SBA-15的硅烷化对钴基催化剂费-托合成性能的影响(英文)

以未硅烷化和硅烷化的SBA-15为载体,采用满孔浸渍法制备了钴基费-托合成催化剂,通过元素分析、N_2吸附-脱附、X射线衍射、H_2程序升温还原、H_2程序升温脱附以及氧滴定等手段对催化剂进行了表征.催化剂的费-托合成活性测试在固定床反应器上进行.研究表明,对于SBA-15硅烷化后制备的催化剂,金属钴与载体之间的相互作用降低,氧化钴的还原度增加.随着三甲基氯硅烷用量的增加,三甲基硅基的表面覆盖度增加,钴的晶粒直径增大.硅烷化后的催化剂的高活性归因于高的还原度.而C_(5+)选择性的增加则归因于钴晶粒直径的增大.     

含钨SBA-15介孔分子筛催化剂的表面酸性和羟基分布

分别以浸渍法和水热晶化法制备了SBA-15介孔分子筛孔中插入氧化钨和碳化钨的催化剂,采用NH3-TPD测定了表面酸性和总酸量,并采用FT-IR研究了它们的表面羟基分布情况.NH3-TPD结果表明,浸渍法制备的含氧化钨的SBA-15介孔分子筛催化剂表面只有SBA-15介孔分子筛的弱酸位,而含碳化钨的SBA-15介孔分子筛催化剂表面还出现了W2C的强酸位.水热晶化法制备的含氧化钨的SBA-15介孔分子筛催化剂表面SBA-15介孔分子筛的弱酸位随W含量的增大略有增强, W含量较高时还出现了钨物种的强酸位;含碳化钨的SBA-15介孔分子筛催化剂表面除了SBA-15介孔分子筛的弱酸位外, W含量较低时有W2C的强酸位, W含量较高时有W2C和WC两种强酸位.傅里叶变换红外光谱结果表明,浸渍法和水热晶化法制备的含氧化钨和碳化钨的SBA-15介孔分子筛催化剂除表面自由硅羟基外,还存在着α, β和γ三种不同类型的氢键羟基,并且氢键羟基和催化剂的制备方法以及催化剂的W含量都有一定的关系.     

镁-双噁唑啉络合物催化3,5-二甲基-N-α,β-不饱和酰基吡唑的不对称共轭氰化反应研究

报道了镁-双噁唑啉络合物体系催化的TMSCN与3,5-二甲基-N-α,β-不饱和酰基吡唑的不对称共轭氰化反应.考察了BOX配体结构、配体与金属比例、温度、溶剂等对反应的影响.研究结果表明,使用双苄基取代的双噁唑啉配体与二丁基镁(物质的量比为2;1)在1,2-二氯乙烷中原位生成手性催化剂,催化剂用量为10 mol％,反应...     

α-和γ-环糊精改性法制备的Ni/SBA-15催化剂的物化性质及其在甲烷二氧化碳重整中的催化性能（英文）

以多羟基有机物α-或γ-环糊精为分散促进剂制备了Ni/SBA-15催化剂,通过N2吸附-脱附、X射线衍射、透射电镜、程序升温还原和热重等手段对该催化剂的物理化学性质进行了表征,并将其应用于甲烷二氧化碳重整(CRM)制合成气反应.结果显示,与采用传统浸渍法制备的Ni/SBA-15催化剂相比,采用α-或γ-环糊精改性法制备的催化剂具有更小的Ni O颗粒,并在CRM中显示出更高的催化活性及更强的抗积碳性能.机理研究表明,采用传统浸渍法制备Ni/SBA-15催化剂时,浸渍液中的Ni2+主要在浓度梯度的作用下逐渐进入到SBA-15孔道内部,Ni2+水合物容易团聚,分散程度较低;而采用α-或γ-环糊精改性方法制备催化剂时,在水溶液中Ni2+与环糊精形成包覆物,环糊精携带Ni2+进入SBA-15孔道内,并且环糊精的存在使得Ni2+之间相互隔离,以高度分散形态存在于SBA-15孔道表面,有利于后续热处理中Ni O在载体上较好地分散.     

L-脯氨酸衍生的手性N,P-配体的合成及其在不对称1,3-偶极环加成反应中的应用

从L-脯氨酸衍生而来的酰胺膦类化合物1,经脱去保护基得到的氨基膦2,用正丁基锂处理后,用2-甲氧基吡啶类化合物捕获,得到一类吡啶型的手性N,P-配体4;氨基醇与碳酸二乙酯生成的噁唑啉酮6,与四氟硼酸三乙氧基鎓盐反应制得的乙氧基噁唑啉7直接与氨基膦2反应,合成了噁唑啉型手性N,P-配体8.将两类手性N,P-配体应用于Ag(I)催化的1,3-偶极环加成反应,通过对反应条件进行优化,发现手性N,P-配体与AgOTf所形成的催化剂能很好地催化1,3-偶极环加成反应,最高可以以93%的收率获得环加成产物,ee值最高可以达到15%.     

温度和pH值双敏感的生物相容性三嵌段共聚物聚(2-乙基-2- 唑啉)-b-聚(ε-己内酯) -b-聚(L-谷氨酸)的合成和表征

研究了由温敏的聚(2-乙基-2-噁唑啉)和pH值敏感的聚(L-谷氨酸)组成的三嵌段共聚物,聚(2-乙基-2-噁唑啉)-b-聚(ε-己内酯)-b-聚(L-谷氨酸)的合成方法,(1)以对甲苯磺酸甲酯为引发剂引发2-乙基-2-噁唑啉进行正离子开环聚合反应,得到了羟基封端的聚(2-乙基-2-噁唑啉)(PEOz-OH);(2)以PEOz-OH为引发剂,以辛酸亚锡为催化剂,在氯苯中合成了PEOz-b-聚(ε-己内酯)两嵌段共聚物(PEOz-b-PCL-OH);(3)将PEOz-b-PCL-OH末端的羟基转换为氨基,得到氨基封端的两嵌段共聚物(PEOz-b-PCL-NH2);(4)以PEOz-b-PCL-NH2为引发剂引发γ-苄基-L-谷氨酸-N-羧酸酐(BLG-NCA)开环聚合,得到了PEOz-b-PCL-b-聚(γ-苄基-L-谷氨酸)(PEOz-b-PCL-b-PBLG)三嵌段共聚物;(5)以HBr的醋酸溶液为脱保护剂脱去苄基保护基,得到PEOz-b-PCL-b-聚(L-谷氨酸)(PEOz-b-PCL-b-PLGlu)三嵌段共聚物.采用1H-NMR、GPC和FT-IR表征了各步聚合物的结构、分子量和分子量分布.     

温度和pH值双敏感的生物相容性三嵌段共聚物聚(2-乙基-2-噁唑啉)-b-聚(ε-己内酯)-b-聚(L-谷氨酸)的合成和表征

研究了由温敏的聚(2-乙基-2-噁唑啉)和pH值敏感的聚(L-谷氨酸)组成的三嵌段共聚物,聚(2-乙基-2-噁唑啉)-b-聚(ε-己内酯)-b-聚(L-谷氨酸)的合成方法,(1)以对甲苯磺酸甲酯为引发剂引发2-乙基-2-噁唑啉进行正离子开环聚合反应,得到了羟基封端的聚(2-乙基-2-噁唑啉)(PEOz-OH);(2)以PEOz-OH为引发剂,以辛酸亚锡为催化剂,在氯苯中合成了PEOz-b-聚(ε-己内酯)两嵌段共聚物(PEOz-b-PCL-OH);(3)将PEOz-b-PCL-OH末端的羟基转换为氨基,得到氨基封端的两嵌段共聚物(PEOz-b-PCL-NH2);(4)以PEOz-b-PCL-NH2为引发剂引发γ-苄基-L-谷氨酸-N-羧酸酐(BLG-NCA)开环聚合,得到了PEOz-b-PCL-b-聚(γ-苄基-L-谷氨酸)(PEOz-b-PCL-b-PBLG)三嵌段共聚物;(5)以HBr的醋酸溶液为脱保护剂脱去苄基保护基,得到PEOz-b-PCL-b-聚(L-谷氨酸)(PEOz-b-PCL-b-PLGlu)三嵌段共聚物.采用1H-NMR、GPC和FT-IR表征了各步聚合物的结构、分子量和分子量分布.     

模型石脑油在硫化Co-Mo／SBA-15催化剂上的加氢异构化反应

通过浸渍法制备了Co/SBA-15、Mo/SBA-15和Co-Mo/SBA-15催化剂,对催化剂的孔结构、物相及表面酸性进行了表征,测定了硫化催化剂上噻吩加氢脱硫及1-己烯加氢异构的反应性能,并与工业Co-Mo/γ-Al2O3催化剂进行了对比.结果表明,Co-Mo/SBA-15催化剂表面具有较强的B酸中心,且对噻吩加氢脱硫具有较高的催化活性;而Co-Mo/γ-Al2O3催化剂表面主要为较强的L酸中心,对1-己烯加氢具有较高的催化活性.Mo/SBA-15催化剂的B酸酸性较强,但同时具有较高的1-己烯加氢活性,故它对1-己烯骨架异构的催化活性不高.Co-Mo/SBA-15催化剂的加氢活性相对较低,1-己烯容易在其较强的B酸中心上发生骨架异构反应,具有潜在的工业化应用前景.     

外表面钝化SBA-15固载奎宁催化不对称Michael加成反应

以聚环氧乙烷-聚环氧丙烷-聚环氧乙烷三嵌段共聚物(P123)为模板剂制备SBA-15分子筛,将未除模板剂的SBA-15用三甲基氯硅烷钝化后固载奎宁制得外表面钝化CH_3-SBA-15-QN非均相催化剂.对非均相催化剂进行XRD、FT-IR、N_2吸附-脱附表征.并以查尔酮类化合物与丙二腈的不对称Michael加成反应为模型来考察非均相催化剂CH_3-SBA-15-QN的催化活性,实验结果表明,非均相催化剂CH_3-SBA-15-QN比SBA-15-QN催化剂对产物表现出较高的对映选择性.4-甲氧基查耳酮为底物时,CH_3-SBA-15-QN为催化剂时,产物对映选择性能够达到77%,甚至比均相催化剂高6%,充分发挥了载体孔道效应和手性催化剂的不对称诱导能力.     

Mo助剂含量对Mo-Ni2P/SBA-15/堇青石整体式催化剂加氢脱硫性能的影响

 采用共浸渍法制备了 P/Ni 摩尔比为 2 的 Ni2P/SBA-15, 再通过二次浸渍引入助剂 Mo 制得 Mo-Ni2P/SBA-15, 将它调制成活性胶后均匀涂敷于预处理后的载体表面, 干燥焙烧后在氢气流中采用程序升温还原法, 制备了一系列 Mo-Ni2P/SBA-15/堇青石整体式催化剂. 采用 X 射线衍射、N2 吸附-脱附和 X 射线光电子能谱对催化剂结构进行了表征, 以二苯并噻吩为模型含硫化合物, 考察了催化剂的加氢脱硫性能. 结果表明, Mo 的加入增大了催化剂的比表面积, 在催化剂表面形成了 MoNiP2, 且 Ni2P 为主要活性物相. Mo 在催化剂表面主要以 Mo6+和 Moδ+形式存在; 当 w(Mo) = 4.2% 时, n(Mo)/n(Ni+Mo) = 0.18 的整体式催化剂上二苯并噻吩的转化率最高, 且在较低反应温度时以直接脱硫机理为主, 而较高反应温度时以加氢脱硫机理为主.     

Preparation, Characterization and Catalytic Performance of La-SO4/SBA-15 in Esterification of Acetic Acid with n-Butanol

La-SO42-/SBA-15 was synthesized with various amounts of lanthanum via incipient-wetness impregnation. Characterization was done by X-ray diffraction（XRD）, transmission electron micrographs（TEM）, nitrogen adsorption, FTIR spectroscopic analysis, thermogravimetric analysis, and the total amount of acidity of catalyst was estimated by TPD of NH3. The results indicate that lanthanum has been incorporated into SBA-15 molecular sieve. The prepared materials（La-SO42-/SBA-15） keep the highly ordered mesoporous two-dimensional hexagonal structure and do not change the mesoporous channel structure of the support SBA-15. The catalyst showed best catalytic activity in the synthesis of n-butyl acetate. The optimum conditions of the esterification by orthogonal experiments were studied： the molar ratio of n-butanol to acetic acid 1：1.2, the amount of catalyst 7.5%, reaction time 80 min. The yield of n-butyl acetate could reach 93.2% under the optimum conditions. The catalyst was recyclable, cost effective and environmental friendly.     

Silicotungstic acid-derived WO3 composited with ZrO2 supported on SBA-15 as a highly efficient mesoporous solid acid catalyst for the alkenylation of p-xylene with phenylacetylene

Highly dispersed silicotungstic acid-derived WO₃ composited with ZrO₂ supported on SBA-15（WZ/SBA-15） as an ordered mesoporous solid acid catalyst was prepared via a facile incipient wetness impregnation（IWI） method that active ingredients,ZrO₂ and WO₃,were impregnated into the channels of SBA-15 simultaneously with a subsequent calcination process.The relationship between catalyst nature and performance was explored by high resolution transmission elec...     

Deep oxidative desulfurization of fuels catalyzed by molybdovanadophosphoric acid on amino-functionalized SBA-15 using hydrogen peroxide as oxidant

This study reports the usage of molybdovanadophosphoric acid catalyst on amino-functionalized SBA-15(PMoV₂/SBA-15-NH₂) for the removal of sulfur from model oil (dibenzothiophene dissolved in n-hexane). To increase the tendency for adsorption of heteropoly acids, mesoporous SBA-15 silica was functionalized with amino groups by postsynthesis grafting, using 3-aminopropyltrimethoxy silane as the coupling agent. Immobilization of molybdovanadophosphoric acid on pure SBA-15 (PMoV₂/SBA-15) was also studied for comparison and the catalysts were characterized by physicochemical and spectroscopic methods. It was found that the catalysts exhibit high catalytic activities and PMoV₂/SBA-15-NH₂ is more durable than PMoV₂ impregnated on unmodified mesoporous SBA-15 silica. The results may bring about improvement for oxidative desulfurization of transportation fuels.     

SBA-15负载钒氧化物催化剂上甲烷选择氧化反应

对SBA-15负载的钒、钼、钨氧化物催化的甲烷选择氧化反应性能进行了比较,发现VO_x/SBA-15催化剂优于MoOx/SBA-15和WOx/SBA-15催化剂.针对钒氧化物催化剂,考察了不同钒源、不同载体以及少量P元素的添加对催化性能的影响,结果表明以SBA-15为载体的催化剂的性能好于MCM-41和Cab-O-Sil为载体的催化剂;与V₂O₅,VO(C₂O₄)相比,NH₄VO₃是制备性能良好的VO_x/SBA-15的钒源;在VO_x/SBA-15中,添加少量P元素后,HCHO的选择性有一定程度的提高.XRD,N₂物理吸附、UN-Raman和H₂-TPR表征结果表明,负载量低于3 wt%时,钒组分可能主要以高分散的单核的VO_x物种存在,我们推测该物种对甲烷选择氧化制甲醛起关键作用.     

Highly ordered mesoporous La(III)-substituted 5-oxopyrrolidine-2-carboxylic acid (Glp) immobilized on SBA-15 as a very efficient nanocatalyst for green aerobic oxidative coupling of thiols to disulfides

Selective aerobic oxidative coupling of thiols that are catalyzed by La(III)-substituted 5-oxopyrrolidine-2-carboxylic acid (Glp) immobilized on SBA-15 (SBA-15@Glp–La; SBA = Santa Barbara amorphous) was studied. Using SBA-15@Glp–La, the complete conversion was achieved at room temperature in the presence of air without producing any over-oxidized yields. SBA-15@Glp–La was prepared by post-grafting technique. 5-Oxopyrrolidine-2-carboxylic acid (Glp) condensation followed by La(III) impregnation caused this La(III)-grafted 5-oxopyrrolidine-2-carboxylic acid (Glp) to immobilize on SBA-15. This SBA-15@Glp–La catalyst shows excellent catalytic activity in the selective aerobic oxidative coupling of thiols. Effects of amount of the catalyst, polarity of the solvent, effects of substrate, and catalyst reusability were investigated. It has been observed that seven repetitive reaction cycles did not cause any appreciable loss in the catalytic activity of this catalyst. The catalyst characterization by scanning electron microscopy, energy-dispersive X-ray spectroscopy, X-ray diffraction, Fourier-transform infrared spectroscopy, thermal gravimetric analysis, transmission electron microscopy, inductively coupled plasma, elemental mapping, and N₂ adsorption–desorption is reported. The procedure developed is heterogeneous and environmentally benign.     

Zr(SO4)2·4H2O/SBA-15固体酸催化剂的制备及其催化性能

以介孔分子筛SBA-15为载体,采用浸渍法制备了系列四水硫酸锆(ZS)负载型催化剂ZS/SBA-15,用FT-IR、EDS、XRD、N₂吸附-脱附、Hammett指示剂等对催化剂的组成、结构和酸强度进行了表征。 结果表明,硫酸锆负载后,催化剂仍基本保持六方有序的孔阵列和尺寸不变的介孔孔道;在负载量＜40%时,硫酸锆均能在载体上高度分散。 该系列催化剂具有中等强度的酸中心,对乙二醇单乙醚与乙酸、正丁醇与柠檬酸的酯化反应有很高的催化活性,且对目标酯产物的选择性为100%。 在最佳的负载量和反应条件下,乙二醇单乙醚和柠檬酸的转化率约高达98%,催化剂重复使用多次仍可保持相当的活性。     

Preparation, Characterization and Catalytic Performance of La-SO42-/SBA-15 in Esterification of Acetic Acid with n-Butanol

La-SO42-/SBA-15 was synthesized with various amounts of lanthanum via incipient-wetness impregnation.Characterization was done by X-ray diffraction(XRD), transmission electron micrographs(TEM), nitrogen adsorption,FTIR spectroscopic analysis, thermogravimetric analysis, and the total amount of acidity of catalyst was estimated by TPD of NH3. The results indicate that lanthanum has been incorporated into SBA-15 molecular sieve. The prepared materials(La-SO42-/SBA-15) keep the highly ordered mesoporous two-dimensional hexagonal structure and do not change the mesoporous channel structure of the support SBA-15. The catalyst showed best catalytic activity in the synthesis of n-butyl acetate. The optimum conditions of the esterification by orthogonal experiments were studied: the molar ratio of n-butanol to acetic acid 1:1.2, the amount of catalyst 7.5%, reaction time 80 min. The yield of n-butyl acetate could reach 93.2% under the optimum conditions. The catalyst was recyclable, cost effective and environmental friendly.     

Nb-P/SBA-15催化剂的制备及其对果糖水解制5-羟甲基糠醛的催化性能

果糖催化脱水制5-羟甲基糠醛（5-HMF）是生物质转化制高附加值化合物过程中的一个重要反应。采用自制的介孔SBA-15,浸渍法制备了Nb/SBA-15催化剂,再经磷酸化处理制得Nb-P/SBA-15催化剂,研究了该催化剂在果糖脱水制5-HMF反应中的性能。SEM、TEM、BET和XRD表征结果表明,Nb/SBA-15和Nb-P/SBA-15完好地保留了SBA-15的微观结构,其内孔道直径为10 nm,铌酸在孔内表面分布均匀;负载铌和磷酸化后,孔壁变薄。NH₃-TPD结果显示,Nb/SBA-15经磷酸预处理后,不仅弱酸性位有所增加,而且产生了中强酸和强酸性位,使得在含水两相体系果糖脱水反应中,Nb-P/SBA-15比Nb/SBA-15具有更高的催化活性和5-HMF选择性。同时考察了反应温度、溶剂比例、反应时间对果糖脱水的影响,结果表明,以水/MIBK（V/V=1/2）为溶剂时,160 ℃下反应1.5 h,果糖转化率和5-HMF收率分别高达96.1%和92.6%。Nb-P/SBA-15经循环使用四次后仍具有较好的催化活性,表明该催化剂具有较高的耐水稳定性。     

Co-Fe/SBA-15与过一硫酸盐联用非均相催化降解水中染料罗丹明B

由于硫酸根自由基(SO4?-)的强氧化性,基于SO4?-的高级氧化技术受到人们的高度关注.采用过渡金属活化过一硫酸盐(PMS)产生SO4?-用以分解有机物,反应体系简单,反应条件温和,且不需要额外的能量供给,因此,成为人们优先选用的方法,其中,采用高效、环境友好的非均相过渡金属催化剂活化PMS处理难降解有机物成为研究热点.本文研究了非均相CoFe/SBA-15-PMS体系对水中难降解染料罗丹明B(RhB)的降解.以SBA-15为载体, Co(NO3)2·6H2O和Fe(NO3)3·9H2O为前驱物,采用一步等体积浸渍法制备了CoFe/SBA-15,通过X射线衍射(XRD)、N2吸附-脱附、扫描电镜(SEM)、能谱(EDS)、透射电镜(TEM)和振动样品磁强计(VSM)等对其进行了表征.考察了焙烧温度、Co与Fe的负载量对CoFe/SBA-15催化性能的影响和该催化剂的重复使用性能,还考察了RhB降解动力学及催化剂CoFe/SBA-15投加量、氧化剂PMS投加量和反应物(RhB和PMS)初始浓度对其性能的影响,探讨了RhB的降解机理.结果表明：对于催化剂CoFe/SBA-15,合成焙烧后在SBA-15上负载的Fe、Co化合物主要是CoFe2O4复合物,它作为催化剂的活性中心负载在SBA-15的孔道内外.制备的焙烧温度对CoFe/SBA-15催化性能几乎无影响,但对Co浸出影响显著.与SBA-15相比,催化剂10Co9.5Fe/SBA-15-700(Co和Fe负载量分别为10 wt%和9.5 wt%,焙烧温度700 oC)的比表面积、孔体积和孔径均减小,分别为506.1 m2/g,0.669 cm3/g和7.4 nm,但仍然保持SBA-15的有序六方介孔结构.该催化剂以棒状体的聚集态存在,聚集体直径大于0.25μm,其磁化强度为8.3 emu/g,因此,可通过外磁铁容易地从水中分离.相比之下,10Co9.5Fe/SBA-15-700具有最佳的催化性能和稳定性,可使RhB的降解率达到96%以上, Co的浸出量小于32.4μg/L.在CoFe/SBA-15和PMS共存下, RhB的降解符合一级动力学方程, RhB降解速率随CoFe/SBA-15和PMS投加量的增加和初始反应物浓度的减小而提高.淬灭实验结果表明,在CoFe/SBA-15, PMS和RhB水溶液体系中,存在的主要活性自由基为SO4?-,它是由CoFe/SBA-15活化PMS产生的,对RhB的降解起决定性的作用. RhB降解过程的UV-vis结果表明, RhB的降解途径主要是蒽环打开, SO4?-优先攻击RhB的有色芳香烃环,然后RhB进一步分解为小分子有机物. CoFe/SBA-15循环使用10次仍能保持高催化活性和稳定性,在每次反应中RhB的降解率均大于84%, Co和Fe的浸出量均分别小于72.1和35μg/L. CoFe/SBA-15作为高效、环境友好的非均相催化剂可有效地活化PMS产生SO4?-降解水中RhB,具有实际应用的潜力.     

Influence of the pore structure of MCM-41 and SBA-15 silica fibers on atomic layer chemical vapor deposition of cobalt carbonyl

Mesoporous high surface area MCM-41 and SBA-15 type silica materials with fibrous morphology were synthesized and used as support materials for the ALCVD (atomic layer chemical vapor deposition) preparation of Co/MCM-41 and Co/SBA-15 catalysts. Co/MCM-41 and Co/SBA-15 catalysts were prepared by deposition of Co2(CO)8 from the gas phase onto the surfaces of preheated support materials in a fluidized bed reactor. For both silica materials, two different kinds of preparation methods, direct deposition and a pulse deposition method, were used. Pure silica supports as well as supported cobalt catalysts were characterized by various spectroscopic (IR) and analytical (X-ray diffraction, Brunauer-Emmett-Teller, elemental analysis) methods. MCM-41 and SBA-15 fibers showed considerable ability to adsorb Co2(CO)8 from the gas phase. For MCM-41 and SBA-15 silicas, cobalt loadings of 13.7 and 12.1 wt % were obtained using the direct deposition method. The cobalt loadings increased to 23.0 and 20.7 wt % for MCM-41 and SBA-15 silicas, respectively, when the pulse deposition method was used. The reduction behavior of silica-supported cobalt catalysts was found to depend on the catalyst preparation method and on the mesoporous structure of the support material. Almost identical reduction properties of SBA-15-supported catalysts prepared by different deposition methods are explained by the structural properties of the mesoporous support and, in particular, by the chemical structure of the inner surfaces and walls of the mesopores. Pulse O2/H2 chemisorption experiments showed catalytically promising redox properties and surface stability of the prepared MCM-41- and SBA-15-supported cobalt catalysts.