首页> 外文期刊>American Chemical Society, Division of Fuel Chemistry, Preprints >FISCHER-TROPSCH SYNTHESIS: EFFECT OF CO CONVERSION ON PRODUCT SELECTIVITIES DURING DEACTIVATION BY OXIDATION OR BY CHANGING SPACE VELOCITY AT STABLE CONDITIONS OVER UNPROMOTED AND RU PROMOTED 25%Co/Al_2O_3 CATALYSTS
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FISCHER-TROPSCH SYNTHESIS: EFFECT OF CO CONVERSION ON PRODUCT SELECTIVITIES DURING DEACTIVATION BY OXIDATION OR BY CHANGING SPACE VELOCITY AT STABLE CONDITIONS OVER UNPROMOTED AND RU PROMOTED 25%Co/Al_2O_3 CATALYSTS

机译:FISCHER-TROPSCH合成:在未经促进和经RU促进的25%Co / Al_2O_3催化剂上,在稳定条件下通过氧化或改变空间速度在钝化过程中,CO转化对产物选择性的影响

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摘要

The effects of CO conversion on hydrocarbon and CO_2rnselectivities were studied under both deactivation and periods ofrnstability but with changes in contact time. Essentially identical trendsrnin changes of selectivities to CH4 (negative), C5+ (positive), 1-olefinrn(negative) and 2-olefin (positive) with CO conversion were observedrnregardless of whether a decrease in CO conversion was caused byrncatalyst deactivation or by an increase in gas space vel℃ity (stablernconditions). However, selectivities to CO_2, total paraffins and totalrnolefins in the C_2-C_4 and C_5-C_(10) ranges did not change significantlyrnduring the marked deactivation from 320 h (XCO: 40-20%) for a cobaltrncatalyst, whereas different trends were observed under stablernconditions with changing contact time, (i.e., CO_2 selectivity and totalrnparaffin content increased almost linearly and total olefin contentrndecreased almost linearly with increasing CO conversion).rnDifferent mechanisms were responsible for the observedrnrelationships between CO conversion and various selectivities underrndeactivating and stable conditions. The formation of cobalt oxidernspecies during catalyst deactivation enhanced methanation and WGSrnreaction pathways, as well as the hydrogenation reaction of olefins orrnC_nH_(2n+1)-S species to paraffins. It is proposed that cobalt oxide speciesrnplay a role in enhancing methanation, perhaps by enhancing the l℃alrncoverage of hydrogen on the catalyst surface by promoting the WGSrnreaction. Therefore, changes in the product selectivities with COrnconversion on the cobalt catalyst under deactivating conditions was arncombination of the effect of contact time and changes in cobaltrnstructure, but the latter factor became dominant in the later portion ofrndeactivation in the long kinetic test run. In contrast, the intrinsicrnrelationship between CO conversion and various selectivities of the Corncatalyst obtained under stable conditions with changing contact timernmainly resulted from the changes in partial pressures of reactantsrnand/or products with changes in contact time.rnUnder natural deactivation conditions, isomerization of 1-olefinsrnwas not observed to be enhanced on cobalt oxidized species; thus thernisomerization of 1-olefins to internal olefins was mainly governed byrnpartial pressure of CO.
机译:研究了在失活和失稳期下,但随着接触时间的变化,CO转化率对烃和CO_2rn选择性的影响。观察到随着CO转化率对CH4(负),C5 +(正),1-烯烃(负)和2-烯烃(正)的选择性变化具有基本相同的趋势-无论CO转化率下降是由催化剂失活还是由于催化剂失活引起的在气体空间速度(稳定条件)下。但是,对于钴催化剂,从320 h开始显着失活(XCO:40-20%)期间,C_2-C_4和C_5-C_(10)范围内的CO_2,总链烷烃和总烯烃的选择性没有显着变化。在接触时间变化的稳定条件下(即CO_2选择性和总烷烃含量几乎呈线性增加,而总烯烃含量随CO转化率几乎呈线性降低)。在失活和稳定条件下,观察到的CO转化率与各种选择性之间的关系是由不同的机理引起的。催化剂失活过程中氧化钴物种的形成增强了甲烷化和WGSrn反应路径,以及烯烃orrnC_nH_(2n + 1)-S物种向链烷烃的氢化反应。有人提出,氧化钴可能起甲烷化作用,可能是通过促进WGS反应提高催化剂表面氢的lAl覆盖率。因此,在失活条件下,钴催化剂上随COrn转化的产物选择性的变化是接触时间和钴结构变化的综合结果,但在长的动力学试验过程中,后者在失活的后期占主导地位。相比之下,在稳定条件下随着接触时间的变化而获得的玉米催化剂的CO转化率与各种选择性之间的内在联系主要是由于反应物和/或产物的分压随接触时间的变化而引起的。在自然失活条件下,1-烯烃的异构化未观察到钴氧化物种的增强;因此1-烯烃向内烯烃的热异构化主要由CO的分压控制。

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    Center for Applied Energy Research, University of Kentucky, 2540 Research Park Drive, Lexington, Kentucky 40511, USA;

    Center for Applied Energy Research, University of Kentucky, 2540 Research Park Drive, Lexington, Kentucky 40511, USA;

    Center for Applied Energy Research, University of Kentucky, 2540 Research Park Drive, Lexington, Kentucky 40511, USA;

    Chemical Engineering Program, Texas A&M University at Qatar, PO Box 23874, Doha, Qatar;

    Chemical Engineering Program, Texas A&M University at Qatar, PO Box 23874, Doha, Qatar;

    Center for Applied Energy Research, University of Kentucky, 2540 Research Park Drive, Lexington, Kentucky 40511, USA;

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