Co/CNT和Co/γ-Al2O3纳米催化剂在费托合成中的失活行为比较

Ahmad Tavasoli, Saba Karimi, Somayeh Taghavi, Zahra Zolfaghari, Hamideh Amirfirouzkouhi
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引用次数: 24

摘要

本文报道了在γ-氧化铝和碳纳米管催化剂上负载钴纳米粒子进行费托合成的广泛研究。20%的钴通过浸渍法加载在支架上。采用固定床微反应器,在220℃、2 MPa、2.7 L/h进料流量条件下对两种催化剂进行了失活研究。对煅烧后的新鲜催化剂和使用过的催化剂进行了广泛的表征,并确定了催化剂失活的不同来源。xCoO·yAl2O3形式的钴载体混合氧化物的形成和钴铝酸盐的形成是Co/γ-Al2O3催化剂失活的主要来源。而钴纳米颗粒的烧结和团簇生长是Co/CNTs催化剂失活的主要原因。对于CO/γ-Al2O3催化剂,在连续FT合成720 h后,钴纳米颗粒的平均直径从15.9 nm增加到18.4 nm,而在相同的反应条件下,CO/ CNTs的钴纳米颗粒的平均直径从11.2 nm增加到17.8 nm。虽然Co/CNTs的初始FT活性比Co/ γ-Al2O3高26%,但经过720 h后,Co/CNTs上的FT活性下降了49%,Co/ γ-Al2O3上的FT活性下降了32%。CO/γ-Al2O3催化剂的总活性损失为6.7%,CO/ CNTs催化剂的总活性损失为11.6%,在相同的第一步再生条件下,催化剂再生后不能恢复。综上所述,与γ-Al2O3载体相比,使用CNTs作为钴催化剂载体有利于碳的利用,但Co/CNTs催化剂更容易失活。
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Comparing the deactivation behaviour of Co/CNT and Co/γ-Al2O3 nano catalysts in Fischer-Tropsch synthesis

An extensive study of Fischer-Tropsch (FT) synthesis on cobalt nano particles supported on γ-alumina and carbon nanotubes (CNTs) catalysts is reported. 20 wt% of cobalt is loaded on the supports by impregnation method. The deactivation of the two catalysts was studied at 220°C, 2 MPa and 2.7 L/h feed flow rate using a fixed bed micro-reactor. The calcined fresh and used catalysts were characterized extensively and different sources of catalyst deactivation were identified. Formation of cobalt-support mixed oxides in the form of xCoO·yAl2O3 and cobalt aluminates formation were the main sources of the Co/γ-Al2O3 catalyst deactivation. However sintering and cluster growth of cobalt nano particles are the main sources of the Co/CNTs catalyst deactivation. In the case of the CO/γ-Al2O3 catalyst, after 720 h on stream of continuous FT synthesis the average cobalt nano particles diameter increased from 15.9 to 18.4 nm, whereas, under the same reaction conditions the average cobalt nano particles diameter of the Co/CNTs increased from 11.2 to 17.8 nm. Although, the initial FT activity of the Co/CNTs was 26% higher than that of the CO/γ-Al2O3, the FT activity over the Co/CNTs after 720 h on stream decreased by 49% and that over the CO/γ-Al2O3 by 32%. For the CO/γ-Al2O3 catalyst 6.7% of total activity loss and for the Co/CNTs catalyst 11.6% of total activity loss cannot be recovered after regeneration of the catalyst at the same conditions of the first regeneration step. It is concluded that using CNTs as cobalt catalyst support is beneficial in carbon utilization as compared to γ-Al2O3 support, but the Co/CNTs catalyst is more susceptible for deactivation.

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来源期刊
Journal of Natural Gas Chemistry
Journal of Natural Gas Chemistry 化学-工程:化工
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