Combined mesophilic anaerobic and thermophilic aerobic digestion process for high-strength food wastewater to increase removal efficiency and reduce sludge discharge
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Jang, H. M.
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Pohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South KoreaPohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
Jang, H. M.
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Park, S. K.
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Ha, J. H.
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Pohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South KoreaPohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
Ha, J. H.
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Park, J. M.
[3
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[1] Pohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
[2] Pohang Univ Sci & Technol, Dept Chem Engn, Pohang 790784, South Korea
[3] Pohang Univ Sci & Technol, Div Adv Nucl Engn, Pohang 790784, South Korea
In this study, a process that combines the mesophilic anaerobic digestion (MAD) process with thermophilic aerobic digestion (TAD) for high-strength food wastewater (FWW) treatment was developed to examine the removal of organic matter and methane production. All effluent discharged from the MAD process was separated into solid and liquid portions. The liquid part was discarded and the sludge part was passed to the TAD process for further degradation. Then, the digested sludge from the TAD process was recycled back to the MAD unit to achieve low sludge discharge from the combined process. The reactor combination was operated in two phases: during Phase I, 40 d of total hydraulic retention time (HRT) was applied; during Phase II, 20 d was applied. HRT of the TAD process was fixed at 5 d. For a comparison, a control process (single-stage MAD) was operated with the same HRTs of the combined process. Our results indicated that the combined process showed over 90% total solids, volatile solids and chemical oxygen demand removal efficiencies. In addition, the combined process showed a significantly higher methane production rate than that of the control process. Consequently, the experimental data demonstrated that the combined MAD-TAD process was successfully employed for high-strength FWW treatment with highly efficient organic matter reduction and methane production.
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Pohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South KoreaPohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
Jang, Hyun Min
Ha, Jeong Hyub
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Pohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
Pohang Univ Sci & Technol, Dept Chem Engn, Pohang 790784, South KoreaPohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
Ha, Jeong Hyub
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Park, Jong Moon
Kim, Mi-Sun
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Korea Inst Energy Res, Biomass & Waste Energy Lab, Daejeon 305343, South KoreaPohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
Kim, Mi-Sun
Sommer, Sven G.
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Univ Southern Denmark, Fac Engn, Inst Chem Engn Biotechnol & Environm Technol, DK-5230 Odense M, DenmarkPohang Univ Sci & Technol, Sch Environm Sci & Engn, Pohang 790784, South Korea
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Gwangju Inst Sci & Technol, Sch Environm Sci & Engn, Gwangju 500712, South KoreaGwangju Inst Sci & Technol, Sch Environm Sci & Engn, Gwangju 500712, South Korea
Jang, Hyun Min
Ha, Jeong Hyub
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Pyeongtaek Univ, Dept Integrated Environm Syst, Seodong Daero 3825, Pyeongtaek 450701, South KoreaGwangju Inst Sci & Technol, Sch Environm Sci & Engn, Gwangju 500712, South Korea
Ha, Jeong Hyub
Kim, Mi-Sun
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Korea Inst Energy Res, Biomass & Waste Energy Lab, Daejeon 305343, South KoreaGwangju Inst Sci & Technol, Sch Environm Sci & Engn, Gwangju 500712, South Korea
Kim, Mi-Sun
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Kim, Jong-Oh
Kim, Young Mo
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Gwangju Inst Sci & Technol, Sch Environm Sci & Engn, Gwangju 500712, South KoreaGwangju Inst Sci & Technol, Sch Environm Sci & Engn, Gwangju 500712, South Korea