Abstract
Biomass such as wood waste, sawdust and agriculture waste can be easily acquired in all parts of the country and may be a most promising renewable resource to make synthetic fuel. In order to convert biomass into liquid fuel, syngas emitted from a circulating fluidized bed gasifier must be cleaned by removing acid gas, such as H2S, COS, and CO2, before going to a F-T(Fischer-Tropsch) process. 0.1Nm3/hr methanol absorption tower were used for simultaneously removing H2S, COS, and CO2 from simulated syngas. The pressure of absorption tower was 0-100psia and the temperature was from 0oC to -25oC. Each concentrations of H2S, COS, and CO2, in a biomass gasifier were 45ppmv, 5ppmv, 18vol%, respectively. In these experiments, H2S, and COS adsorption ratio was up to 99.5%, and CO2 adsorption ratio was 38% to 51% at various operation conditions.
| Original language | English |
|---|---|
| Journal | ACS National Meeting Book of Abstracts |
| State | Published - 2011 |
| Event | 241st ACS National Meeting and Exposition - Anaheim, CA, United States Duration: 2011.03.27 → 2011.03.31 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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