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Cobalt‐Iron‐Manganese Catalysts for the Conversion of End‐of‐Life‐Tire‐Derived Syngas into Light Terminal Olefins

机译:钴铁锰催化剂用于将报废轮胎合成气转化为轻质烯烃

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摘要

Co‐Fe‐Mn/γ‐Al2O3 Fischer–Tropsch synthesis (FTS) catalysts were synthesized, characterized and tested for CO hydrogenation, mimicking end‐of‐life‐tire (ELT)‐derived syngas. It was found that an increase of C2‐C4 olefin selectivities to 49 % could be reached for 5 wt % Co, 5 wt % Fe, 2.5 wt % Mn/γ‐Al2O3 with Na at ambient pressure. Furthermore, by using a 5 wt % Co, 5 wt % Fe, 2.5 wt % Mn, 1.2 wt % Na, 0.03 wt % S/γ‐Al2O3 catalyst the selectivity towards the fractions of C5+ and CH4 could be reduced, whereas the selectivity towards the fraction of C4 olefins could be improved to 12.6 % at 10 bar. Moreover, the Na/S ratio influences the ratio of terminal to internal olefins observed as products, that is, a high Na loading prevents the isomerization of primary olefins, which is unwanted if 1,3‐butadiene is the target product. Thus, by fine‐tuning the addition of promoter elements the volume of waste streams that need to be recycled, treated or upgraded during ELT syngas processing could be reduced. The most promising catalyst (5 wt % Co, 5 wt % Fe, 2.5 wt % Mn, 1.2 wt % Na, 0.03 wt % S/γ‐Al2O3) has been investigated using operando transmission X‐ray microscopy (TXM) and X‐ray diffraction (XRD). It was found that a cobalt‐iron alloy was formed, whereas manganese remained in its oxidic phase.
机译:Co-Fe-Mn /γ-Al2O3费-托合成(FTS)催化剂经过合成,表征和测试以进行CO加氢,模拟了寿命终止(ELT)衍生的合成气。结果发现,在环境压力下,Na含量为5%(重量)的Co,5%(重量)的Fe,2.5%(重量)的Mn /γ-Al2O3可使C2-C4烯烃的选择性提高到49%。此外,通过使用5wt%的Co,5wt%的Fe,2.5wt%的Mn,1.2wt%的Na,0.03wt%的S /γ-Al2O3催化剂,可以降低对C5 +和CH4馏分的选择性,而选择性在10 bar下,C4烯烃的比例可以提高到12.6%。此外,Na / S比会影响产物中所观察到的末端烯烃与内部烯烃的比率,也就是说,高的Na含量会阻止伯烯烃的异构化,如果目标产物1,3-丁二烯是不希望的。因此,通过微调促进剂元素的添加,可以减少ELT合成气处理期间需要回收,处理或升级的废物流的量。使用操作透射X射线显微镜(TXM)和X-X研究了最有希望的催化剂(5 wt %% Co,5 wt %% Fe,2.5 wt%Mn,1.2 wt%Na,0.03 wt%S /γ-Al2O3)。射线衍射(XRD)。发现形成了钴铁合金,而锰保留在其氧化相中。

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