Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value
Catalysis, Kinetics and Reaction Engineering|Updated:2026-01-06
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Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value
Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value
中国化学工程学报(英文版)2018年26卷第4期 页码:747-752
Affiliations:
Key Lab for Green Chemical Technology of Ministry of Education, School of Chemical Engineering and Technology, Tianjin University,Tianjin,China,300072
Author bio:
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DOI:
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纸质出版:2018
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Zhenhua Li, Mengyao Si, Li Xin, 等. Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value[J]. 中国化学工程学报(英文版), 2018,26(4):747-752.
Zhenhua Li, Mengyao Si, Li Xin, Renjie Liu, Runxue Liu, Jing Lü. Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value[J]. Chin.J.Chem.Eng., 2018, 26(4): 747-752.
Zhenhua Li, Mengyao Si, Li Xin, 等. Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value[J]. 中国化学工程学报(英文版), 2018,26(4):747-752.DOI:
Zhenhua Li, Mengyao Si, Li Xin, Renjie Liu, Runxue Liu, Jing Lü. Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value[J]. Chin.J.Chem.Eng., 2018, 26(4): 747-752.DOI:
Cobalt catalysts for Fischer-Tropsch synthesis: The effect of support, precipitant and pH value
摘要
Abstract
In this report
Co-based catalysts supported on ZnO
Al
2
O
3
and ZrO
2
as well as the ZrO
2
derived from different precipitants and different pH values were prepared by co-precipitation method. Their catalytic Fischer-Tropsch synthesis (FTS) performance was investigated in a fixed-bed reactor. The results revealed that Co catalyst supported on ZrO
2
exhibited better FTS catalytic performance than that supported on ZnO or Al
2
O
3
. For the Co/ZrO
2
catalyst
different precipitants showed the following an activity order of NaOH Na
2
CO
3
NH
4
OH
and the best pH value is 13. The catalysts were characterized by N
2
adsorption-desorption
XRF
XRD
H
2
-TPR
H
2
-TPD and TEM. It was found that the main factor affecting the CO conversion of the catalyst was the amounts of low-temperature active adsorption sites. Moreover
the selectivity of C
5
+
hydrocarbons had a positive relationship with the peak temperature of the weak hydrogen adsorption sites. The higher the peak temperature
the higher the C
5
+
sel
ectivity is.
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相关作者
Li Jingrui
Xi Shuangli
Ma Youcai
Li Xiaoting
Hu Erfeng
Wang Jianshan
Li Ming
Zhang Heng
相关机构
State Key Laboratory of Vanadium and Titanium Resources Comprehensive Utilization
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State Key Laboratory of Clean and Efficient Coal Utilization, Taiyuan University of Technology