镁铝复合氧化物载体的制备与性质研究

以硝酸镁和硝酸铝为原料,用氨水溶液作为pH调节剂,采用共沉淀法制备了镁铝复合氧化物载体,研究了制备过程中镁铝比、pH调节剂种类、水解过程pH值的大小、反应温度、焙烧温度及回流晶化温度对复合氧化物载体理化性质的影响。并以RFCC汽油加氢脱硫为探针反应,考察了以镁铝复合氧化物为载体的催化剂选择性加氢脱硫性能。实验结果表明,在镁铝分子比为10、反应温度为80℃、pH值为9.5条件下制备的镁铝复合氧化物载体具有适宜的比表面积和均匀的孔分布,且晶型较完整,结晶度高。以该复合氧化物为载体制备的催化剂具有良好的RFCC汽油选择性加氢脱硫反应性能。     

铈镁铝混合氧化物催化剂的脱NOx性能

 用共沉淀法制得Mg-Al水滑石和二氧化铈的混合物,经750 ℃热活化,得到铈镁铝混合氧化物催化剂. 考察了催化剂的组成、反应温度、反应体系中氧含量、水蒸气及二氧化硫的存在对NO和CO反应活性的影响. 结果表明,铈镁铝混合氧化物催化剂具有较高的脱NOx活性,并具有优异的水热稳定性和一定的抗氧性及抗二氧化硫毒化的能力.     

以镁铝水滑石为前驱体制备复合氧化物催化丙酮气相缩合反应

采用共沉淀-恒温晶化法制备了系列镁铝水滑石(Mg-Al-LDH)样品,对镁铝水滑石在500 ℃焙烧得到镁铝复合氧化物(Mg-Al-LDO),采用IR、XRD、CO₂-TPD、SEM及N₂吸附-脱附等方法对Mg-Al-LDH和Mg-Al-LDO进行了表征。在温度250 ℃、液时空速1 h^-1条件下,采用固定床对镁铝复合氧化物催化剂对丙酮缩合反应的性能进行微反活性评价。研究结果表明,晶化时间与镁铝复合氧化物的弱碱性位和强碱性位的密度相关。丙酮缩聚反应的主要产物为异佛尔酮(IP)和异丙叉丙酮(MO),以及少量的异丙烯基丙酮、双丙酮醇,均三甲苯等。丙酮缩聚制备异佛尔酮的反应需要催化剂表面弱碱性位(S_w)与强碱性位(S_s)的协同作用,S_w与S_s需要匹配。晶化12 h得到的镁铝复合氧化物催化剂(LDO-12)的S_w/S_s=1.3,异佛尔酮(IP)选择性为65.3%,单程有效收率(IP+MO)为14.8%。     

具有Ru-M (M=Fe, Co, Ni, Mo)双金属活性中心的负载型氨合成催化剂

 研究了钾促进的双金属中心Ru-M (M=Fe, Co, Ni, Mo)氨合成催化剂.结果表明, Ru-Co催化剂活性最高, Ru和Co含量均为2%的Ru-Co催化剂具有最好的应用价值,其催化活性与Ru和Co含量均为4%的催化剂相近. 此外,还对以镁铝尖晶石、氧化镁和镁铝复合氧化物等不同氧化物为载体的Ru-Co双金属中心催化剂进行了对比研究. 结果表明,以高温煅烧制得的氧化镁作载体的催化剂活性最高.     

Pd-基金属-酸-碱多功能催化剂的制备及其丙酮一步法合成MIBK性能研究

甲基异丁基酮 (MIBK) 是一种重要的化学品, 广泛应用于涂料以及有机合成领域, 下游产品包括特种涂料溶剂、高品质脱蜡溶剂和高性能橡胶防老剂等. 近年来随国民经济的快速发展, 甲基异丁基酮的年需求量与价格逐年上升, 应用领域也不断拓宽. 因此, 开展 MIBK 绿色合成工艺的研究对提高原子经济性、打破国际技术壁垒以及满足国内市场需求具有重要意义. 目前生产 MIBK 最绿色、高效的生产方法是丙酮一步法, 包括缩合、脱水以及加氢等一系列反应过程, 该工艺顺利实施的关键在于所使用的催化剂. 根据丙酮一步法合成 MIBK 反应特点, 所用催化剂表面必须具备多种催化活性中 心, 从而保证缩合、脱水以及加氢反应的顺利进行, 实现从反应物到产物的高效转化. 因此, 高活性和高选择性多功能催化剂的制备是提高 MIBK 生产效率的有效途径.本文采用浸渍法将具有加氢活性的贵金属 Pd 负载在表面具有丰富酸性位点或碱性位点的固体酸或固体碱氧化物载体上, 制备了 Pd/MOx(M = Ti, Ce, Al, Si, La, Ca和Mg) 双功能催化剂, 并用于丙酮一步法合成 MIBK 反应中. 结果表明, Pd基金属-酸/碱双功能催化剂均可以催化该连串反应的进行, 其性能高于 Pd 基金属-酸双功能催化剂, 其中 Pd/MgO 催化剂上丙酮转化率为30.67%, MIBK 产率可达27.61%. 构效关系研究显示, 催化剂表面酸性位点和碱性位点对于该连串反应的各反应步骤催化性能有所不同, 其中碱性位点有利于丙酮缩合反应, 而酸性位点有利于二丙酮醇脱水反应, 且强路易斯碱性中心位点可以更好的催化缩合反应的进行, 同时中强度路易斯酸性中心位点具有最佳的催化脱水反应的能力. 此外, 表面具有最强路易斯碱性中心位点 Pd/La2O3催化剂并未表现出最高的MIBK产率, 说明在丙酮一步法合成MIBK反应中, Pd基双功能催化剂表面各位点间的协同对其催化性能具有重要的影响.本文进一步采用水热法和沉淀沉积法制备了系列MgTiOx、MgAlOx和CaTiOx二元复合氧化物 (MMO) 以及 CaMgAlOx和 TiMgAlOx三元MMO, 并以其为载体, 通过浸渍焙烧还原制备 Pd 基多功能催化剂, 并用于丙酮一步法合成MIBK反应中,发现Pd/MgAl-MMO多功能催化剂具有最高的催化活性及 MIBK 产率. 对其表面多功能位点数量进行调变, 并通过 XRD、CO2-TPD、NH3-TPD、吡啶红外、CO2红外和HRTEM等进行表征, 结果表明, 经过450 ℃焙烧酸碱中心摩尔量比为0.4的0.1%Pd/Mg3Al-MMO多功能协同催化剂三种催化活性中心位点协同作用最佳, 其丙酮转化率为38.20%, MIBK产率可达31.63%. Pd/Mg3AlMMO多功能协同催化剂三种活性位点接近性研究表明, 在多功能催化剂中分离酸中心活性位点、碱中心活性位点以及加氢活性位点后, 获得的双功能催化剂产率均明显下降, 说明Pd/Mg3Al-MMO多功能催化剂在三种活性位点相互接近时才能更好催化反应的进行. 根据多功能催化剂构效关系研究结果, 对各催化活性中心的密度及分布进行调控, 结果显示, 通过沉淀沉积法制备的Pd/Mg3Al-MMO催化剂性能进一步提高, 丙酮转化率为42.11%, 产率高达37.20%.     

镁助剂改性Pd/Al_2O_3甲烷催化燃烧催化剂:Mg/Al物质的量比对催化剂载体及活性物种形成的影响

本文研究了系列不同含量镁助剂改性的Pd/Al_2O_3催化剂的甲烷催化燃烧反应。研究表明,随着镁添加量的增加,载体由Al_2O_3转变为尖晶石型MgAl_2O_4,进一步增加Mg/Al物质的量比至3∶1时,形成了Mg(Al)O_x固溶体;催化剂中活性相Pd物种以金属Pd,PdO_x或Pd-载体复合氧化物形式存在,各物种的相对含量以及Pd?PdO间的转化能力存在一定的差异。PdO_x物种表现为具有较高的低温活性,而金属Pd和Pd-载体复合氧化物的高温活性较好。当Mg/Al物质的量比为1∶3时,催化剂的Pd?PdO转化能力最强,表现出了最高的甲烷催化燃烧反应活性。     

负载PtSn金属助剂的镁铝水滑石上的丙烷脱氢反应研究

我们研究了以镁铝水滑石作为载体,利用水滑石层间阴离子的可交换性,负载活性金属铂和锡的丙烷脱氢反应.在镁铝水滑石载体中加入Ga能够影响丙烷脱氢活性,当镓的含量为1%时催化剂丙烷脱氢反应活性最高,反应初始时,丙烷转化率为46.5%,反应2 h后,丙烷转化率仍有37.5%.当以Mg(Ga)(Al)O-1%为载体时,考察了不同H_2/C_3H_8摩尔比对丙烷脱氢活性的影响,结果表明当H_2/C_3H_8摩尔比为0.5∶1时,丙烷脱氢反应具有最佳的反应活性,即当在原料气中加入H_2时,能够使得丙烷脱氢的转化率大幅度提升,且选择性也有所提升.烷烃脱氢是一个吸热反应,同时考察了温度对烷烃脱氢反应性能影响,结果表明温度越高,丙烷脱氢反应具有更高的转化率.对催化剂进行长时间寿命实验考察,发现当反应经过40 h后,丙烷的转化率仍有23.5%,说明Pt Sn-Mg(Ga)(Al)O-1%催化剂具有较好的稳定性.     

镁铝复合金属氧化物负载纳米Pd催化剂的制备及其在醇胺一步合成亚胺反应中的应用

以共沉淀法制备的Pd2+掺杂水滑石为前驱体,通过焙烧、还原得到了镁铝复合金属氧化物负载纳米Pd催化剂.利用X射线粉末衍射(XRD),X射线光电子能谱(XPS),场发射透射电子显微镜(TEM)等手段对催化剂进行表征,发现通过Pd2+掺杂水滑石为前驱体制备的复合金属氧化物负载纳米Pd催化剂,可以实现Pd纳米颗粒(3.6 nm)在镁铝复合氧化物表面的均匀分散.该催化剂在催化苯甲醇和苯胺一步法合成N-苄叉苯胺时,在温和的反应条件下表现出良好的催化性能以及对N-苄叉苯胺较高的选择性,产物收率99%.在循环实验过程中,催化剂表现出较好的稳定性,并且催化活性未见下降.     

不锈钢丝网上Cu基催化剂的制备及反应性能

采用阳极氧化技术在不锈钢丝网上成功地自生长了结构致密的氧化物膜,并以此为载体,通过电化学沉积工艺制备了Cu/不锈钢丝网催化剂。以甲苯、丙酮、乙酸乙酯及二氯甲烷为模型反应,考察了4种不同种类挥发性有机化合物(VOCs)在该催化剂上的完全氧化活性。结果表明电化学沉积时间为15 min制备得到的催化剂上完全氧化丙酮、甲苯、乙酸乙酯及二氯甲烷的温度分别为240、220、260和440℃。在220℃反应条件下进行60 h的甲苯氧化稳定性试验结果显示该催化剂催化氧化甲苯的转化率一直保持98%以上,表现出较好的稳定性。扫描电镜,X射线衍射及X射线光电子能谱等表征结果表明,不锈钢丝网载体表面的阳极氧化物膜有利于提高活性组分的分散度。设计采用电沉积工艺大大提高了催化剂表面活性物种与载体的结合牢固度。     

空心结构磁性固体碱催化剂Fe3O4@LDO的制备与性能

基于水滑石类化合物的复合氧化物(LDO)是一类性能优异的固体碱催化剂,对其进行改性和功能化引起了越来越多的关注。本文将空心结构和Fe_3O_4引入到镁铝复合氧化物中,制备了一种空心结构磁性固体碱催化剂Fe_3O_4@LDO。这种空心结构磁性固体碱催化剂粒子具有以镁铝复合氧化物为壳层,空心Fe_3O_4为核的核壳结构。由于其独特的空心结构,Fe_3O_4@LDO粒子的悬浊液具有良好的稳定性,将其应用于催化Knoevenagel缩合反应,达到平衡后苯甲醛的转化率约为62%,显示出较好的催化性能。同时,Fe_3O_4@LDO粒子具有较强的磁性,非常方便分离与回收,是一种性能优良的磁性固体碱催化剂。     

固载脯氨酸类手性催化剂的制备及在不对称Aldol反应中的催化作用

制备了两种二氧化硅-甲基纤维素-脯氨酸类手性小分子复合催化剂,证明了它们可以在室温下催化不对称Aldol反应.所得产物产率较高,ee值最高能达到86.8%.这些催化剂比较稳定,并具有一定的重复使用的性能.     

Adsorption and oxidation of propan-2-ol on WO3/MgO

Magnesia-supported tungsta catalysts have been prepared by impregnation, with different tungsta contents and calcined at different temperatures in air. All samples are active for propan-2-ol dehydrogenation above 473 K, and selective towards acetone formation. At low W content, acetone is further oxidized. The behavior has been related to the W-containing phases existing in the samples.     

丙酮一步法合成甲基异丁基酮催化剂研究

用浸渍法制备了丙酮一步法合成甲基异丁基酮负载型催化剂，考察了载体的预处理温度、添加镧助剂对催化剂性能的影响；用BET法测定了催化剂的表面积；采用H2-O2滴定法测定Pd的分散度．结果发现，用经过1．023K焙烧过的Al2O3为载体的催化剂具有较好的催化性能，添加镧助剂后催化剂的分散度、活性有较大的提高．     

Insights into Promoting Effect of Sm on Catalytic Performance of the CeO2/Beta Catalyst in Direct Conversion of Bioethanol to Propylene

Aseries of Sm-doped CeO₂/Beta composite catalysts with various Sm/Ce atomic ratios(0.1-0.4) was prepared by an incipient impregnation method, followed by calcination at 650 ^oC. They were characterized by X-ray diffraction(XRD), N₂ adsorption, X-ray photoelectron spectroscopy(XPS), Raman, NH₃-temperature programmed desorption(TPD) and CO₂-TPD. The incorporation of Sm into CeO₂/Beta increases obviously the propylene yield for the selective conversion of ethanol to propylene. The promoting effect of Sm on CeO₂/Beta can be attributed to two reasons. One is more acetone intermediates are generated on the Sm-doped catalysts due to the enhanced formation of oxygen vacancies. The other is the conversion of acetone intermediate to propylene is enhanced owing to weaker and fewer acid sites on the Sm-doped catalysts.     

Preparation of rhodium catalysts on laminar and zeolitic structures by anchoring of organometallic rhodium

Rhodium catalysts supported on six different aluminosilicate structures were prepared by hydrogen reduction of a cationic organometallic rhodium complex anchored to the support. The precursor active phase was incorporated in acetone medium through ion exchange using [Rh(Me₂CO)_x(NBD)]ClO₄ as the metal precursor species, in which NBD is 2,5‐norbornadiene and (Me₂CO)_x is acetone. The effect of the structure and characteristics of the support on metal load and dispersion was studied in the heterogeneous catalysts thus prepared. The supports were characterized by X‐ray diffraction, energy‐dispersive X‐ray analysis, volumetric adsorption and surface acidity. For the precursors and catalysts, the metal load was determined by UV–VIS spectra, the reduction temperature was determined by differential scanning calorimetry, and rhodium dispersion was measured by chemisorption. The structure of the materials used as supports had a great influence on the catalyst prepared. A higher metal content was achieved in the supports with laminar structures, whereas better dispersion was shown by the catalysts supported on zeolitic structures. Copyright © 2001 John Wiley & Sons, Ltd.     

浸渍溶剂对Fe／AlPO_4－5催化剂性能的影响

浸渍溶剂对Ｆｅ／ＡｌＰＯ_４－５催化剂性能的影响马静红，范彬彬，李瑞丰，曹景慧（太原工业大学精细化工研究所，太原０３００２４）关键词Ｆｅ／ＡｌＰＯ_４－５催化剂，制备方法，浸渍溶剂，ＣＯ加氢反应ＡＩＰＯ４－５是一种新型的分子筛，其独特的晶体结构和表面选...     

Acetone oxidation using ozone on manganese oxide catalysts

Supported manganese oxide catalysts were prepared by the impregnation of alumina foam blocks washcoated with alumina and silica. The manganese content based on the weight of the washcoats was 10 wt % calculated as MnO2. Fourier transform profiles of the Mn K-edge EXAFS spectra for these samples gave three distinctive peaks at 0.15, 0.25, and 0.32 nm and were close to the profiles of Mn3O4 and beta-MnO2. The number of surface active sites was determined through oxygen chemisorption measurements at a reduction temperature (Tred = 443 K) obtained from temperature-programmed reduction (TPR) experiments. Acetone catalytic oxidation was studied from room temperature to 573 K, and was found to be highly accelerated by the use of ozone on both catalysts with substantial reductions in the reaction temperature. The only carbon-containing product detected was CO2. The alumina-supported catalyst was found to be more active than the silica-supported catalyst in acetone and ozone conversion, with higher turnover frequencies (TOFs) for both reactions. The pressure drop through the foam was low and increased little (0.003 kPa/10 000 h(-1)) with space velocity. In situ steady-state Raman spectroscopy measurements during the acetone catalytic oxidation reaction showed the presence of an adsorbed acetone species with a C-H bond at 2930 cm(-1) and a peroxide species derived from ozone with an O-O bond at 890 cm(-1).     

单层分散型Pt/Ni双金属催化剂的制备及其C=C和C=O催化加氢性能

 利用金属置换反应制备了表面单层分散型Pt/Ni双金属催化剂,并测定了该催化剂对环己烯、苯乙烯、丙酮和丁醛气相加氢反应的催化性能. 结果发现,这种催化剂具有比传统浸渍法制备的相同Pt含量的Pt/Ni和Pt/Al2O3催化剂更高的催化活性.     

Effect of Tin Precursor on the Catalytic Properties of Pt-Sn/Al2O3 Sol-Gel Prepared Catalysts

Tin-alumina supports were prepared by cogelation of aluminum tri-sec-butoxide and tetrabutyltin or tin tetrachloride. Aqueous or acetone platinum solutions were used for impregnation. The results show that the specific surface area and the acidity of the catalysts were only slightly modified by the metal precursors used. On cyclohexane dehydrogenation andn-hexane conversion, high selectivity to olefins and low cracking products were detected.     

Aldol condensation of furfural and acetone on layered double hydroxides

The Aldol condensation of furfural (Fur) with acetone (Ac) to 4-(2-Furyl)-3-buten-2-one (FAc) is one of the most important processes in the aqueous-reforming of oxygen-containing biomass derivatives and has been carried out in the presence of solid-base catalysts, calcined-rehydrated Layered Double Hydroxides (LDH). The Mg-Al Layered Double Hydroxides has been prepared by the coprecipitation, calcination and regeneration from mixed oxides by rehydration. The catalyst prepared with different Mg/Al molar ratios showed different catalytic performance and the best catalyst was with the Mg/Al molar ratio of 2.5. Phenol adsorption showed that the best catalyst had the largest numbers of accessible basic sites. The appropriate rehydration temperature and time for mixed oxides obtained by calcination were also investigated. The Mg-Al LDH catalysts can be regenerated by calcination at 773 K and rehydration in decarbonate water, but the regeneration is complex and incomplete. In addition, the catalyst calcined at high temperature also had activity, which was attributed to the formation of the Mg-Al spinels.