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Title: Experimental investigation of hardwood air gasification in a pilot scale bubbling fluidized bed reactor and CFD simulation of jet/grid and pressure conditions

Abstract

A pilot scale pressurized (50 psi) fluidized bed gasification was performed to investigate the effects of the jet/ grid air ratio (5:95–90:10) and equivalence ratio (ER = 0.23–0.45) on the gasification products such as syngas, tar, contaminant gas, and biochar. There was a noticeable effect of the jet/grid ratios on the syngas concentration. An increase in CO, CH4, and C2 gases was obtained at the condition closer to jet/grid = 50:50, whereas a higher jet/grid ratio favored water–gas shift reaction by increasing CO2 and H2 gases under the pressurized condition. The highest lower heating value (LHV) of 7.7 MJ/Nm3 was obtained at the lowest ER = 0.23. Both the jet/grid ratio and ER were important parameters in determining the H2 concentration. The cold gasification and carbon conversion efficiencies were obtained as high as 66% and 94%, respectively. Also, higher temperature and ER promoted a reduction in contaminant gases as well as tar yield. Tar product yield was also reduced significantly after a wet scrubber, and the tar consisted of chemicals of a carbon number less than 13 (≤C12). Here, the gasification biochar was also analyzed and showed an effective carbon sequestration property with a relatively higher surface area (105 m2/g).more » Furthermore, computational fluid dynamics simulation was performed to determine the effects of different jet/grid air ratio and pressure conditions on the hydrodynamics in the fluidized bed reactor.« less

Authors:
ORCiD logo [1];  [2]; ORCiD logo [3];  [3];  [3];  [3]
  1. Auburn University, AL (United States); Korea Institute of Energy Research (KIER), Daejeon (Korea)
  2. University of Guanajuato (Mexico)
  3. Auburn University, AL (United States)
Publication Date:
Research Org.:
Univ. of Tennessee, Knoxville, TN (United States)
Sponsoring Org.:
USDOE Office of Energy Efficiency and Renewable Energy (EERE); USDA
OSTI Identifier:
1781056
Alternate Identifier(s):
OSTI ID: 1691726
Grant/Contract Number:  
EE0006639; 2015-67021-22842; ALA014-6-17027
Resource Type:
Accepted Manuscript
Journal Name:
Energy Conversion and Management
Additional Journal Information:
Journal Volume: 168; Journal ID: ISSN 0196-8904
Publisher:
Elsevier
Country of Publication:
United States
Language:
English
Subject:
30 DIRECT ENERGY CONVERSION; pressurized gasification; pilot scale fluidized bed; jet/grid ratio; CFD hydrodynamic analysis; tar; contaminant gas

Citation Formats

Nam, Hyungseok, Rodriguez-Alejandro, David Aaron, Adhikari, Sushil, Brodbeck, Christian, Taylor, Steven, and Johnson, James. Experimental investigation of hardwood air gasification in a pilot scale bubbling fluidized bed reactor and CFD simulation of jet/grid and pressure conditions. United States: N. p., 2018. Web. doi:10.1016/j.enconman.2018.05.003.
Nam, Hyungseok, Rodriguez-Alejandro, David Aaron, Adhikari, Sushil, Brodbeck, Christian, Taylor, Steven, & Johnson, James. Experimental investigation of hardwood air gasification in a pilot scale bubbling fluidized bed reactor and CFD simulation of jet/grid and pressure conditions. United States. https://doi.org/10.1016/j.enconman.2018.05.003
Nam, Hyungseok, Rodriguez-Alejandro, David Aaron, Adhikari, Sushil, Brodbeck, Christian, Taylor, Steven, and Johnson, James. Fri . "Experimental investigation of hardwood air gasification in a pilot scale bubbling fluidized bed reactor and CFD simulation of jet/grid and pressure conditions". United States. https://doi.org/10.1016/j.enconman.2018.05.003. https://www.osti.gov/servlets/purl/1781056.
@article{osti_1781056,
title = {Experimental investigation of hardwood air gasification in a pilot scale bubbling fluidized bed reactor and CFD simulation of jet/grid and pressure conditions},
author = {Nam, Hyungseok and Rodriguez-Alejandro, David Aaron and Adhikari, Sushil and Brodbeck, Christian and Taylor, Steven and Johnson, James},
abstractNote = {A pilot scale pressurized (50 psi) fluidized bed gasification was performed to investigate the effects of the jet/ grid air ratio (5:95–90:10) and equivalence ratio (ER = 0.23–0.45) on the gasification products such as syngas, tar, contaminant gas, and biochar. There was a noticeable effect of the jet/grid ratios on the syngas concentration. An increase in CO, CH4, and C2 gases was obtained at the condition closer to jet/grid = 50:50, whereas a higher jet/grid ratio favored water–gas shift reaction by increasing CO2 and H2 gases under the pressurized condition. The highest lower heating value (LHV) of 7.7 MJ/Nm3 was obtained at the lowest ER = 0.23. Both the jet/grid ratio and ER were important parameters in determining the H2 concentration. The cold gasification and carbon conversion efficiencies were obtained as high as 66% and 94%, respectively. Also, higher temperature and ER promoted a reduction in contaminant gases as well as tar yield. Tar product yield was also reduced significantly after a wet scrubber, and the tar consisted of chemicals of a carbon number less than 13 (≤C12). Here, the gasification biochar was also analyzed and showed an effective carbon sequestration property with a relatively higher surface area (105 m2/g). Furthermore, computational fluid dynamics simulation was performed to determine the effects of different jet/grid air ratio and pressure conditions on the hydrodynamics in the fluidized bed reactor.},
doi = {10.1016/j.enconman.2018.05.003},
journal = {Energy Conversion and Management},
number = ,
volume = 168,
place = {United States},
year = {Fri May 25 00:00:00 EDT 2018},
month = {Fri May 25 00:00:00 EDT 2018}
}

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Cited by: 22 works
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