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Mn-based binary oxides as catalysts for the conversion of methane to C-2 hydrocarbons with carbon dioxide as oxidant

机译:锰基二元氧化物作为催化剂,以二氧化碳为氧化剂将甲烷转化为C-2烃

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摘要

Binary oxides, mainly Ca-Mn, Sr-Mn and Ba-Mn, have been studied as catalysts for the coupling of CH4 to C-2 hydrocarbons (C2H6 and C2H4) using CO2 as oxidant. At temperatures of greater than or equal to 840 degreesC, the Ca-Mn catalyst exhibits quite similar performances to those of other Ca-containing binary oxide catalysts (Ca-Ce, Ca-Cr and Ca-Zn) reported previously; C-2 selectivity and yield at 850 degreesC increase remarkably with increasing partial pressure of CO2, and apparent activation energies observed over these catalysts are roughly the same (190-220 kJ mol(-1)). When the temperature is decreased from 840 to 825 degreesC, CH4 conversion and C-2 selectivity over the Ca-Mn catalyst abruptly drop; here a discontinuous change also is seen in the Arrhenius plots. On the other hand, the Sr-Mn and Ba-Mn catalysts show different kinetic features from the Ca-Mn system; C-2 selectivity at 850 degreesC changes only slightly with partial pressure of CO2, and the activation energies are constant over the whole temperature range examined and notably lower. Characterizations reveal that solid solution of Ca0.48Mn0.52O is the main phase for the Ca-Mn catalyst after reaction at 850 degreesC, while, at 800 degreesC, some Ca2+ ions separate from the solid solution to form CaCO3, which covers the catalyst surface. Such a difference probably accounts for the discontinuous change in the catalytic behavior with temperature. With the Sr-Mn and Ba-Mn catalysts, SrCO3 and BaCO3 are formed along with MnO after reaction, and the carbonates are suggested to react with MnO to form SrMnO2.5 and BaMnO2.5 in the conversion process of CH4 with CO2. The mechanism for C-2 formation involving SrMnO2.5 and BaMnO2.5 as intermediates is discussed. (C) 2001 Elsevier Science B.V. All rights reserved.
机译:已经研究了二元氧化物,主要是Ca-Mn,Sr-Mn和Ba-Mn,作为使用CO2作为氧化剂将CH4与C-2碳氢化合物(C2H6和C2H4)偶联的催化剂。在高于或等于840摄氏度的温度下,Ca-Mn催化剂表现出与先前报道的其他含Ca的二元氧化物催化剂(Ca-Ce,Ca-Cr和Ca-Zn)非常相似的性能。 C-2的选择性和850℃下的产率随CO2分压的增加而显着增加,并且在这些催化剂上观察到的表观活化能大致相同(190-220 kJ mol(-1))。当温度从840℃降低到825℃时,在Ca-Mn催化剂上的CH 4转化率和C-2选择性急剧下降。在Arrhenius图中也可以看到不连续的变化。另一方面,Sr-Mn和Ba-Mn催化剂表现出与Ca-Mn体系不同的动力学特征。 850℃下的C-2选择性仅随CO2的分压而略有变化,并且活化能在所考察的整个温度范围内是恒定的,并且明显较低。表征表明,Ca0.48Mn0.52O的固溶体是Ca-Mn催化剂在850℃反应后的主要相,而在800℃时,一些Ca2 +离子会从固溶体中分离形成CaCO3,覆盖催化剂表面。 。这种差异可能解释了催化行为随温度的不连续变化。使用Sr-Mn和Ba-Mn催化剂,反应后会与MnO一起形成SrCO3和BaCO3,并建议碳酸盐在与CH2转化为CO2的过程中与MnO反应生成SrMnO2.5和BaMnO2.5。讨论了以SrMnO2.5和BaMnO2.5为中间体的C-2形成机理。 (C)2001 Elsevier Science B.V.保留所有权利。

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    WANG Y; OHTSUKA Y; 王野;

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