过渡金属取代磷钼酸催化剂的制备及氧化脱硫性能研究

以有机氨功能化的SBA-15为载体,制备过渡金属取代的磷钼酸(PMo₁₁M,M=Fe, Co, Cu)负载型催化剂。利用XRD、FT-IR、BET、TEM、TG等手段对催化剂结构进行表征,结果表明,过渡金属成功负载到载体SBA-15上;催化剂的整体结构没有发生明显改变,催化剂活性组分均匀地分散在介孔SBA-15的表面和孔道中。结合XPS数据和氧化脱硫实验结果,发现催化剂表面的氧空位,可以活化活性氧物种,有助于催化剂脱硫性能的提升。以二苯并噻吩（DBT）为底物,进行氧化脱硫反应,考察引入的过渡金属对催化剂结构的改变和催化活性的影响。得到Co取代催化剂(PMo₁₁Co-NH₂-SBA-15)的脱硫效果最好,DBT的转化率达到91.15%。PMo₁₁Co-NH₂-SBA-15催化剂具有良好的循环稳定性。     

负载型Fe_2O_3对乙苯脱氢反应的催化性能

以正硅酸乙酯(TEOS)为硅源,分别以十六烷基三甲基溴化铵(CTAB)和P123为模板剂通过溶胶凝胶法、水热合成法合成出MCM-41、Al-MCM-41、SBA-15介孔分子筛,然后将其作为催化剂载体负载Fe2O3,应用到乙苯催化脱氢制苯乙烯的反应中,考察了不同负载量对乙苯脱氢反应性能的影响,探讨了催化剂的活性保持时间。结果表明,将介孔分子筛作为催化剂载体负载Fe2O3应用到乙苯脱氢反应,当负载量为60%时乙苯的转化率和苯乙烯的选择性均最高。当n Si/n Al为60时,Fe2O3/Al-MCM-41催化性能最好。Fe2O3/SBA-15所持续的活性时间最长。     

Cu-La2O3-Al2O3/SBA-15催化剂上乙醇催化转化制正丁醇

为了进一步提高Cu基催化剂的活性、选择性及稳定性,提出一种以有序介孔氧化硅分子筛(SBA-15)为载体制备负载型Cu基催化剂的方法.采用共浸渍法制备Cu-La2O3-Al2O3/SBA-15催化剂,并将该催化剂应用于固定床乙醇制正丁醇反应.在温度为533 K,压力为3 MPa,液体时空速率(LHSV)=2 mL?h?1...     

Co-Mo／SBA-15柴油加氢脱硫研究

以介孔分子筛SBA-15为载体,担载Co—Mo双金属活性组分制备了深度加氢脱硫催化剂。通过XRD和BET表征表明,负载金属后SBA-15分子筛仍然保持二维晶相结构,表面积略有下降。以直馏柴油为原料,在固定床反应器上评价了催化剂的脱硫反应活性的结果表明,SBA-15介孔分子筛Co—Mo的负载量为W（CoO）=5％,w（MoO3）=25％;脱硫适宜的反应条件为：反应温度360℃,压力4．0MPa,氢油体积比400．0,空速2．0h^-1。在此条件下,柴油硫含量可由1350μg／g降至39μg／g。     

ZSM-5/SBA-15催化氧化脱硫催化剂的制备表征及脱硫性能研究

结合分子筛ZSM-5与SBA-15自身的优点,合成了不同质量比例的ZSM-5/SBA-15微孔-介孔复合分子筛,并进行XRD、N2吸附-脱附表征,分析其结构特征。以其为载体负载金属W、Ni、Ce、Cu,制备出不同的氧化脱硫催化剂,对模拟油进行氧化脱硫研究。结果表明,负载金属W制备出的WO3-ZSM-5/SBA-15(ZSM-5质量分数为10%)复合分子筛,脱硫效果最好,脱硫率为75.44%。     

ZSM-5/SBA-15催化氧化脱硫催化剂的制备表征及脱硫性能研究

结合分子筛ZSM-5与SBA-15自身的优点,合成了不同质量比例的ZSM-5/SBA-15微孔-介孔复合分子筛,并进行XRD、N2吸附-脱附表征,分析其结构特征。以其为载体负载金属W、Ni、Ce、Cu,制备出不同的氧化脱硫催化剂,对模拟油进行氧化脱硫研究。结果表明,负载金属W制备出的WO3-ZSM-5/SBA-15(ZSM-5质量分数为10%)复合分子筛,脱硫效果最好,脱硫率为75.44%。     

K_2O/SBA-15的制备及其催化性能研究

以介孔分子筛SBA-15为载体,负载KNO3后焙烧制得K2O/SBA-15固体碱催化剂,以合成丙烯酸正丁酯的酯交换反应为探针反应,在间歇式反应釜中对K2O/SBA-15催化剂进行催化活性评价。结果表明,当K2O负载量为2%,K2O/SBA-15催化剂对此酯交换反应的催化活性最高。     

介孔分子筛SiW_(12)/SBA-15催化合成柠檬酸三丁酯

:将硅钨酸负载在纯硅介孔分子筛SBA-15的表面上,XRD结果表明负载型催化剂SiW12/SBA-15具有纯硅SBA-15的介孔结构.将该催化剂用于合成柠檬酸三丁酯的酯化反应.采用正交实验考察了反应温度、催化剂用量、酸醇摩尔比对柠檬酸转化率的影响,得出最佳反应条件为:反应温度120℃、催化剂用量为总物料质量的1.5%、酸醇摩尔比1:4.在此条件下反应4 h,柠檬酸转化率可达到91.5%,产物的纯度为99.3%.     

连续催化湿式过氧化处理腈纶废水研究

以金属Mn和Ce的硝酸盐为活性组分的前驱物,以介孔分子筛SBA-15为载体,浸渍焙烧法制备了负载型催化剂MnOx/SBA-15、CeOx/SBA-15及MnOx-CeOx/SBA-15,并以H2O2为氧化剂,在温和条件下连续催化湿式过氧化(CWPO)处理腈纶废水。结果表明,MnOx-CeOx/SBA-15催化剂表现出较好的催化活性和稳定性。试验选择了连续流固定床反应装置,考察了反应温度、进料流量、催化剂投加量、H2O2投加量等因素对COD去除率的影响。由试验得出,在150℃,进料流量25 mL/min,催化剂投加30 g/L,H2O2投加5%时,腈纶废水的COD去除率达到80%左右。     

Cu2+改性SBA-16固定化漆酶的研究

以介孔分子筛SBA-16为载体,用浸渍法将Cu2+负载于SBA-16上制备了Cu/SBA-16,然后用吸附法固定化漆酶,以2,2-联氮-二(3-乙基-苯并噻唑-6-磺酸)二铵盐为底物考察了漆酶的最适pH值、固定化体系中的载酶量以及Cu2+对固定化漆酶活性的影响。结果表明,在p H值为3时,漆酶具有较高的活性;固定化漆酶的活性随着酶和载体质量比的升高先快速升高然后趋于稳定,当酶和载体质量比为96 mg/g时,固定化漆酶的活性达到较高值;负载Cu2+后,Cu/SBA-16固定化漆酶的活性与Cu2+负载量呈现一定的正相关性。     

SBA-15 mesoporous silica modified with metal oxides by MDD method in the role of DeNOx catalysts

SBA-15 mesoporous silica was modified with metal (Al, Ti, Cu, Fe) oxides by the molecular designed dispersion (MDD) method using acetylacetonate complexes of metals as precursors of the catalytically active components. The modified mesoporous silicas were characterized with respect to texture (BET), composition (EPMA), coordination and aggregation of transition metal species (UV–vis-DRS), reducibility of the deposited transition metals (TPRed) and surface acidity (FT-IR). Deposition of aluminium and titanium species on the SBA-15 surface significantly increased its acidity, mainly by generation of strong Lewis acid sites. Copper and iron deposited on the surface of pure SBA-15 were present nearly exclusively in the form of mononuclear cations. Deposition of Fe or Cu on the SBA-15 supports modified with alumina or titania resulted in a formation of significant amounts of oligomeric metal oxide clusters. The SBA-15 based samples have been found to be active and selective catalysts of the DeNO_x process. The modification of the silica surface with titanium or aluminium prior to the deposition of iron or copper significantly improved the activity of the SBA-15 based catalysts.     

Vanadium, niobium and tantalum modified mesoporous molecular sieves as catalysts for propene epoxidation

SBA-3 mesoporous molecular sieves doped with transition metal ions (Fe, V, Nb and Ta) have been applied for selective oxidation of propene towards propylene oxide in the presence of N₂O as an oxidant. The kind and amount of applied modifiers significantly affected the catalytic activity. V/SBA-3 was found to be the most active among the catalyst under study. In spite of relatively high selectivity towards propylene oxide (reaching up to 23%), the main oxidation product was still propionaldehyde. Surprisingly, CO_x was not formed over V, Nb and Ta modified SBA-3 catalysts. Additional modification of V containing samples (V/SBA-3) with iron complexes resulted in the further increase in the catalysts activity for epoxidation reaction. A PO selectivity of about 20% could be achieved at a propylene conversion of 17% over mixed Fe/V/SBA-3 catalytic system.     

Catalytic combustion of benzene over metal oxides supported on SBA-15

The catalytic combustion of benzene over metal oxides supported on SBA-15 was investigated. The catalysts were prepared by the incipient wetness method and characterized by XRD, BET, TEM, ESR and TPR. The calcined siliceous SBA-15 and CuO/SBA-15 samples displayed well-resolved patterns with a sharp peak at about 1.0°. It is clear that the loading of CuO on the silica matrix drastically decreases the surface area and pore volume of the catalysts, as would be expected for the incorporation of CuO. Among the supported metal oxides, CuO supported on SBA-15 was found to have the highest activity for benzene oxidation. In addition, copper oxide supported on SBA-15 gives higher catalytic activity than copper oxide supported on MCM-41. From the ESR results, the CuO dispersed on the SBA-15 acts as the active site of the CuO/SBA-15 catalysts in the oxidative decomposition of benzene. The catalytic activity gradually increases with increasing CuO loading on SBA-15.     

MgO-SBA-15 Supported Pd-Pb Catalysts for Oxidative Esterification of Methacrolein with Methanol to Methyl Methacrylate☆

Novel MgO–SBA-15 supported catalysts were prepared for oxidative esterification of methacrolein (MAL) with methanol to methyl methacrylate (MMA). The MgO–SBA-15 supports were synthesized with different...     

SBA-15 mesoporous silica modified with rhodium by MDD method and its catalytic role for N<Subscript>2</Subscript>O decomposition reaction

SBA-15 mesoporous silicas modified with rhodium were studied as catalysts for the N₂O decomposition reaction. Rhodium was deposited on SBA-15 by the Molecular Designed Dispersion (MDD) method using Rh(acac)₃ as a precursor of active phase. The same method was used for the deposition of Cu, Fe, Al and Ti. The SBA-15 support modified with metals were characterized with respect to metal loading (EPMA), structure (XRD), texture (BET), morphology (SEM), Rh dispersion (oxygen chemisorption), surface acidity (pyridine adsorption) and chemical nature of introduced copper and iron species (UV–vis-DRS). The rhodium-containing SBA-15 samples were found to be active catalysts for the N₂O decomposition reaction. Deposition of Al on the Rh-loaded catalyst increased its activity. An opposite effect was observed for the samples modified with Cu and Fe.     

Enhanced ketalization activity of cyclohexanone and ethanediol over immobilized ionic liquid in mesoporous materials

Three different mesoporous molecular sieves, including MCM-41, MCM-48, and SBA-15, were synthesized by hydrothermal process and characterized by XRD, BET and TEM. The chlorine-aluminate acidic ionic liquid of 1-butyl-3-methylimidazolium chloride-aluminum chloride ([Bmim]Cl-AlCl₃, denoted as Al-ILs) was prepared by two-step method. The immobilized ionic liquid (SBA-15/Al-ILs, MCM-41/Al-ILs, MCM-48/Al-ILs) was prepared through impregnating Al-ILs. The structures of composite catalysts were characterized by XRD, BET, FT-IR, TEM and XPS. The amounts of aluminum present in the resulting composite catalysts were detected by ICP-AES to calculate the amount of AL-ILs impregnated. The ketalization between cyclohexanone and ethanediol was used as the model reaction to test the catalytic activities of the composite catalysts. The effects of molar ratio of the reactants, reaction time, the catalyst dose, as well as the addition of cyclohexane were discussed in detail. Also, catalytic activities of three catalysts with different pore sizes were compared. Under comparable conditions, the SBA-15/Al-ILs composite catalyst exhibited much high catalytic activity and gave a maximum yield that was ca. 85.1%.     

Nitrous Oxide Reduction with Ammonia and Methane Over Mesoporous Silica Materials Modified with Transition Metal Oxides

Transition metal oxides (Cu, Cr and Fe) were deposited on various mesoporous silicas (MCM-48, SBA-15, MCF and x-MSU) by an impregnation method. Electron microprobe analysis, BET, UV-VIS-DRS and temperature programmed desorption of NH₃ were used for the characterization of the samples. The modified mesoporous silicas were tested as catalysts of the N₂O decomposition and the N₂O reduction using ammonia and methane. The Cu-containing samples presented the highest catalytic activity in the N₂O decomposition, while the Cr- and Fe-modified materials were more active in the reduction of nitrous oxide with NH₃ and CH₄. The type of the silica support strongly influenced the catalytic performance of the studied materials.     

MOx/Y催化剂常温催化臭氧氧化甲苯的性能

以Y分子筛为载体,采用等体积浸渍法制备了MO_x/Y催化剂,并用于常温催化臭氧氧化甲苯反应。采用XRD、BET、H_2-TPR、甲苯吸附对催化剂进行表征,以甲苯转化率维持95%以上的时间(t_(95))为指标对催化性能进行评价。结果表明:10%MnO_2/Y催化剂〔m(MnO_2)/m(Y)=0.1〕具有较大的比表面积(538.6m~2/g)和孔容积(0.440 cm~3/g),较好的催化臭氧氧化甲苯活性(t95=210 min);CuO的加入提高了催化活性,5%MnO_2-5%CuO/Y〔m(MnO_2)/m(Y)=0.05且m(CuO)/m(Y)=0.05〕催化剂上t95=240min,CO_x选择性为80.6%,CO_2与CO摩尔比为4.970。由表征结果可知,较大的比表面积和孔容积有利于甲苯吸附,CuO与Mn O_2之间的相互作用促进了氧化还原性能的提高,进而有利于催化活性的提高。GC-MS结果表明:反应副产物堵塞催化剂孔道,占据催化剂表面活性位,导致催化剂失活。5%MnO_2-5%CuO/Y催化剂失活-再生4次后t_(95)可达220 min。     

One-pot hydrothermal preparation of SBA-15 supported Keggin-type 12-tungstophosphoric heteropolyacid mesoporous material and its bifunctional catalytic performance

In this work, a series of 12-tungstophosphoric acid (HPW) catalysts supported on mesoporous molecular sieves SBA-15 were prepared by a one-pot hydrothermal method and their physical and chemical properties were characterized by various techniques such as fourier transform infrared spectroscopy, powder X-ray diffraction, nitrogen adsorption–desorption and transmission electron microscopy. It has been found that all the catalysts retained the mesopore structure of SBA-15 and the primary Keggin-type structure of heteropoly acid. The surface areas and pore volumes of HPW-SBA-15 decreased with the increase of HPW heteropoly acid loadings. HPW units were mostly encapsulated inside the mesopores of SBA-15. The prepared catalysts showed excellent multifunctional catalytic properties. Their bifunctional catalytic performances were examined by photo-catalytic degradation of rhodamine-B dye and microwave-catalytic synthesis of isoamyl acetate. The sample with 20 wt% loading of 12-tungstophosphoric acid was found to be more active than the other catalysts under the photo and microwave-catalytic reaction conditions. Accordingly, reasons for the catalytic activity difference were simply explicated by the effect of HPW concentration on the physicochemical characteristic of HPW-SBA-15 catalysts such as surface areas, porosity, and mesostructure.