CuZnAl类水滑石衍生复合氧化物催化环己醇脱氢反应的研究

采用共沉淀法合成了不同CuZnAl配比的类水滑石,通过不同温度焙烧制备其衍生复合氧化物.采用X-射线衍射(XRD)、差热热重(TG-DTA)、N2吸附-脱附和CO2程序升温脱附法(CO2-TPD)对类水滑石和衍生复合氧化物进行了表征.将所得复合氧化物用于环己醇脱氢制备环己酮的反应中考察其催化活性.实验结果表明:CuZnAl类水滑石衍生复合氧化物对该反应具有很高的催化活性,在反应温度220℃时以CuZnAl[n(Cu)/n(Zn)/n(Al)=1.34/0.66/1.0]类水滑石为前躯体,400℃焙烧所得的衍生复合氧化物表现出最佳的催化活性,环己醇转化率高达94.9%,环己酮的选择性近100%.     

Zn-Al水滑石催化碳酸二甲酯与苯酚酯交换反应的研究

用共沉淀法制备了Zn-Al水滑石,并用于多相催化酯交换合成碳酸二苯酯的反应.研究了不同n(Zn)/n(Al)比的水滑石及其焙烧产物等对酯交换反应的催化活性.结果表明,Zn-Al水滑石催化剂对该反应的催化活性和选择性很高,当n(Zn)/n(Al)=3时,在150～180℃,n(PhOH)/n(DMC)=2,催化剂用量为反应物总质量的1.5%,在反应时间为12h的条件下,DMC的转化率达到55.9%,DPC和MPC的收率分别为25.3%和27.0%,酯交换产物的选择性达到93.6%.利用XRD,TG-DTA和TEM等手段对催化剂进行了表征.     

K改性NiAl类水滑石衍生复合氧化物催化分解N2O

制备了Ni/Al=4.1(原子比)的NiAl类水滑石,焙烧获得NiAl复合氧化物,浸渍K2CO3溶液制备了K改性NiAl复合氧化物催化剂,其中K/Ni=0.05~0.2(原子比),用于N2O催化分解反应.通过元素分析、XRD、BET、H2-TPR、XPS等技术表征了催化剂的组成结构,考察了NiAl类水滑石的预处理方式、...     

阳离子掺杂水滑石的制备及其在合成异佛尔酮制备中的应用

并流共沉淀法制备水滑石及Li 、Ba2 、Ca2 掺杂的水滑石,将水滑石焙烧得复合氧化物.XRD结果表明掺杂的水滑石形成了类似水滑石的层状结构.FT-IR结果表明3种掺杂后的氧化物具有相似的结构及表面吸附性能.将所得的复合氧化物用于丙酮合成异佛尔酮的反应中,实验结果表明:与未掺杂的水滑石型复合氧化物相比,3种掺杂的水滑石复合氧化物在合成异佛尔酮的反应中均表现出良好的活性.     

K改性Ni-Co-Al三元复合氧化物催化分解N2O

制备了(Ni+Co)/Al=3、Ni/Co=0.2(原子比)的NiCoAl三元类水滑石样品,焙烧获得NiCoAl复合氧化物,表面浸渍K₂CO₃溶液制备了K改性催化剂,用于N₂O分解反应,考察了K负载量、焙烧温度等制备参数和O₂、H₂O等反应气氛对催化剂活性的影响。用BET、XRD、H₂-TPR、XPS等技术表征了催化剂的组成结构。结果表明,K的表面改性提高了催化剂对N₂O分解反应的催化活性,其中,400℃预焙烧NiCoAl类水滑石制得复合氧化物,初湿浸渍K₂CO₃溶液,K的负载量为K/(Ni+Co)=0.05,400℃ 再焙烧制备的催化剂活性较高,有氧有水条件下500℃ 反应时N₂O可完全分解;在NiCoAl复合氧化物表面负载K₂CO₃组分,降低了催化剂表面Co、Ni元素的电子结合能,弱化了表面Co-O、Ni-O化学键,从而提高了催化剂活性和抗水性能。     

铝基类水滑石和复合氧化物负载Pt催化剂的制备及对甲基苯酚加氢脱氧反应的催化性能

采用共沉淀法制备了多种铝基类水滑石,焙烧后得到对应的复合氧化物;以水滑石或复合氧化物为载体,制备了系列Pt基催化剂,研究了该催化剂对甲基苯酚加氢脱氧反应的催化性能。结果表明,Pt基催化剂的性能与载体的组分组成和结构相关;当以不经焙烧的类水滑石做载体时,所制备的Pt基催化剂具有较高的活性。其中,Pt-Ni-Al-H催化剂的加氢脱氧活性最高,对甲基苯酚转化率达到99.8%,甲苯选择性为1.4%,而Pt-Zn-Al-H催化剂的直接脱氧活性最高,在275℃和氢压2MPa下反应1h后,甲苯选择性达到84.1%。研究发现,反应过程中所生成的甲基环己烷可进一步发生脱氢反应转化为甲苯,说明所制备的Pt基催化剂具有较好的脱氢活性,可节省脱氧过程中的氢气消耗量。     

铝基类水滑石和复合氧化物负载Pt催化剂的制备及对甲基苯酚加氢脱氧反应的催化性能（英文）

采用共沉淀法制备了多种铝基类水滑石,焙烧后得到对应的复合氧化物;以水滑石或复合氧化物为载体,制备了系列Pt基催化剂,研究了该催化剂对甲基苯酚加氢脱氧反应的催化性能。结果表明,Pt基催化剂的性能与载体的组分组成和结构相关;当以不经焙烧的类水滑石做载体时,所制备的Pt基催化剂具有较高的活性。其中,Pt-Ni-Al-H催化剂的加氢脱氧活性最高,对甲基苯酚转化率达到99.8%,甲苯选择性为1.4%,而Pt-Zn-Al-H催化剂的直接脱氧活性最高,在275℃和氢压2 MPa下反应1 h后,甲苯选择性达到84.1%。研究发现,反应过程中所生成的甲基环己烷可进一步发生脱氢反应转化为甲苯,说明所制备的Pt基催化剂具有较好的脱氢活性,可节省脱氧过程中的氢气消耗量。     

含钯类水滑石衍生复合氧化物Pd/M3AlO(M=Mg,Co, Ni,Cu, Zn)催化剂上氯苯的催化氧化

采用共沉淀法制备了系列含Pd类水滑石材料, 类水滑石基体为M3Al-HT (M=Mg, Co, Ni, Cu, Zn), 经焙烧制备出含Pd类水滑石衍生复合氧化物催化剂. 通过X射线衍射(XRD), 热重-差热分析(TG-DTG), H2程序升温还原(H2-TPR), O2程序升温脱附(O2-TPD)和N2吸脱附等表征技术手段研究了不同二价金属元素对含Pd类水滑石衍生复合氧化物催化剂物理化学性质及其对挥发性有机污染物氯苯催化氧化性能的影响. XRD和TG-DTG结果表明, 不同二价金属元素, 除Cu外, 都能形成类水滑石层状结构, Pd在不同类水滑石前驱物中均能良好分散. 不同的二价金属元素对催化剂性能的影响不同, 其中Pd/Co3AlO催化剂表现出最高的氯苯催化氧化活性, 其起燃温度和全转化温度分别为182和283 ℃. H2-TPR和O2-TPD测试表明, Pd和类水滑石衍生复合氧化物存在着协同作用, Pd的引入促进了复合氧化物的还原, 从而影响氧化物的氧化还原性能. Pd/M3AlO系列催化剂的活性主要受催化剂的氧化还原性能及其表面活性氧物种的影响.     

制备方法对NiCoPrLa类水滑石及其衍生复合氧化物结构及催化性能的影响

用微波法,水热法和微波水热法合成NiCoPrLa类水滑石,并用XRD,TG,TPO,TPR,TPD和FT-IR等对NiCoPrLa类水滑石的晶相结构、热稳定性及相应的衍生复合氧化物的晶相结构、还原性能、吸附性能和抗积碳性能等进行了表征,同时以乙醇水蒸气重整制氢为探针反应考察了制备方法对NiCoPrLa类水滑石的衍生复合氧化物的初活性和选择性的影响.结果表明,制备方法影响类水滑石的结构和热稳定性,水热法制备的类水滑石结晶度较好,微波水热法制备的类水滑石具有较好热稳定性,其中微波水热法所制备的类水滑石衍生复合氧化物具有较好的催化活性和抗积炭性能,在350℃温度下乙醇转化率达到86%.     

有氧气氛中碱金属改性CuAl复合氧化物催化分解N2O的活性

合成了Cu/Al原子比分别为2.0、3.1、4.1的CuAl类水滑石样品,焙烧得到CuAl复合氧化物。在Cu/Al原子比为3.1的CuAl氧化物表面浸渍碱金属盐溶液,制备改性CuAl复合氧化物,用AES、XRD、FT-IR、BET、H₂-TPR、XPS等技术对催化剂进行了结构表征,考察了CuAl复合氧化物组成、碱金属助剂类型和K的前驱物对改性催化剂在有氧气氛中催化分解N₂O活性的影响。结果表明,Na、K、Cs改性CuAl复合氧化物均提高了催化剂活性,但K助剂的增强效应最显著;钾的不同前驱物改性CuAl复合氧化物的催化活性有显著差异,加入碳酸钾、草酸钾提高了催化剂的活性,而加入醋酸钾、硝酸钾反而降低了催化剂活性。优化出的K改性CuAl复合氧化物催化剂在含氧含水气氛的N₂O分解反应中表现出了较高的活性。     

Soybean biodiesel methyl esters,free glycerin and acid number quantification by 1H nuclear magnetic resonance spectroscopy

Production of alternative fuels, such as biodiesel, from transesterification of vegetable oil driven by heterogeneous catalysts is a promising alternative to fossil diesel. However, achieving a successful substitution for a new renewable fuel depends on several quality parameters. ¹H NMR spectroscopy was used to determine the amount of methyl esters, free glycerin and acid number in the transesterification of soybean oil with methanol in the presence of hydrotalcite‐type catalyst to produce biodiesel. Reaction parameters, such as temperature and time, were used to evaluate soybean oil methyl esters rate conversion. Temperatures of 100 to 180 °C and times of 20 to 240 min were tested on a 1 : 12 molar ratio soybean oil/methanol reaction. At 180 °C/240 min conditions, a rate of 94.5 wt% of methyl esters was obtained, where free glycerin and free fatty acids were not detected. Copyright © 2012 John Wiley & Sons, Ltd.     

水滑石负载钾盐催化酯交换反应合成生物柴油

以水滑石为载体,负载钾盐作为酯交换合成生物柴油的催化剂,采用XRD、Hammett指示剂-苯甲酸滴定、N2吸附-脱附、TG-DSC研究了活性组分和载体类型、焙烧温度和时间以及负载量对催化剂碱性和酯交换活性的影响.H-介于9.3 ～15的中强碱量是决定催化剂活性的主要因素.钾与水滑石高温焙烧形成的相互作用物种是催化剂中强...     

有机阴离子柱撑水滑石催化酯交换合成碳酸二苯酯

 A series of organic anion-pillared hydrotalcites were synthesized by the ion exchange method and characterized by X-ray diffraction and Fourier transform infrared spectroscopy. The hydrotalcite precursor and pillared hydrotalcites with different anions was tested as catalysts in transesterification of dimethyl carbonate (DMC) with phenol. The results show that the catalytic selectivity of this transesterification reaction over these organic anion-pillared hydrotalcites is significantly improved. The catalytic selectivities of C4H4O4-, C6H8O4-, C10H16O4-, 1,4-C8H4O4-, and C7H5O2-pillared hydrotalcites for transesterified products (diphenyl carbonate and methyl phenyl carbonate) are all greater than 90%, at least 10% higher than that of the hydrotalcite precursor. Under the conditions of n(phenol)/n(DMC)=4, catalyst amount=1.5%, and t=10 h, the C6H8O4-pillared hydrotalcite presents the best catalytic performance, and the DMC conversion and the selectivity for transesterified products reach 43.8% and 93.2%, respectively.     

酯交换制生物柴油的CaO固体碱催化剂

用不同的前驱物合成了三种CaO催化剂, 并以X射线衍射(XRD)、扫描电子显微镜(SEM) 、程序升温脱附(TPD)等方法加以表征. 这些CaO被用作大豆油(SBO)经酯交换制取脂肪酸甲酯(FAME), 即生物柴油的催化剂, 由方解石制备的氧化钙(Cal(N))表现了最好的SBO酯交换活性. 检测发现CaO的酯交换活性与它们的碱性强度密切相关, 当暴露于CO2气氛下, 显著降低了CaO的酯交换催化活性(Raman光谱测试显示当置CaO于常温空气中, 其表面形成的CaCO3和Ca(OH)2将阻止CaO继续参与SBO的酯交换反应). CO2的毒化颇受制于CaO前驱体种类, Cal(N)比来自文石的CaO(即Ara(N))有更好的抗CO2毒化能力; 这些受损的CaO催化活性可部分复原. 提出了CaO催化剂受CO2毒化及其再生的机理, 同时讨论了SBO酯交换活性相到底是CaO固体表面, 拟或溶解了的CaO的问题.     

Thermal characterization of hydrotalcite used in the transesterification of soybean oil

Hydrotalcite was synthesised by co-precipitation method, calcined and characterized by XRD, BET, IR and TG/DTA/DTG analyses and tested as solid base catalyst in the transesterification of soybean oil with methanol, achieving a methyl ester content of 99.5%. The thermal decomposition of hydrotalcite calcined occurred in four mass loss steps at 28, 105, 203 and 400 °C. The hydrotalcite was recovered and through a simple evaluation by TG/DTA/DTG techniques it was found that at 500 °C is the temperature, where the organic matter should be eliminated from the catalyst. This study shows the importance of thermal analysis in the evaluation of the recovery temperature of hydrotalcite.     

Brønsted双核碱性离子液体的合成及其在制备生物柴油过程中的催化性能

以N-甲基吗啡啉和1,4-二溴丁烷为原料,通过两步法合成了新型Brønsted碱性双核离子液体.分别采用¹H-NMR、FT-IR和元素分析对合成的离子液体进行结构分析;采用TGA测试离子液体的热稳定性;同时测定了离子液体的溶解性和碱性.此外,考察了双核碱性离子液体在大豆油和甲醇酯交换反应中的催化活性.结果表明,当甲醇:大豆油=14:1(物质的量比)、离子液体用量为大豆油质量的5%、反应时间5 h、反应温度60 ℃时、生物柴油收率为 95.6%(质量分数),且离子液体经回收、真空干燥,重复使用6次后催化活性没有明显降低,仍能达到94%以上.     

花球状镁铝复合氧化物负载Ni⁃Co催化剂的合成及正十二烷水蒸气重整制氢

采用水热晶化的方法制备了花球状镁铝层状水滑石材料,经过高温焙烧和氢气还原成功制备了镁铝复合氧化物负载的Ni?Co合金催化剂。通过扫描电子显微镜、透射电子显微镜、氮气吸附-脱附测试、粉末X射线衍射、程序升温还原等技术表征了所制备催化剂的物理化学性质,并且测试了所制备催化剂催化正十二烷水蒸气重整制氢性能。实验结果表明:水热晶化后催化剂的前驱体是花球状层状水滑石结构,焙烧后催化剂以复合氧化物的结构存在,且存在非常丰富的介孔和大孔。通过调控Co的加入量,可以调控金属载体相互作用的强度及金属颗粒尺寸。还原后,Ni和Co形成合金且均匀地分布在层状薄片镁铝复合氧化物上面。所制备的催化剂用于正十二烷水蒸气重整制氢,结果显示,相比于Ni单金属催化剂,形成Ni?Co合金的催化剂的活性及产氢率均有较大程度的提升,且抗积碳性能大幅度提高。这归因于Ni?Co协同的合金状态和较小的金属纳米颗粒尺寸。     

Optimization of biodiesel production via transesterification of soybean oil using α-MoO3 catalyst obtained by the combustion method

A catalyst based on MoO₃ was synthesized by a simple and fast pilot-scale combustion reaction method and applied to the conversion of soybean oil to biodiesel via transesterification. For that, the statistical analysis of the catalyst amount and temperature, factors that influence the process, was evaluated by means of central composite design 2². MoO₃ was characterized in terms of structure by X-ray diffraction (XRD), textural characterization Brunauer-Emmett-Teller (BET), density by helium pycnometry (DE), particle size analysis (DG) and acidity tests by temperature-programmed desorption of ammonia (NH₃-TPD), chemical analysis by X-ray fluorescence (EDX), morphology by scanning electron microscopy (SEM) and catalytic properties. The transesterification products were characterized by gas chromatography (GC), acidity index (AI) and kinematic viscosity (KV). The results indicate the catalyst formation with a surface area of 1.36 m²g^?1, and density of 4.5 g/cm³ which consists of a single crystalline phase of orthorhombic configuration, with total NH₃ acidity of 33.61 μ.mol/g. Morphological characterization revealed that the catalyst is formed by irregular plates of various sizes and shapes, with a wide sizes range of agglomerated particles. In the soybean oil transesterification reactions, the catalyst was active showing 96.9% conversion to ethyl esters. The experimental design was meaningful and predictive, with a reliability level of 95%. The statistical analysis identified temperature as a significant variable for the adopted planning. To conclude, a new single-phase catalyst (α-MoO₃) has been developed and successfully applied to the biodiesel Synthesis from soybean oil. These results have a positive and promising impact for biodiesel production by transesterification of soybean oil against ethanol.     

XRD and TPR Studies of Cu-Al Hydrotalcite Derived Highly Dispersed Mixed Metal Oxides

A series of Cu/Al catalysts, containing different proportions of copper and aluminium, have been prepared by coprecipitation using metal nitrate precursors and Na₂CO₃. The dried precipitate catalyst precursors were characterized by X-ray diffraction (XRD) to show the presence of Cu-Al binary hydrotalcite-like phase. The dried precipitates were calcined at 873 K for 3 h. The calcined catalysts were characterized by XRD and temperature-programmed reduction (TPR) methods to show the presence of unidentified mixed oxides. The results showed that the extent of metal-support interaction increased with copper loading due to the mixed oxides formed from the hydrotalcite-type phase during calcination. High dispersion of the mixed metal oxides was indicated by comparison with similar studies on Cu-Al catalysts, prepared by similar methods, whose precursors showed no hydrotalcite formation.