稀土氧化钐上甲烷氧化偶联反应的FT—IR研究

用傅里哀变换红外(FT-IR)光谱原位考察了稀土氧化钐上甲烷氧化偶联反应及乙烯,乙烷的氧化反应。在700℃以下,甲烷,乙烯和乙烷分别与氧化钐表面反应时,除检测到表面碳酸基外,未观察到其它表面物种。这些表面碳酸基物种只有在700℃以上才大部分脱附,在氧存在下,高于700℃时这些低碳烃的完全氧化很显著,但在内循环反应体系中发现过量的气相CO_2可抑制烃类的深度氧化。甲烷的偶联反应在700℃以上才可明显观察到。而大部分表面碳酸基也在700℃以上才脱附,但经脱碳酸基或高温氧化处理后的氧化钐上均未明显观察到O~-物种的ESR峰。本文认为经高温脱碳酸基后形成的表面配位不饱和氧物种O~(δ-)(1<δ<2)在甲烷氧化偶联反应中起主要作用。     

甲烷在SrO-La2O3/CaO催化剂上的氧化偶联Ⅲ.动力学处理及其反应机理

动力学的比较研究发现,在20％La_2O_3/CaO(LC)催化剂中添加SrO(SLC),改变了甲烷氧化偶联的反应机制。根据前文的动力学实验结果,提出了简化的反应网络和几种反应机理,并且进行了动力学处理。结果表明,在LC催化剂上的甲烷氧化偶联满足Langmuir-Hin-shelwood机理,反应的活性氧物种为分子态吸附氧物种O_2~*,CO_x来源于[CH_3·]同气相分子氧的相互作用;而SLC催化剂的甲烷氧化偶联却满足修正的Rideal-Redox机理,反应的活性氧物种为表面氧物种O~-,CO_x由[CH_3·]同O~-的相互作用产生。     

Rh／SiO2催化剂上甲烷部分氧化制合成气反应

 利用程序升温脱附、程序升温还原、程序升温表面反应、程序升温反应和化学捕获反应等手段，对Rh／SiO2催化剂上甲烷部分氧化制合成气反应进行了研究．结果表明，Rh／SiO2催化剂上甲烷部分氧化制合成气机理属于热解－氧化反应机理．甲烷首先在催化剂上发生解离吸附，产生具有不同H／C比的化学吸附物种CHx（x＝1～3）．其中，具有较高H／C比的CHx可能是甲烷部分氧化反应的活性物种，而具有较低H／C比的CHx可能是催化剂上积碳并导致催化剂失活的来源．活性物种CHx在活性氧物种的作用下，生成含氧中间体物种CHxO或继续脱氢．含氧中间体物种进一步分解，即生成CO和H2；CO2也可由CHx或CHxO物种进一步氧 化生成．     

Ir/SiO2上甲烷部分氧化制合成气反应的原位时间分辨红外和原位Raman光谱表征

采用原位时间分辨红外光谱和原位显微Raman光谱技术对Ir/SiO₂上甲烷部分氧化(POM)制合成气反应的初级产物和反应条件下催化剂表面物种进行了跟踪考察,实验结果表明,在H₂预还原的新鲜Ir/SiO₂表面,CO是V(CH₄):V(O₂):V(Ar)=2:1:45混合气反应的初级产物,因而甲烷的直接氧化过程是CO生成的主要途径;而在稳态反应条件下,CO生成的途径可能主要来自CO₂和H₂O与催化剂表面积碳物种(CHx)和/或CH₄的反应.催化剂上生成的积碳可能是导致稳态条件下Ir/SiO₂上POM反应机理不同于H₂预还原的新鲜催化剂的主要原因.     

甲烷催化部分氧化制合成气的反应机理

借助脉冲反应、质谱-程序升温表面反应（MS-TPSR）等技术研究了Ni／α-Al2O3催化剂上甲烷催化部分氧化制合成气（POM）的反应机理．结果表明,NiO上CH4不能解离产生H2只有当NiO被CH4还原为Ni0后,CH4才能解高产生H2,Ni0是CH4活化和POM反应的活性相;POM反应机理遵循直接氧化机理,CH4和O2均在Ni0上活化,活化过程形成的Ni…C和Niδ…Oδ物种是反应历程中的关键物种,Niδ …Oδ物种高选择性地与CH4解离产生的碳物种Ni…C反应生成CO．     

稀土Pr6O11上CO和表面羟基反应的原位FT-IR研究

利用FT-IR原位考察了稀土氧化镨上CO和表面羟基的反应。在473K以下,未检测到CO和氧化镨表面反应的吸附物种;在CO气氛中,升温到473K,观察到甲酸根吸附物种的红外特征峰1578,1371和1367cm~(-1)。用同位素D_2部分还原的氧化镨吸附CO以及甲酸吸附证实了CO与氧化镨表面的羟基反应可生成表面甲酸根吸附物种。讨论了CO在氧化镨表面的反应机理及甲酸根的氧化过程。     

甲烷氧化偶联W-Mn／SiO2催化剂上02-脉冲频率效应（PFE）的研究

采用频率脉冲反应方法，以Mn-Na2WO4／SiO2催化剂上甲烷氧化偶联为探针反应，通过实时、原位的四极质谱检测手段，研究氧物种对甲烷C-H键选择性活化的微观历程．首次发现了Mn-Na2 WO4／SiO2催化剂上O2-脉冲频率效应，即脉冲反应产物量随氧脉冲注入频率的增加而增加．研究结果表明。在反应条件下，Mn-Na2 WO4／SiO2催化剂上有两种活化甲烷的氧物种同时存在，它们活化甲烷的方式不同。     

甲烷氧化偶联W-Mn/SiO2催化剂上O2-脉冲频率效应(PFE)的研究

采用频率脉冲反应方法,以Mn-Na2WO4/S iO2催化剂上甲烷氧化偶联为探针反应,通过实时、原位的四极质谱检测手段,研究氧物种对甲烷C-H键选择性活化的微观历程.首次发现了Mn-Na2WO4/S iO2催化剂上O2-脉冲频率效应,即脉冲反应产物量随氧脉冲注入频率的增加而增加.研究结果表明,在反应条件下,Mn-Na2WO4/S iO2催化剂上有两种活化甲烷的氧物种同时存在,它们活化甲烷的方式不同。     

Pd/MWCNTs贫燃甲烷催化燃烧性能研究

以MWCNTs为载体,用HNO_3做氧化剂对MWCNTs进行处理,通过XPS研究了处理前后MWCNTs表面官能团的变化,并采用超声浸渍法制得Pd/MWCNTs催化剂,借助TEM,揭示了Pd粒子在催化剂表面分散度和粒径与MWCNTs表面含氧量、羟基和羰基间的关系。并考察了Pd/MWCNTs催化剂预处理方法对低浓甲烷催化燃烧活性和稳定性的影响,研究表明,Pd的价态以及Pd粒子的粒径,都与催化剂的甲烷燃烧活性直接关联。单质Pd的氧化和Pd粒径的长大是导致催化剂性能衰减的原因。通过原位FT-IR技术对反应气氛下中间物种的监测,提出了Pd/MWCNTs催化剂上的低浓度甲烷催化氧化反应机理。     

Ni/Al2O3催化剂上甲烷部分氧化制合成气反应CO2主要来源

负载型金属催化上甲烷催化部分氧化剂合成反应机理存在着燃烧－重整机理和直接氧化之争,如果反应按燃烧－重整机理进行,则ＣＯ２则是反应的一次产物而ＣＯ２是二次产物;如果反应按直接氧化机理进行,则ＣＯ是一次产物。本文采用同位素瞬变技术,对Ｎｉ／Ａｌ２Ｏ３催化上甲烷部分氧化制合成气反应中ＣＯ２的来源进行了研究,结果表明ＣＯ２同ＣＯ－样,主要来源于催化剂表面ＮｉＯ与甲烷分解生成的ＮｉｘＣ的反应,这就有力地证明     

Platinum- and CuOx-Decorated TiO2 Photocatalyst for Oxidative Coupling of Methane to C2 Hydrocarbons in a Flow Reactor

Oxidative coupling of methane (OCM) is considered one of the most promising catalytic technologies to upgrade methane. However, C₂ products (C₂H₆/C₂H₄) from conventional methane conversion have not been produced commercially owing to competition from overoxidation and carbon accumulation at high temperatures. Herein, we report the codeposition of Pt nanoparticles and CuO_x clusters on TiO₂ (PC-50) and use of the resulting photocatalyst for OCM in a flow reactor operated at room temperature under atmospheric pressure for the first time. The optimized Cu_0.1Pt_0.5/PC-50 sample showed a highest yield of C₂ product of 6.8 μmol h⁻¹ at a space velocity of 2400 h⁻¹, more than twice the sum of the activity of Pt/PC-50 (1.07 μmol h⁻¹) and Cu/PC-50 (1.9 μmol h⁻¹), it might also be the highest among photocatalytic methane conversions reported so far under atmospheric pressure. A high C₂ selectivity of 60 % is also comparable to that attainable by conventional high-temperature (>943 K) thermal catalysis. It is proposed that Pt functions as an electron acceptor to facilitate charge separation, while holes could transfer to CuO_x to avoid deep dehydrogenation and the overoxidation of C₂ products.     

On the porous structure of coals: Evidence for an interconnected but constricted micropore system and implications for coalbed methane recovery

An experimental and theoretical study of adsorption and diffusion of carbon dioxide and methane in coals of widely varying rank was carried out. Low pressures adsorption isotherms of CO₂ were obtained and analyzed using Dubinin's theory of volume filling of micropores. High-pressure adsorption isotherms of CH₄ were obtained and analyzed using tracer pulse chromatography in conjunction with an appropriate adsorption/diffusion model. A preliminary¹²⁹Xe NMR analysis of chemical shifts experienced by xenon atoms in particles of different sizes is also reported.The heretofore undocumented and/or underestimated effects of activated diffusion of CO₂ at 273–298 K complicate the elucidation of the true microporous structure of coals, especially its dependence on coal rank. Activated diffusion of both CO₂ and methane at room temperature does not allow reliable estimates of coalbed gas content to be made. A model of an interconnected network of pores which includes randomly distributed, numerous and ultramicroporous constrictions (at any size scale) is consistent with all these experimental and theoretical findings.Presented in part at the International Conference on Coal Science, Banff, Alberta, Canada. September 1993, and at the 21st Biennial Conference on Carbon, Buffalo, NY, June 1993.     

Experimental investigation of fluidized-bed reactor performance for oxidative coupling of methane

Performance of the oxidative coupling of methane in fluidized-bed reactor was experimentally investigated using Mn-Na2WO4/SiO2,La2O3/CaO and La2O3-SrO/CaO catalysts.These catalysts were found to be stable,especially Mn-Na2WO4/SiO2 catalyst.The effect of sodium content of this catalyst was analyzed and the challenge of catalyst agglomeration was addressed using proper catalyst composition of 2%Mn2.2%Na2WO4/SiO2.For other two catalysts,the effect of Lanthanum-Strontium content was analyzed and 10%La2O 3-20%SrO/CaO catalyst was found to provide higher ethylene yield than La2O3/CaO catalyst.Furthermore,the effect of operating parameters such as temperature and methane to oxygen ratio were also reviewed.The highest ethylene and ethane (C2) yield was achieved with the lowest methane to oxygen ratio around 2.40.5% selectivity to ethylene and ethane and 41% methane conversion were achieved over La2O3-SrO/CaO catalyst while over Mn-Na2WO4 /SiO2 catalyst,40% and 48% were recorded,respectively.Moreover,the consecutive effects of nitrogen dilution,ethylene to ethane production ratio and other performance indicators on the down-stream process units were qualitatively discussed and Mn-Na2WO4/SiO2 catalyst showed a better performance in the reactor and process scale analysis.     

Rule of 100:An inherent limitation or performance measure in oxidative coupling of methane?

The oxidative coupling of methane over La 2 O 3 /CaO type-catalyst in a fixed-bed reactor is studied under a wide range of operating conditions(973相似文献   

Syntheses and structural characterization of heterometallic bis(pyrazolyl)methane complexes of rhenium and platinum

The new heterometallic complex {μ-1,3,5-[CH(pz)₂]₃C₆H₃}[Re(CO)₃Br][Pt(p-tolyl)₂]₂ has been prepared by reaction of 1 equiv. of the dimer [Pt(p-tolyl)₂(μ-SEt₂)]₂ with the monometallic rhenium precursor {1,3,5-[CH(pz)₂]₃C₆H₃}Re(CO)₃Br, where 1,3,5-[CH(pz)₂]₃C₆H₃ is the tritopic, arene-linked bis(pyrazolyl)methane ligand 1,3,5-tris[bis(1-pyrazolyl)methyl]benzene. Similarly, the heterometallic complex {μ-1,3,5-[CH(pz)₂]₃C₆H₃}[Re(CO)₃Br]₂[Pt(p-tolyl)₂] has been made by the reaction of the dirhenium compound {μ-1,3,5-[CH(pz)₂]₃C₆H₃}[Re(CO)₃Br]₂ and one-half of an equivalent of [Pt(p-tolyl)₂(μ-SEt₂)]₂. X-ray crystallographic studies of the new compounds reveal significant noncovalent interactions in their molecular and supramolecular structures.     

Partial Oxidation of Methane to Methanol with Oxygen or Air in a Nonequilibrium Discharge Plasma

The partial oxidation of methane to methanol with oxygen or air was investigated experimentally and theoretically in a dielectric-barrier discharge (DBD). The predominant parameters of specific electric energy, oxygen content, flow rate, temperature, and gas pressure were determined in CH ₄ /O ₂ and CH ₄ /air mixtures. Optimum selectivities toward methanol formation were found at an oxygen concentration of about 15% in both feed gas mixtures. Low specific energy favors the selectivity toward methanol and suppresses the formation of carbon oxides. The experiments indicate that high methanol selectivities can be obtained at high methane conversion. The highest methanol yield of 3% and the highest methanol selectivity of about 30% were achieved in CH ₄ /O ₂ mixtures. In CH ₄ /air mixtures, as high as 2% methanol yield was also obtained. In addition, other useful products, like ethylene, ethane, propane, and ethanol, were detected. Experiment and numerical simulations show that the formation of H ₂ O and CO has a strong negative influence on methanol formation.     

Effect of Dimethyl Ether Co-feed on Catalytic Performance of Methane Dehydroaromatization over Mo／HZSM-5 Catalyst

The effect of dimethyl ether (DME) co-feed on the catalytic performance of methane dehydroaxomatization (MDA) over 6Mo/HZSM-5 catalyst was investigated as a function of DME concentration under reaction conditions of T=1023 K, p=101 kPa and SV=1500 ml/(g.h). A high benzene yield wasobtained and the stability of the catalyst was improved by adding 1.5%DME to the CH4 feed. The C6H6 yield was as high as ca. 10% even after reaction for 6 h. The stability of the catalyst was further improved when DME concentration in the co-feed gas was increased to an appropriate value. TGA and TPO results of the used 6Mo/HZSM-5 catalyst showed that the amount of coke on the used catalyst was reduced and the chemical nature of the coke was changed. When 1.5%DME was added to the CH4 feed, the coke formed on the catalyst could be burned off more easily than that when only CH4 was used as reactant. It is supposed that the oxygen in DME may play a role in preventing the coke burnt off at lower temperature from transforming into the coke burnt off at higher temperature, which results in the improvement of the stability of the catalyst.     

Oxidative coupling of methane over （Na2WO4＋Mn or Ce）/SiO2 catalysts： In situ measurement of electrical conductivity

The effects of manganese oxide or ceria promoters on the performance of Na2WO4/SiO2 catalysts for oxidative coupling of methane (OCM) are reported. The OCM reaction was performed in a continuous-flow microreactor at 800 ℃, atmospheric pressure and under GHSV = 13200 ml gC-1at h-1. Catalysts were characterized by in situ conductivity measurement, FT-IR spectroscopy, XRD, SEM and temperature programmed reduction analysis. Manganese oxide promoted Na2WO4/SiO2 is considered as one of the active and selective ca...     

Synthesis of an anthracene-based bis(pyrazolyl)methane ligand and the structural characterization of its dinuclear tricarbonylrhenium(I) complex

The new anthracene-based, bitopic bis(pyrazolyl)methane ligand 1,8-bis(4-[bis(1-pyrazolyl)methyl]phenyl)anthracene (1,8-[4-CH(pz)₂C₆H₄]₂C₁₄H₈) has been prepared by the cobalt-catalyzed reaction between thionyldipyrazole and 1,8-bis(4-formylphenyl)anthracene. The reaction between 1,8-[4-CH(pz)₂C₆H₄]₂C₁₄H₈ and Re(CO)₅Br yielded the dirhenium complex {μ-1,8-[4-CH(pz)₂C₆H₄]₂C₁₄H₈}[Re(CO)₃Br]₂. The solid state structure of this complex displays extensive noncovalent interactions, particularly CH-π and π-π interactions.