Simulation and Optimisation of Integrated Anaerobic-Aerobic Bioreactor (IAAB) for the Treatment of Palm Oil Mill Effluent

被引:15
|
作者
Chong, Jun Wei Roy [1 ]
Chan, Yi Jing [1 ]
Chong, Siewhui [1 ]
Ho, Yeek Chia [2 ]
Mohamad, Mardawani [3 ]
Tan, Wen Nee [4 ]
Cheng, Chin Kui [5 ,6 ]
Lim, Jun Wei [7 ]
机构
[1] Univ Nottingham Malaysia, Fac Sci & Engn, Dept Chem & Environm Engn, Semenyih 43500, Selangor, Malaysia
[2] Univ Teknol Petronas, Ctr Urban Resource Sustainabil, Civil & Environm Engn Dept, Inst Self Sustainable Bldg, Seri Iskandar 32610, Perak Darul Rid, Malaysia
[3] Univ Malaysia Kelantan, Fac Bioengn & Technol, Jeli Campus, Jeli 17600, Kelantan, Malaysia
[4] Univ Sains Malaysia, Sch Distance Educ, Chem Sect, Minden 11800, Penang, Malaysia
[5] Khalifa Univ, Coll Engn, Dept Chem Engn, POB 127788, Abu Dhabi, U Arab Emirates
[6] Khalifa Univ, Ctr Catalysis & Separat CeCaS, POB 127788, Abu Dhabi, U Arab Emirates
[7] Univ Teknol Petronas, Dept Fundamental & Appl Sci, HICoE Ctr Biofuel & Biochem Res, Inst Self Sustainable Bldg, Seri Iskandar 32610, Perak Darul Rid, Malaysia
关键词
palm oil mill effluent (POME); anaerobic; aerobic; biogas; optimisation; HYDRAULIC RETENTION TIME; PERFORMANCE EVALUATION; BIOGAS PRODUCTION; WASTE-WATER; DIGESTION; STRATEGIES; FOOD;
D O I
10.3390/pr9071124
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Y This study highlights an innovative piece of hybrid technology, whereby the combination of anaerobic and aerobic processes into a single reactor, namely, the integrated anaerobic-aerobic bioreactor (IAAB) can surpass the limits of conventional methods treating palm oil mill effluent (POME). Optimisation of IAAB using SuperPro Designer V9 simulator for maximum biogas yield while addressing its economic and environmental trade-offs was conducted for the first time. Parameters such as hydraulic retention time (HRT) and organic loading rate (OLR) were optimised in the anaerobic compartment from 10 days and 6.2 g COD/L day to 9 days and 6.9 g COD/L day, respectively. Furthermore, sludge recycle ratio was optimised from 20% to 50% in the aerobic compartment. The optimisation was successful where the biogas yield increased from 0.24 to 0.29 L CH4/g CODremoved with excellent Chemical Oxygen Demand (COD), and Biological Oxygen Demand (BOD) removal efficiencies up to 99% with 5.8% lower net expenditure. This simulation results were comparable against the pre-commercialized IAAB with 11.4% increase in methane yield after optimisation. Economic analysis had proven the optimised process to be feasible, resulting in return on investment (ROI), payback time, and internal rate of return (IRR) of 24.5%, 4.1 years, and 17.9%, respectively.
引用
收藏
页数:19
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