TY - JOUR
T1 - Enhancing the performance of pilot-scale fermentative hydrogen production by proper combinations of HRT and substrate concentration
AU - Lin, Ping Jei
AU - Chang, Jo Shu
AU - Yang, Lee Hao
AU - Lin, Chiu Yue
AU - Wu, Shu Yii
AU - Lee, Kuo Shing
N1 - Funding Information:
The authors gratefully acknowledge the financial support by Taiwan’s Bureau of Energy (Grant Nos. 98D0204-3 & 99D0204-3 ).
PY - 2011/10
Y1 - 2011/10
N2 - Our recent work showed the feasibility of using a 400 L pilot-scale bioreactor for hydrogen production via dark fermentation. However, the H 2 production performance of the pilot system was unsatisfactory when compared with that of lab-scale fermentors under the same conditions. This study applied engineering approaches to enhance the hydrogen production performance of the pilot bioreactor. First, a higher agitation rate was used to promote mass transfer efficiency. Next, the pilot system was operated under different combinations of hydraulic retention time (HRT) and substrate concentration (CS) that gives different sets of organic loading rate (OLR) to improve bioH2 production efficiency. With 25-30 rpm agitation rate and a OLR of 60 g COD/L/d (from combination of 8 h HRT and 20 g COD/L C S), the H2 production rate (HPR) of the pilot system reached 0.55 mol/L/d (13.4 m3/m3/d), which is 3.1 fold of that obtained from using a lower agitate rate (10-15 rpm). When operating at HRT = 6 h and CS = 30 g COD/L (i.e., OLR = 120 g COD/L/d), the pilot system obtained the highest HPR, hydrogen yield and overall hydrogen production efficiency of 1.18 mol/L/d, 3.84 mol H2/mol sucrose and 47.2%, respectively. This performance is similar to that obtained from the lab-scale system and is significantly higher than that from the original pilot tests prior to process optimization.
AB - Our recent work showed the feasibility of using a 400 L pilot-scale bioreactor for hydrogen production via dark fermentation. However, the H 2 production performance of the pilot system was unsatisfactory when compared with that of lab-scale fermentors under the same conditions. This study applied engineering approaches to enhance the hydrogen production performance of the pilot bioreactor. First, a higher agitation rate was used to promote mass transfer efficiency. Next, the pilot system was operated under different combinations of hydraulic retention time (HRT) and substrate concentration (CS) that gives different sets of organic loading rate (OLR) to improve bioH2 production efficiency. With 25-30 rpm agitation rate and a OLR of 60 g COD/L/d (from combination of 8 h HRT and 20 g COD/L C S), the H2 production rate (HPR) of the pilot system reached 0.55 mol/L/d (13.4 m3/m3/d), which is 3.1 fold of that obtained from using a lower agitate rate (10-15 rpm). When operating at HRT = 6 h and CS = 30 g COD/L (i.e., OLR = 120 g COD/L/d), the pilot system obtained the highest HPR, hydrogen yield and overall hydrogen production efficiency of 1.18 mol/L/d, 3.84 mol H2/mol sucrose and 47.2%, respectively. This performance is similar to that obtained from the lab-scale system and is significantly higher than that from the original pilot tests prior to process optimization.
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U2 - 10.1016/j.ijhydene.2011.04.147
DO - 10.1016/j.ijhydene.2011.04.147
M3 - Article
AN - SCOPUS:83055194547
SN - 0360-3199
VL - 36
SP - 14289
EP - 14294
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
IS - 21
ER -
