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Articles

Experimental investigation of synthetic gas composition in a two-stage fluidized bed gasification process: effect of activated carbon as bed material

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Pages 1169-1175 | Received 06 Mar 2016, Accepted 30 Jul 2016, Published online: 19 Aug 2016
 

ABSTRACT

In this study, a two-stage fluidized bed gasifier was used to investigate the effect of the equivalence ratio (ER) and steam/biomass ratio (S/B) on the synthetic gas distribution while activated carbon (AC) was added as the bed material in secondary gasifier (Stage II). The experimental results showed that when the empty bed (without the bed material) was used for the Stage II reaction, the hydrogen (H2) content in the synthetic gas emitted from the Stage II reactor was 2–3 mol% higher than that from the first-stage gasifier (Stage I). It was supposed that using the Stage II reactor prolongs the reaction time and thereby increases the H2 production. Besides, when the AC was added in the Stage II gasifier, the H2 concentration, the total gas yield, and gas heating value reached their maximum (30 mol%) when ER and S/B were 0.3 and 1.5, respectively.

Disclosure statement

No potential conflict of interest was reported by the authors.

Additional information

Funding

Supported by Science and Technology Planning Project of Guangdong Province, China (2014A050503063, 2016A050502059), Guangzhou Special Fund for the Industry-University-Research Institute Collaborative Innovation (2016201604030058).

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