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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

Postal Subscription Code 80-969

2018 Impact Factor: 2.809

Front Chem Eng Chin    2010, Vol. 4 Issue (4) : 441-444    https://doi.org/10.1007/s11705-010-0507-8
RESEARCH ARTICLE
Preparation and selection of Fe-Cu sorbent for COS removal in syngas
Bowu CHENG, Zhaofei CAO, Yong BAI, Dexiang ZHANG()
Department of Chemical Engineering for Energy Resources, East China University of Science and Technology, Shanghai 200237, China
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Abstract

A series of iron-based sorbents prepared with iron trioxide hydrate, cupric oxide by a novel method was studied in a fixed-bed reactor for COS removal from syngas at moderate temperature. In addition, the sorbents mixed with various additives in different ratios were tested. The effects of additive type and ratio on the breakthrough capacity and desulfurization performance, as well as the influence of operating conditions on sulfidation behavior of the sorbent, were investigated. The simulate gas contained 1% COS, 5% CO2, 20%–30% CO and 60%–70% H2. The outlet gases from the fixed-bed reactor were automatically analyzed by on-line mass spectrometry, and the COS concentration before breakthrough can be kept steady at 1 ppmv. The result shows that the breakthrough sulfur capacity of the sorbent is as high as 25 g-S/100 g. At 700 K and space velocity of 1000 h-1, the efficiency of sulfur removal and breakthrough sulfur capacity of the sorbent increase with the increase of copper oxide with an optimum value. The result shows that the species and content of additives also affect desulfurization performance of the sorbent.

Keywords sorbent      desulfurization      COS removal      syngas     
Corresponding Author(s): ZHANG Dexiang,Email:zdx@ecust.edu.cn   
Issue Date: 05 December 2010
 Cite this article:   
Bowu CHENG,Zhaofei CAO,Yong BAI, et al. Preparation and selection of Fe-Cu sorbent for COS removal in syngas[J]. Front Chem Eng Chin, 2010, 4(4): 441-444.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-010-0507-8
https://academic.hep.com.cn/fcse/EN/Y2010/V4/I4/441
Fig.1  Experimental apparatus sketch of removing COS
1 gas cylinder; 2 decompression valve; 3 gases control system; 4 main valve; 5 quartz-tube; 6 electrical heating furnace ; 7 mass spectrometry; 8 absorption liquid; 9 three way valve; 10 cooler; 11 temperature controller
Fig.2  Effects of CuO content on COS breakthrough curves
sorbentratio of Fe∶Cusulfur capacity /(g·100g-1)
FC1100 ∶ 516.3
FC2100 ∶ 1021.19
FC3100 ∶ 1524.08
FC4100 ∶ 2021.52
Tab.1  Effect of content of Cu on sorbent
sorbentadditives typesulfur capacity /(g·100g-1)
FC3A1kaoline24.23
FC3B1diatomite24.11
FC3C1bentonite24.13
Tab.2  Effect of species of additives on sorbent
sorbentsulfur capacity /(g·100g-1)
FC3A124.23
FC3A325.55
FC3A524.68
FC3A724.03
FC3A924.39
Tab.3  Effect of additive’s content on sulfur capacity
Fig.3  Effects of species of additives on COS breakthrough curves
Fig.4  Effect of additive’s content on COS breakthrough curves
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