TY - JOUR
T1 - Experimental Study of Rice Husk Fluidization Without a Sand Bed Material on a Bubbling Fluidized Bed Gasifier
AU - Sonjaya, Abeth Novria
AU - Safitri, Kania
AU - Surjosatyo, Adi
N1 - Funding Information:
The authors would like to express their gratitude to the Ministry of Research and Technology/BRIN for funding this research [NKB-52/UN2.RST/HKP.05.00/2020].
Publisher Copyright:
© The author(s). Published by CBIORE.
PY - 2023/1
Y1 - 2023/1
N2 - This study aimed to determine the effect of rice husk fluidization and variation in the equivalence ratio of bubbling fluidized bed gasifiers without sand bed materials. It also aimed to improve the fluidization quality by reducing the diameter of rice husks. Therefore, the bulk density increases, whereas voidage decreases, both of which are the main parameters for improving the quality of fluidization in solid particles. Experiments were carried out at a velocity of 0.82 m/s, by varying the equivalent ratios ranging from 0.20 to 0.35, and analyzing the syngas composition, cold gas and carbon conversion efficiencies, lower heating value, and temperature distribution. An equivalence ratio of 0.30 was obtained for a bubbling fluidized gasifier with syngas compositions of 7.415%, 15.674%, 3.071%, 17.839%, and 56.031% for H2, CO, CH4, CO2, and N2, respectively. Under these conditions, we obtained cold gas and carbon conversion efficiencies and a lower heating value of 31.340%, 37.120%, and 3.881 MJ/Nm3, respectively.
AB - This study aimed to determine the effect of rice husk fluidization and variation in the equivalence ratio of bubbling fluidized bed gasifiers without sand bed materials. It also aimed to improve the fluidization quality by reducing the diameter of rice husks. Therefore, the bulk density increases, whereas voidage decreases, both of which are the main parameters for improving the quality of fluidization in solid particles. Experiments were carried out at a velocity of 0.82 m/s, by varying the equivalent ratios ranging from 0.20 to 0.35, and analyzing the syngas composition, cold gas and carbon conversion efficiencies, lower heating value, and temperature distribution. An equivalence ratio of 0.30 was obtained for a bubbling fluidized gasifier with syngas compositions of 7.415%, 15.674%, 3.071%, 17.839%, and 56.031% for H2, CO, CH4, CO2, and N2, respectively. Under these conditions, we obtained cold gas and carbon conversion efficiencies and a lower heating value of 31.340%, 37.120%, and 3.881 MJ/Nm3, respectively.
KW - bubbling fluidized bed gasifier
KW - equivalence ratio
KW - rice husk
KW - syngas
UR - http://www.scopus.com/inward/record.url?scp=85146226505&partnerID=8YFLogxK
U2 - 10.14710/ijred.2023.46068
DO - 10.14710/ijred.2023.46068
M3 - Article
AN - SCOPUS:85146226505
SN - 2252-4940
VL - 12
SP - 1
EP - 9
JO - International Journal of Renewable Energy Development
JF - International Journal of Renewable Energy Development
IS - 1
ER -