Tetradecanol dehydrogenation over CuO catalyst supported on BaO, CaO and MgO

Bimetallic Cu/Mg, Ca, Ba mixed oxide compounds acted as catalyst in the dehydrogenation of tetradecanol into tetradecanal, and were characterized by thermal gravimetric analysis, surface area, X-ray diffraction, temperature-programmed reduction and desorption of CO₂. Alkaline earth oxides increased the total basic site concentration in the order of Mg>Ca>Ba. A correlation was found between the total basic site concentration and initial dehydrogenation rate. This revised version was published online in June 2006 with corrections to the Cover Date.     

亚微米ZSM-5负载Cr催化剂上乙烷CO2气氛下脱氢制乙烯

石油资源的日趋短缺使天然气和页岩气的开发利用受到重视,因而低碳烷烃脱氢制取低碳烯烃也随之引起了人们越来越多的关注.由于乙烷纯脱氢反应的平衡收率低,能耗高,而氧气氧化脱氢又易将乙烷深度氧化为CO2或CO,因此开发具有反应条件温和、装置投资和操作费用低等优势的CO2气氛下乙烷脱氢的技术路线日益得到重视. CrOx是该反应理想的催化剂之一, CO2的加入可使CrOx对乙烷脱氢的催化活性提升3倍,然而受困于CrOx过小的比表面积,通常将CrOx制备成负载型催化剂使用. CrOx的常见载体有Al2O3, ZrO2和SiO2等氧化物及MCM-41, SBA-15, SBA-1和MSU-x等介孔硅材料, ZSM-5作为载体负载CrOx用于低碳烷烃脱氢的研究则较少,所得结果也不甚理想.我们采用亚微米尺寸的ZSM-5作为载体制备了负载型CrOx催化剂,研究了其在CO2气氛下催化乙烷脱氢反应,发现该催化剂具有非常优异的脱氢活性,高硅铝比和Na型的ZSM-5作载体对反应更加有利,而且在反应进行50 h后,催化剂依然保持很好的活性和很高的乙烯收率,这是在一般负载型CrOx催化剂上所不能实现的.
　　X射线光电子能谱(XPS)表征发现, Na型ZSM-5载体制得的催化剂具有更高的Cr6+/Cr3+比.一般认为, Cr6+是Cr系催化剂进行低碳烷烃脱氢反应时的活性位(或活性位前驱体),因此可以初步判定, Na型载体具有很好催化效果的原因可能是由它制得的催化剂具有更多的反应活性位.程序升温还原(H2-TPR)表征结果证实了这一点, Na型载体明显具有更高的H2消耗量;也就是说, Na型载体制得的催化剂具有更多的可还原Cr物种,即脱氢活性位.进一步表征发现,反应活性还与Cr物种存在形式有关.文献报道,低聚态的Cr物种和孤立态的Cr物种比Cr2O3有更好的催化活性.通过漫反射紫外-可见光谱(UV-Vis)对Cr物种的存在形态进行表征后发现, Na型载体上Cr主要以四配位形式存在,而在H型载体上出现了对应于六配位的Cr物种;激光Raman表征结果表明, Na型载体上出现的都是低聚态Cr物种和孤立态Cr物种,而H型载体上出现了明显的对应于α-Cr2O3的峰,说明相较于H型载体, Na型载体更有利于Cr组分分散,这也是Na型ZSM-5载体催化剂具有更高活性的原因之一.
　　CO2引入后对乙烷脱氢反应具有明显的促进作用,特别是在CO2/C2H6=5时,催化剂上C2H6转化率是非CO2气氛下的3.2倍;同时, CO2的引入也提高了脱氢反应的稳定性.在非CO2气氛下,反应进行6 h后, C2H6转化率降低到初活性的60%左右,而在CO2/C2H6=5时,相同时间内催化剂活性下降仅有5%左右.实验分析了CO2对脱氢反应具有促进作用的原因.在脱氢反应温度650 oC下, CO2/H2=1时进行了逆水煤气反应测试,发现CO2的转化率达到22.5%,说明引入CO2后可以通过逆水煤气反应有效地消耗掉乙烷脱氢反应生成的H2,从而促进反应向脱氢方向进行; CO2的引入也可以促进Cr物种的CrOx/CrOx-1循环,从而提高催化剂效率,减缓催化剂失活; CO2还可与反应中生成的积碳类物质发生Boudouard反应,将反应活性位暴露出来,从而提高催化剂的稳定性. CO2气氛下反应6 h后催化剂的积碳量为3.0%,低于非CO2气氛下的3.4%,同时在脱氢反应中生成的CO量与消耗掉的CO2量的比值约为1.4,也有力地说明Boudouard反应的存在.     

HCl存在下CeO2基催化剂上乙烷氧化脱氢制乙烯

报道了一种HCl存在时温和条件下的乙烷氧化脱氢制乙烯催化转化新途径. 研究发现,在多种金属氧化物催化剂中,CeO₂呈现最佳乙烯生成的催化性能. 与纳米粒子相比,具有棒状和立方体状形貌的CeO₂纳米晶具有较高的乙烷转化率和乙烯选择性. 以MnO_x修饰CeO₂可进一步提高催化性能. 在8 wt% MnO_x-CeO₂催化剂上,723K反应2 h时乙烷转化率和乙烯选择性分别为94%和69%. 该催化剂性能稳定,反应100 h乙烯收率可保持在65%-70%. HCl的存在对乙烯的选择性生成起着至关重要的作用,一部分乙烯来自于氯乙烷的脱HCl反应.     

Oxidative dehydrogenation of ethane with carbon dioxide over sulfated zirconia supported metal oxides catalysts

Several metal oxides supported on sulfated zirconia catalysts were tested for the oxidative dehydrogenation of ethane into ethylene by carbon dioxide. It is found that the catalytic behavior of supported oxide catalysts differ depending on the nature of metal oxides. Chromium oxide-sulfated zirconia exhibits the highest ethane conversion and medium level of ethylene selectivity, producing 38% ethylene yield at 50% ethane conversion at 650°C.     

Oxidative dehydrogenation of ethane over movmnw oxide catalysts

Catalysts based on mixed oxide of MoVMn are active at relatively low temperature for oxidative dehydrogenation of ethane. Incorporation of tungsten into MoVMn oxides enhances the catalytic activity. Enhancement of the activity is explained in the light of acid-base interaction accompanied with a redox mechanism of surface reoxidation. This revised version was published online in June 2006 with corrections to the Cover Date.     

Oxidative dehydrogenation of propane

At temperatures near 650°C and residence times ofca. 3 s, the homogeneous oxidative dehydrogenation (OXD) of propane to propylene and ethylene approached oxygen limiting conditions, even when the reactor was filled with quartz chips. The addition of catalysts that are known to be effective in the OXD of ethane slightly increased the reaction rate, but the selectivities at a given conversion level were the same as those that were achieved in the homogeneous reaction.     

Oxidative dehydrogenation of ethane to ethylene with carbon dioxide over supported Ga,Fe, and Cr-containing catalysts

Oxydative dehydrogenation of ethane to ethelene over Ga-, Fe- and Cr-oxide systems has been investigated. CO₂ was used as an oxidizing agent. The activity and stability of the synthesized catalysts were studied. The most efficient catalytic system was selected and the experimental conditions for the optimal conversion/selectivity ratio were found.     

乙烷在氧化镍上催化氧化脱氢的反应机理研究

应用O~2-TPD,脉冲实验,原位Weiss磁测量以及TAP(temporalanalysisofproducts)技术对NiO上的乙烷氧化脱氢制乙烯催化作用机理进行了研究。结果表明,NiO中的非化学计量氧表现出与气相氧交换的可逆性,其中在较低温度下脱附的α氧(很可能是O~2^-,O~2^2^-)仅存在于催化剂表面,与气相氧交换迅速,而较高温下脱附的β氧(很可能是O^-)不仅存在于催化剂表面,还存在于催化剂体相。β氧较α氧表现出更高的乙烯选择性。在反应条件下,Ni均应处于高氧化态(Ni^(^2^+^δ^)^+,0≤δ≤1),一旦催化剂中有微量Ni^0生成,乙烷便发生裂解反应,乙烯选择性立即降为零。乙烷在NiO上的氧化脱氢(ODHE)的可能反应机理为:首先乙烷与NiO中的非化学计量氧O~n(~s~)作用脱除一个α-H生成乙基自由基,然后进一步脱除一个β-H生成乙烯,乙烯生成的整个过程是在催化剂表面上进行的;副产物CO~2是由表面乙烯进一步氧化(很可能是与O~2^-,O~2^2^-作用)生成的。失去O~n~(~s~)的NiO在反应体系(一定的氧分压)中,重新生成含非化学计量氧的NiO。     

Room temperature dehydrogenation of ethane to ethylene

The transient titanium alkylidyne, (PNP)Ti≡C(t)Bu (PNP = N[2-P(i)Pr(2)-4-methylphenyl](2)(-)), activates a C-H bond of ethane at room temperature, and a β-hydrogen of the resulting ethyl ligand is subsequently transferred to the adjacent alkylidene ligand to form an ethylene adduct of titanium. Treatment of the ethylene complex with two-electron oxidants such as organic azides results in extrusion of ethene concomitant with formation of a mononuclear titanium imido complex.     

Oxidative dehydrogenation of ethane to ethene over a superbase supported LiCl system

<正>LiCl-promoted superbase catalysts were found to be stable and highly selective to ethene for oxidative dehydrogenation of ethane,giving 84%ethane conversion and 74%ethene yield at 923 K.Results indicated that the stronger the basicity of LiC1-based catalysts,the better the catalytic performance.     

Oxidative dehydrogenation of ethane over sufated zirconia supported oxides catalysts

The oxidative dehydrogenation of ethane into ethylene has been investigated on metal oxide-based sulfated zirconia catalysts at temperatures of 400–600°C. It is found that the activity and selectivity toward ethylene depend on the nature of metal oxide and temperature and that Ni and V oxides supported on sulfated zirconia exhibited higher ethylene yields.     

Oxidative dehydrogenation of propane over Ni-Mo-Mg-O catalysts

In this work, a series of Ni-Mo-Mg-O catalysts with mesoporous structure prepared by sol-gel method were investigated for the oxidative dehydrogenation of propane (ODHP). The techniques of temperature-programmed reduction with H2 (H2-TPR), N2 adsorption-desorption, Fourier transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD) and X-ray photoelectron spectra (XPS) were employed for catalyst characterization. It is found that the activity of the catalysts for ODHP increases first and then decreases with the increase of Mo content. The catalyst with a Mo/Ni atomic ratio of 1/1 exhibits the best catalytic activity, which gives the propene selectivity of 81.4% at a propane conversion of 11.3% under 600°C and maintains the good catalytic performance for 22 h on stream. This is related not only to its high reducibility and dispersion as revealed by TPR and XRD, but also to the formation of more selective oxygen species on the MoOx-NiO interface as identified by XPS.     

羟基化氮化硼催化乙烷氧化脱氢制乙烯

乙烯是最为重要的化工原料之一,目前其工业来源主要来自于烃类的水蒸汽裂解过程.该过程本质上是一个高温均相裂解过程,温度(>800?℃)高,能耗大,碳排放严重.乙烷氧化脱氢制乙烯属于放热反应,反应温度低,速率快,无积碳等限制,是一条更富有竞争力的工艺路线.然而,常用的金属或金属氧化物催化剂容易导致乙烯深度氧化,从而降低了乙烯选择性.纳米碳材料在烃类氧化脱氢反应中展现出一定的催化活性,但容易被氧化,难以用于反应温度高的乙烷氧化脱氢反应.本文报道了羟基化的氮化硼(BNOH)可高效催化乙烷氧化脱氢制乙烯.氮化硼边沿羟基官能团脱氢生成了动态活性位,从而引发了乙烷的脱氢反应.BNOH对乙烷氧化脱氢制乙烯显示出高选择性.当乙烷转化率在11%,乙烯选择性可高达95%;当乙烷转化率增加到40%,乙烯选择性保持在90%.重要的是,当乙烷转化率超过60%时,BNOH仍然可保持80%的乙烯选择性以及50%的乙烯收率.这些性能指标与现有工业乙烷水蒸气裂解过程运行性能相当.进一步优化反应条件,BNOH催化剂能够实现高达9.1 gC2H4 gcat-1 h-1的时空收率.经过200 h的氧化脱氢反应测试,BNOH催化剂活性和选择性基本恒定,表明其具有非常好的稳定性.X射线粉末衍射结果显示,反应前后BNOH催化剂的物相没有发生变化.透射电子显微镜测试证实,反应后BNOH催化剂的形貌和微观结构也没有明显改变.X射线光电子能谱结果显示,反应200 h后BNOH催化剂表面的氧含量仅从反应前的6.9 atom%微增到8.3 atom%.1H固体核磁共振谱测试显示,反应200 h后,BNOH催化剂上羟基含量无明显改变.结合原位透射红外光谱和同位素示踪实验,初步确定了BNOH催化剂上引发乙烷氧化脱氢反应的活性中心.氮化硼边沿的氧官能团并不能引发乙烷的氧化脱氢反应,而羟基官能团才是氧化脱氢反应发生的活性位.在乙烷氧化脱氢条件下,分子氧脱除羟基官能团上的氢原子动态生成BNO·?和HO2·?活性位.密度泛函理论计算表明,乙烷首先在BNO·?或HO2·?位活化生成乙基自由基,这些中间物进一步与气相氧物种发生反应脱氢生成乙烯.动力学测试结果也验证了上述实验和理论结果.     

活性炭负载Pt-Ni双金属催化剂上十氢化萘脱氢

采用等体积浸渍法制备了活性炭负载的具有脱氢活性的Pt-Ni双金属催化剂及相应的Pt单金属催化剂,并用X射线衍射、N2吸附-脱附和NH3-程序升温脱附对其进行了表征.在290°C下,研究了间歇反应条件下催化剂以过热液膜状态催化十氢化萘脱氢活性,考察了温度、浸渍顺序和Pt/Ni摩尔比对十氢化萘脱氢活性和萘产率的影响.结果表明,与单金属催化剂相比,Pt-Ni双金属催化剂上产氢效率显著提高.当Pt/Ni摩尔比为1:1,Pt首先浸渍时,得到的催化剂上脱氢转化率和萘产率最高.将实验结果与密度泛函理论计算的氢原子在不同催化表面的结合能关联证实,具有更强原子氢结合能的双金属表面具有更高的脱氢活性.     

Oxidative dehydrogenation of ethane and propane on CuTh oxide catalysts

CuThO oxides prepared with different atomic ratios Cu/Th have been tested in the oxidative dehydrogenation of ethane and propane. These catalysts are active and selective in the formation of ethene and propene, but the activity and selectivity change with the nature of the alkane.     

Theoretical study of Sn adsorbed on the MgO(100) surface with defects

In this study, the adsorption of Sn atom at various sites on the MgO(100) surface was characterized using a theoretical approach based on density functional theory calculations. Both regular adsorption centers (O^2? and Mg²⁺) and defects (such as neutral and charged O and Mg vacancies) were considered. Several key parameters for these sites with the adsorbed Sn atom were determined to provide its geometric, energetic, and electronic characterization. The interaction between Sn and the Mg vacancy sites is very strong and is associated with a relatively small distance of the adsorbed Sn atom from the surface and with a large electronic charge transfer from Sn to the surface. A much smaller strength of Sn atom adsorption is observed for the O vacancies and regular sites. Among them, the ${{\text{F}}_{\text{s}}}^{\text{0}}$ center binds the Sn atom strongest and, in consequence, this atom acquires a significant amount of electronic charge.     

溶胶-凝胶法制备Cr-基催化剂及其CO2氧化乙烷制乙烯

以硝酸铬为Cr源,正硅酸乙酯为Si源,采用溶胶-凝胶法制备了Cr质量分数为2.5%~10%的Cr-基催化剂;采用XRD、BET、SEM、H₂ TPR等分析测试技术对催化剂的结构进行了表征;在微型固定床反应器中对催化剂乙烷二氧化碳氧化脱氢制乙烯的催化性能进行了评价,并考察了反应条件对催化性能的影响。结果表明,催化剂中Cr的质量分数大于5%时,Cr的物相为Cr₂O₃,但Cr质量分数较低时,检测不到Cr的物相;Cr质量分数为5%的催化剂具有较大的比表面积,Cr质量分数变大或变小,催化剂的比表面积都会减小;催化剂的孔径在2nm左右,并与Cr的质量分数关系不大;Cr质量分数为5%的催化剂具有最好的催化活性,在750℃的反应条件下,乙烷和二氧化碳的转化率可达79.29%和23.74%,乙烯的收率可达67.91%;Cr质量分数为5%的催化剂具有适宜的氧化还原性能,这有利于乙烷和二氧化碳的转化。     

In situ CO2 reactivation of FeCrOx/C catalyst in the oxidative dehydrogenation of ethane to ethylene

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Magnesium promoted autocatalytic dehydrogenation of amine borane complexes: A reliable,non-cryogenic,scalable access to boronic acids

Owing to the unusual reactivity of dialkylamine-borane complexes, a methodology was developed to simply access boronic acids. The intrinsic instability of magnesium aminoborohydride was tweaked into a tandem dehydrogenation borylation sequence. Proceeding via an autocatalytic cycle, amineborane dehydrogenation was induced by a variety of Grignard reagents. Overall, addition of the organomagnesium species onto specially designed dialkylamine-borane complexes led to a variety of boronic acids in high yields. In addition, the reaction can be performed under Barbier conditions, on a large scale.     

Oxidative dehydrogenation of ethane over Cr/ZSM-5 catalysts using CO2 as an oxidant

Highly active catalysts for oxidative dehydrogenation of ethane with CO2 were characterized by temperature-programmed reduction (TPR), temperature-programmed oxidation (TPO), Fourier transform infrared (FTIR) spectroscopy, and X-ray absorption fine-structure (XAFS) analysis. In the active catalysts, Cr/H-ZSM-5 (SiO2/Al2O3 > 190), Cr6+ = O, or possibly Cr5+ = O was the catalytic species on the zeolite support. In contrast, little Cr6+ (or Cr5+) was detected in the less-active catalysts. The Cr6+ (or Cr5+) species was reduced to an octahedral Cr3+ species by treatment with ethane at 773 K, and the reduced Cr species was reoxidized to the Cr6+ (or Cr5+) species by treatment with CO2 at 673-773 K. The Cr redox cycle played an important role in the catalyst's high activity.