Citation:
ZHOU Guang-lin, WANG Mei-qing, WANG Xiao-sheng, JIANG Wei-li, ZHOU Hong-jun. Removal of COS in coke-oven gas by NiO/ZnO-Al2O3 adsorption[J]. Journal of Fuel Chemistry and Technology,
;2015, 43(4): 470-475.
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The NiO/ZnO-Al2O3 adsorbent was prepared by incipient method and characterized by XRD and mercury porosimeter. The performance of the adsorbent in the removal of COS from the simulated coke-oven gas was tested in a fixed-bed reactor. The results show that the appropriate reaction conditions are 350 ℃, 0.40 MPa and GHSV of 500~1 000 h-1. The adsorbent could remove COS from 320~450 mg/m3 to 0.5 mg/m3 as well as olefins from 2.3%~4.5% to 0 without changing other component. The breadthrough sulfer capacity is 17.18%. The regeneration test shows that the crystal form, pore structure and sulfer capacity of the regenerated adsorbent have no significant change compared with the fresh adsorbent. A desulfurization mechanism is proposed as follows:first COS is absorbed on the reduced Ni atoms to form NiS via the breaking of the S-C bond, then NiS is transformed to H2S in the presence of H2, finally H2S is captured by ZnO.
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Keywords:
- coke-oven gas,
- adsorbent,
- COS,
- olefins,
- desulfurization
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