.初步探究其在萘和甲醇的甲基化反应中的失活原因.结果表明,催化剂失活的主要原因是在萘和甲醇的甲基化反应过程中生成大量的水,经高温水脱铝导致分子筛结构坍塌,从而导致分子筛失活.     

Synthesis of Highly ordered Large Size Mesoporous Silica and Effect of Stabilization as Enzyme Supports in Organic Solvent

ＩｎｔｒｏｄｕｃｔｉｏｎＴｈｅｔｅｃｈｎｉｑｕｅｆｏｒｅｎｖｉｒｏｎｍｅｎｔｐｒｏｔｅｃｔｉｏｎｈａｓｂｅ ｃｏｍｅｉｎｃｒｅａｓｉｎｇｌｙｉｍｐｏｒｔａｎｔ .Ｔｈｅｃｌｅａｒｂｉｏｄｅｃｏｍｐｏｓｉ ｔｉｖｅｍｅｔｈｏｄｓｈａｖｅｂｅｅｎｎｏｔｅｄｉｎｒｅｃｅｎｔｙｅａｒｓ ,ａｎｄｐｅｒｏｘｉｄａｓｅｓ(ｈｅｍｅｅｎｚｙｍｅ)ｈａｖｅｂｅｅｎｗｉｄｅｌｙｕｔｉｌｉｚｅｄｉｎｓｏｍｅａｐｐｌｉｃａｔｉｏｎｓｓｕｃｈａｓｄｅｐｏｌｙｍｅｒｉｚａｔｉｏｎｏｆｌｉｇｎｉｎｏｒｃｏａｌ[1,2 ] ,ａｎｄｔｈｅｎ…     

Mesoporous zirconosilicate doughnuts with high performance in liquid oxidative dehydrogenation of hydroquinone to quinone

Unusual partially crystalline ordered mesoporous zirconosilicate doughnuts with Si/Zr ratio as low as 1.5 were synthesized from the aqueous polymerisation of a single source molecular precursor Zr[OSi(Ot-BuO)(3)](4) without the use of any templating agent. A radial homogenous mesoporosity (4 nm) was observed inside these very regular sub-micrometric (600 nm) doughnuts. These structures were partially crystallized in hydrothermal conditions (100°C) into an analogous zircon (ZrSiO(4)) framework. The formation mechanism has been investigated. It is evidenced that chlorine anions Cl(-) concentration and pH value are essential to achieve the process, even if their role is still a matter of investigations. The obtained materials demonstrated even higher catalytic activity, selectivity and stability in the liquid oxidative dehydrogenation of hydroquinone to 1,4-benzoquinone compared to TS-1 zeolite catalysts and amorphous highly ordered mesoporous zirconosilicate materials.     

Zr-TUD-1: a Lewis acidic, three-dimensional, mesoporous, zirconium-containing catalyst

A three-dimensional, mesoporous, silicate containing zirconium, Zr-TUD-1, was synthesized by a direct hydrothermal treatment method with triethanolamine as a complexing and templating reagent to ensure that zirconium was incorporated as isolated atoms. The mesoporosity of Zr-TUD-1 was confirmed by X-ray diffraction (XRD), N(2) sorption and high-resolution transmission electron micrograph (HR-TEM) studies. The nature and strength of the Lewis acid sites present in Zr-TUD-1 were evaluated by FTIR studies of pyridine adsorption and temperature-programmed desorption of ammonia. FTIR, X-ray photoelectron spectroscopic (XPS) and UV/Vis spectroscopic studies showed that, at Si/Zr ratios of 25 and higher, all the zirconium was tetrahedrally incorporated into the mesoporous framework, while at low Si/Zr ratios, a small part of the zirconium was present as ZrO(2) nanoparticles. Zr-TUD-1 is a Lewis acidic, stable and recyclable catalyst for the Meerwein-Ponndorf-Verley (MPV) reaction and for the Prins reaction.     

A vanadyl complex grafted to periodic mesoporous organosilica: a green catalyst for selective hydroxylation of benzene to phenol

Selective benzene hydroxylation: A periodic mesoporous organosilica embedded with a vanadyl(IV) acetylacetonate complex has been synthesized through a co-condensation method. This system is a catalyst for direct hydroxylation of benzene to phenol, presenting a selectivity of 100?% towards the phenol formation as well as an excellent catalytic recyclability (see scheme).     

Investigation of Size-Selective Zr(2)@Si(n) (n = 16-24) Caged Clusters

The size-selective Zr(2)Si(n) (n = 16-24) caged clusters have been investigated by density functional approach in detail. Their geometries, relative stabilities, electronic properties and ionization potentials have been discussed. The dominant structures of bimetallic Zr(2) doped silicon caged clusters gradually transform to Zr(2) totally encapsulated structures with increase of the clustered size from 16 to 24, which is good agreement with the recent experimental result (J. Phys. Chem. A. 2007, 111, 42). Two novel isomers, i.e., naphthalene-like and dodecahedral Zr(2)Si(20) clusters, are found as low-lying conformers. Furthermore, the novel quasi-1D naphthalene-like Zr(n)Si(m) nanotubes are first reported. The second-order energy differences reveal that magic numbers of the different sized neutral Zr(2)Si(n) clusters appear at n = 18, 20 and 22, which are attributed to the fullerene-like, dodecahedral and polyhedral structures, respectively. The HOMO-LUMO gaps (>1 eV) of all the size-selective Zr(2)Si(n) clusters suggest that encapsulation of the bimetallic zirconium atoms is favorable for increasing the stabilities of silicon cages.     

钒改性六方介孔硅分子筛催化苯羟基化制苯酚

以偏钒酸铵为钒源,采用溶胶-凝胶法合成了不同钒含量的六方介孔硅（V-HMS）分子筛,利用X射线衍射、N2吸附-脱附和程序升温还原(H2-TPR)对合成的催化剂进行了表征,考察了V-HMS对苯羟基化反应的影响。 结果表明,钒进入了分子筛骨架,并且在HMS分子筛上具有较好的分散性。 V-HMS对苯羟基化反应具有良好的催化活性;高分散的钒氧物种有利于提高苯的羟基化反应性能,溶剂乙腈对反应促进作用明显。 乙腈为溶剂,w(V(5.8)-HMS)=2%,60 ℃反应5 h,苯酚收率达到18.55%,选择性达到100%。     

制备条件对ZrO2晶相结构的影响

不同晶体结构ＺｒＯ２的制备探索表明,二氧化锆的晶体结构极大地依赖于它的制备条件,从同一种原料可以制备出不同晶体结构的二氧化锆,也可以从不同的锆直产制备出同一种晶体结构的二氧化锆。     

Ti—MCM—41的结构特征与芳烃羟化反应的化学亲和选择性

以不同硅源合成了Si/Ti比不同的Si-Ti－MCM－41,并在引入Ti的同时引入Al,合成了Si/Al比不同的Si-Ti-Al-MCM-41。XRD、TEM、低温N2吸附的表征结果说明,Ti-MCM-41具有长程有序一维孔道,且比表面积较高,FT－IR光谱表征说明,Ti对骨架Si的取代使MCM－41表面出现缺陷羟基。Al的引入有利于Ti-MCM-41有序结构的形成。且可调变Ti-MCM-41的表面性质。Ti-MCM-41在不同极性芳烃化合物的羟化过程中表现出化学亲和选择性,且调变Ti-MCM-41的表面性质可实现对化学亲和选择性的控制。     

Influencing the selectivity of zeolite Y for triglycine adsorption

In prior work we studied the adsorption of triglycine on zeolite Y under reference conditions. This study aims to solve the question of which adsorbent properties and process conditions influence the adsorption triglycine from an aqueous solution by zeolite Y. Relevant zeolite parameters to study are: the amount of acidic sites (Si/Al(2) ratio), counter ion, micropore structure. Process conditions that may influence triglycine adsorption are pH, other components such as sugars, amino acids and salts, and temperature. Adsorption of triglycine on zeolite HY is dominated by ionic interaction. The capacity and selectivity of zeolite HY for triglycine can be changed by choosing different Si/Al(2) ratios or changing the counter ion. The presence of cations and basic anions in solutions reduces triglycine adsorption. Fructose and glycine have no significant influence on triglycine adsorption. Temperature only has a slight influence. The pore structure of zeolite Y is not a critical factor for triglycine adsorption, provided pores are accessible to triglycine and in the micropore range (<2 nm). While this allows other zeolites than zeolite Y to be applied, the presence of the supercage structure of zeolite Y is beneficial to obtain better adsorption of triglycine in its neutral form.