2018
DOI: 10.1002/ange.201801397
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Shape‐Selective Zeolites Promote Ethylene Formation from Syngas via a Ketene Intermediate

Abstract: Syngas conversion by Fischer-Tropsch synthesis (FTS) is characterized by aw ide distribution of hydrocarbon products ranging from one to af ew carbon atoms.R eported here is that the product selectivity is effectively steered toward ethylene by employing the oxide-zeolite (OX-ZEO) catalyst concept with ZnCrO x -mordenite (MOR). The selectivity of ethylene alone reaches as high as 73 %a mong other hydrocarbons at a2 6% CO conversion. This selectivity is significantly higher than those obtained in any other dire… Show more

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Cited by 38 publications
(15 citation statements)
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“…It is more attractive that the CO 2 selectivity is less than 2% throughout the whole process, and the byproducts are mainly ethylene and CO, which are both valuable feedstocks for a vast array of chemicals. 51,52 Weight hourly space velocity (WHSV) affects the propane conversion and propylene selectivity as well (Figure S17a), and the reaction order of reaction gas (2.23 for propane and 0.77 for O 2 , Figure S17b) is in good agreement with the previous reports. 16,18 The long-term stability of SS-BNNSs for ODHP was conducted at 490 °C for 100 h (Figure 5c).…”
Section: ■ Results and Discussionsupporting
confidence: 89%
“…It is more attractive that the CO 2 selectivity is less than 2% throughout the whole process, and the byproducts are mainly ethylene and CO, which are both valuable feedstocks for a vast array of chemicals. 51,52 Weight hourly space velocity (WHSV) affects the propane conversion and propylene selectivity as well (Figure S17a), and the reaction order of reaction gas (2.23 for propane and 0.77 for O 2 , Figure S17b) is in good agreement with the previous reports. 16,18 The long-term stability of SS-BNNSs for ODHP was conducted at 490 °C for 100 h (Figure 5c).…”
Section: ■ Results and Discussionsupporting
confidence: 89%
“…13 , we believe that CO 2 hydrogenation cannot proceed over H-ZSM-5. Some evidences were put forward by Jiao et al 14 , 17 , 20 to support the ketene intermediate mechanism for STO or STA reactions over oxides/zeolites composite catalysts, however, we consider that this mechanism does not work in CO 2 hydrogenation over ZnAlO x &H-ZSM-5 due to very low concentration of CO in the reaction process.
Fig.
…”
Section: Resultsmentioning
confidence: 64%
“…骤组成了复杂的反应网络 [41] . 通过反应耦合催化新 技术, 包信和课题组 [26,28] 、王野课题组 [27,29] 相继发展 了 一 系 列 突 破 ASF 规 则 限 制 的 策 略 . 此 外 , 基 于 C-C/C-O键选择活化的生物质水相重整制烃类燃料 过程 [42] , 复杂反应网络基元反应步骤的耦合控制也 [37] Figure 8 (Color online) The olefin-based methanol-to-olefin reaction network [37] 表观反应结果, 烃分子与分子筛催化材料的孔道尺 Hydrocarbon is a vital kind of chemical compounds to form liquid fuels and polymer monomers.…”
Section: 在合成气转化反应中 链增长、链终止等基元步unclassified