微波场对固态氧离子导体上的甲烷氧化偶联的影响

研究了微波场下甲烷在具有δ－Ｂｉ２Ｏ３结构的固态氧离子导体上氧化偶联反应行为。与常规加热条件下的反应结果相比较，微波辐射下的反应有上特点：（１）在达到相同甲烷转化率时，微波辐照下所需床层温度要远低于常规加热条件下所需床层温度；（２）微波辐照下，甲烷氧化偶联产物中Ｃ２烃的选择性普遍较高，在低温区尤为突出。微波场下甲烷偶联产物乙烷、乙烯的再氧化得到一定程度的抑制，致使微波场下的甲烷氧化偶联反应通常有较     

甲烷氧化偶联CaF2／Sm2O3催化剂的研究

甲烷氧化偶联ＣａＦ_２／Ｓｍ_２Ｏ_３催化剂的研究周水琴，龙瑞强，黄亚萍，万惠霖，蔡启瑞（厦门大学化学系，固体表面物理化学国家重点实验室，厦门，３６１００５）关键词甲烷氧化偶联，氟化钙，三氧化二钐，离子交换，氧物种甲烷氧化偶联制乙烯是催化领域中最活跃的?..     

甲烷氧化偶联催化反应的特征

应用程序升温反应（ＴＰＲ）及质谱分析表征了ＣａＯ，Ｓｍ２Ｏ３，０．５－１０％Ｓｍ／ＣａＯ催化剂上的甲烷氧化偶联反应特性。谱图分析表明，在４００－１０００℃范围内，甲烷氧化偶联反应产物的变化呈现三个反应温度区域：（１）完全氧化区，反应主要为ＣＨ３·在催化剂表面完全氧化形成ＣＯｘ和Ｈ２：（２）偶联区，主要为ＣＨ３·的氧化和偶联竞争反应，Ｈ２谱线出现明显的低温峰；（３）氧耗尽区，反应为高温气相反应，产物     

微波场对固态氧离子导体上的甲烷氧化偶朕的影响

研究了微波场下甲烷在具有Bi2O3结构的固态氧离子导体上氧化偶联反应行为．与常规加热条件下的反应结果相比较,微波辐照下的反应有如下特点;（1）在达到相同甲烷转化率时,微波辐照下所需床层温度要远低于常规加热条件下所需床层温度;（2）微波辐照下,甲烷氧化偶联产物中C2烃的选择性普遍较高,在低温区尤为突出．微波场下甲烷偶联产物乙烷、乙烯的再氧化得到一定程度的抑制,致使微波场下的甲烷氧化偶联反应通常有较低的烯／烷比．     

氟化锶／氧化钕催化剂的甲烷氧化偶联性能及其吸附氧物种的原位FTIR光谱研究

氟化锶／氧化钕催化剂的甲烷氧化偶联性能及其吸附氧物种的原位ＦＴＩＲ光谱研究龙瑞强，万惠霖，赖华龙，蔡启瑞（厦门大学化学系固体表面物理化学国家重点实验室，厦门，３６１００５）关键词甲烷氧化偶联，氟化锶／氧化钕，吸附氧物种近年来，甲烷氧化偶联（ＯＣＭ）的...     

在Li2O／MgO上以脉冲法研究甲烷氧化偶联

在Ｌｉ_２Ｏ／ＭｇＯ上以脉冲法研究甲烷氧化偶联戚蕴石，卫上方（华东理工大学工业催化研究所，上海，２００２３７）关键词甲烷氧化偶联，晶格氧，脉冲法对甲烷氧化偶联（ＯＣＭ）的研究已有较多报道［１～４］，对其反应机理的研究亦取得了较大的进展．Ｏｔｓｕｋａ［?..     

电场增强催化天然气合成碳二烃

电场增强催化天然气合成碳二烃许根慧孙洪伟何菲杜丽苹（天津大学Ｃ１化工国家重点实验室３０００７２）天然气是储量丰富和廉价的资源，利用天然气取代石油原料将其合理地转化成有价值的碳二烃（乙烯，乙烷等）是目前Ｃ１化工重要的研究课题。多年来国内外对甲烷氧化偶联...     

激光促进甲烷氧化偶联表面反应规律的研究

采用ＩＲ、ＴＰＤ、选频ＴＥＡＣＯ２激光等技术，考察了单组分及多组分表面材料上激光促进的甲烷氧化偶联反应．在实验条件下，甲烷在ＬｉＣｌＯ４／Ｐｂ３（ＰＯ４）２固体表面上的转化率达到３２％以上，生成乙烯的选择性为９３％．结果分析表明，晶格氧参与了反应，激光频率是影响激光能量利用的主要因素．     

非平衡等离子体条件下甲烷脱氢偶联反应

非平衡等离子体条件下甲烷脱氢偶联反应刘万楹，雷正兰（中国科学院成都有机化学研究所天然气化学开放实验室，６１００４１）甲烷直接转化是天然气化学研究和天然气化学利用的重要课题。甲烷偶联形成Ｃ２烃具有重要的学术和经济意义。甲烷氧化偶联研究已取得了一些有意义...     

担载型过渡金属催化剂上CH4＋C2H4→C3H8反应的初步研究

担载型过渡金属催化剂上ＣＨ４＋Ｃ２Ｈ４→Ｃ３Ｈ８反应的初步研究阎子峰薛锦珍沈师孔①王弘立（中国科学院兰州化学物理研究所羰基合成与选择氧化国家重点实验室，兰州７３００００）关键词甲烷同系化过渡金属催化剂乙烯１前言在均相催化体系中，甲烷与其它饱和烃类的反...     

Oxidative Conversion of Methane/Natural Gas into Higher Hydrocarbons

Oxidative coupling of methane (OCM) to ethylene and ethane is a futuristic process of great practical importance for the effective utilization of methane/natural gas. A brief summary of the work carried out at National Chemical Laboratory (Pune) for the development of catalyst and catalytic process for OCM, particularly addressing the major issues/limitations of the OCM process and efforts made to overcome the problems is presented. This review particularly covers the development of a number of highly active/selective and stable unsupported and supported (using commercial catalyst carriers) catalysts for the OCM process and also the process of improvements/modifications to overcome most of the limitations of OCM.     

Pulse reactions of methane, ethane and ethylene over Li-, La- and Sm-promoted MgO catalysts in the presence and absence of free oxygen

Pulse reaction of methane in the presence and absence of free (or gaseous) oxygen and that of ethane and ethylene in the absence of free oxygen over Li−MgO, La−MgO and Sm−MgO (Li or La or Sm/Mg ratio=0.1) have been investigated for elucidating the role of lattice and free oxygen in oxidative coupling of methane (OCM) over these catalysts. No significant role is played by the lattice oxygen from these catalysts in the OCM process. The presence of free oxygen is essential for all these catalysts to be active and selective in OCM process. However, lattice oxygen plays some role in ethane conversion but a very significant role in ethylene conversion over these catalysts.     

氧载体的氧物种直接氧化甲烷制合成气

甲烷部分氧化制合成气由于合成气中n(H2)/n(CO)接近2,可直接用于甲醇合成或烃类F-T合成等后续工业过程而在国内外受到了广泛的关注。利用氧载体的氧物种在无气相氧下直接选择氧化甲烷制合成气是天然气化工利用的新方法,本文介绍了该方法的基本原理、概念工艺和对氧载体的性能要求,对应用于该方法的铈基复合氧化物的掺杂和助剂对选择氧化甲烷性能的影响、钙钛矿氧化物氧载体的氧缺陷、氧物种迁移、结构稳定性及其氧物种氧化甲烷的性能进行了阐述和分析,提出了控制氧载体表面状态是获得高合成气选择性的关键,并对该技术今后的研究重点进行了展望。     

Conversion of Methane and Carbon Dioxide in a DBD Reactor: Influence of Oxygen

A continuous plug flow reactor supported by a dielectric barrier discharge (DBD) is used to study the conversion of methane, carbon dioxide, and oxygen at different compositions. The three studied gases were diluted with helium to 3 % with an overall flow rate of 200 sccm. The 13.56 MHz plasma was ignited at atmospheric pressure. The product stream and the inlet flow were analyzed by a FTIR spectrometer equipped with a White-cell and by a quadrupole mass spectrometer. The DBD reactor generates hydrogen, carbon monoxide, ethane, ethene, acetylene, formaldehyde, and methanol. Additional oxygen in the feed has positive effects on the yield of methanol, formaldehyde and carbon monoxide and reduces the total consumed energy. The hydrogen yield reaches its maximum at medium amounts of oxygen in the inlet flow. The conversion of methane increases to a limiting value of about 35 %. Methane rich feeds increase the yield of hydrogen, ethane and methanol. On the other hand, additional oxygen has a negative influence on the produced amount of C2 hydrocarbons. The conversion of methane and carbon dioxide as well as the yield of synthesis gas components and C2 hydrocarbons increases by changing the plasma power to higher values.     

气相色谱法测定乙二醇生产中无机气体成分

煤制乙二醇工艺过程中,需要测定生产过程中的无机气体成分,对工艺生产作出指导.采用气相色谱法,通过一个十通阀和一个六通阀,HN填充柱与毛细管色谱柱HP-MOLESIEVE组合,经过多次实验探究优化,最终确立了高纯氩气为载气,配备恒温外置小柱箱,柱箱采用程序升温,最优的切换十通阀、六通阀时间,实现了一次性测定样品气中二氧化...     

Modeling the oxidative coupling of methane： Heterogeneous chemistry coupled with 3D flow field simulation

The oxidative coupling of methane (OCM) over titanate perovskite catalyst has been developed by three-dimensional numerical simulations of flow field coupled with heat transfer as well as heterogeneous kinetic model. The reaction was assumed to take place both in the gas phase and on the catalytic surface. Kinetic rate constants were experimentally obtained using a ten step kinetic model. The simulation results agree quite well with the data of OCM experiments, which were used to investigate the effect of temperature on the selectivity and conversion obtained in the methane oxidative coupling process. The conversion of methane linearly increased with temperature and the selectivity of C2 was practically constant in the temperature range of 973–1073 K. The study shows that CFD tools make it possible to implement the heterogeneous kinetic model even for high exothermic reaction such as OCM.     

混合导体透氧膜反应器中甲烷部分氧化反应的催化行为(英文)

应用组成为Ba0.5Sr0.5Co0.8Fe0.2O3-(的钙钛矿型混合导体陶瓷膜制成膜反应器。该膜在进行氧分离的同时具有活化甲烷氧化偶联的催化功能。随着温度升高和膜的富氧端氧分压的增大,透氧量有所增加。在空气、氦气的氧分压梯度下,850(C,膜厚度为1.5 mm时,JO2可达到1.2 mL/(cm3(min)。同时在800(C~900(C温度范围内,该膜对于甲烷转化为乙烷和乙烯一般只具有0.5%~3.5%的低转化率,而选择性可达40%~70%。在反应尾气中发现了大量的未反应的分子氧,说明过量的氧与甲烷未经催化反应的气相反应导致了C2的选择性相对较低。OCM膜反应模式情况下的透氧量与空气、氦气梯度情况下的透氧量相比只有微小增加,这与POM膜反应模式情况下透氧量大量增加显著不同。     

电场增强等离子催化反应由天然气合成碳二烃

本研究借助电场作用通过交流或直流等离子催化反应在常压、低下将天然气（甲烷）直接转一烃。甲烷被等离子场激活后直接和催化剂活性位作用生成乙烷、乙烯等碳二烃，由气相色谱在线分析其组成。考察了反应条件和催化剂的影响。得到了本实验较适宜反应条件下的碳二烃选择性在９０％以上的结果。     

FORCED PERIODIC OSCILLATORY OPERATION FOR OXIDATIVE COUPLING OF METHANE ON Fe-P-O CATALYST

IntroductionAsearlyasthemiddleofl960s,manychemistsandchemicalengineerstookmuchinterestinthedynamicoperationpropertiesofreactor.TheoPinionthattheoutputofreaCtrcouldbeimprovedbyoscillatoryfeedingoPerationwasprop0sedinthcory'.ThesclfxiscillationphenomenaobservedexPerimentall}'inmanychcmicalandcatalyticreactionshavstronglysupPOrtedthisoPinion.Inreeentyears,thestudics0ntheforcedperiodicoscillationhaveattraCtedgreaattenioninheterogencousodlyticproccsses,includingS02oxidaionIll,C0oxidaionl2'3l,a…