TY - JOUR
T1 - Design and Development of Bubbling Fluidized Bed Gasifier for Non-Woody Biomass Gasification
AU - Hossain, Mohammad Shahadat
AU - Kumar, Deepak
AU - Paul, Nishat
AU - Rahman, Syed Jahid
AU - Rahman, Mohammad Anisur
AU - Uddin, Mohammad Rakib
AU - Pirozzi, Domenico
AU - Uddin, Mohammad Nazim
AU - Yousuf, Abu
N1 - Publisher Copyright:
Copyright © 2022, AIDIC Servizi S.r.l.
PY - 2022
Y1 - 2022
N2 - Bubbling fluidized bed (BFB) reactor is advantageous for synthesis gas or syngas production among other available gasifiers. In this study, a BFB gasifier has been designed, utilizing non-woody biomass (rice straw) and air as gasifying medium, to investigate the effect of equivalence ratio (ER), static bed height, and operating temperature on synthesis gas yield and gasification efficiency. To calculate various structural and operating parameters, a reaction chamber with a diameter of 10 cm and a bed material of 400-500 μm has been studied. Considering the minimum fluidization velocity, slugging velocity, and terminal velocity, the optimum operating velocity has been taken as 17.25 cm/s. The calculated optimum transport disengagement height (TDH) is 86 cm, and the freeboard height is approximately 116 cm. Thus, the overall height of the reactor has come up as 202 cm. Almost 80% carbon conversion efficiency (CCE) was achieved from this BFB reactor with an optimum ER value of 0.35 during rice straw gasification. The same gasifier results in a synthesis gas yield of 3.6 Nm3/kg with a lower heating value (LHV) of about 3.5 MJ/Nm3at optimum ER value. Further scaling up this process based on the findings of this study for industrial-scale synthesis gas production can pave a way for bioenergy generation from non-woody biomass.
AB - Bubbling fluidized bed (BFB) reactor is advantageous for synthesis gas or syngas production among other available gasifiers. In this study, a BFB gasifier has been designed, utilizing non-woody biomass (rice straw) and air as gasifying medium, to investigate the effect of equivalence ratio (ER), static bed height, and operating temperature on synthesis gas yield and gasification efficiency. To calculate various structural and operating parameters, a reaction chamber with a diameter of 10 cm and a bed material of 400-500 μm has been studied. Considering the minimum fluidization velocity, slugging velocity, and terminal velocity, the optimum operating velocity has been taken as 17.25 cm/s. The calculated optimum transport disengagement height (TDH) is 86 cm, and the freeboard height is approximately 116 cm. Thus, the overall height of the reactor has come up as 202 cm. Almost 80% carbon conversion efficiency (CCE) was achieved from this BFB reactor with an optimum ER value of 0.35 during rice straw gasification. The same gasifier results in a synthesis gas yield of 3.6 Nm3/kg with a lower heating value (LHV) of about 3.5 MJ/Nm3at optimum ER value. Further scaling up this process based on the findings of this study for industrial-scale synthesis gas production can pave a way for bioenergy generation from non-woody biomass.
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U2 - 10.3303/CET2292049
DO - 10.3303/CET2292049
M3 - Article
AN - SCOPUS:85133701021
SN - 1974-9791
VL - 92
SP - 289
EP - 294
JO - Chemical Engineering Transactions
JF - Chemical Engineering Transactions
ER -