Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor
The biological conversion of biomass into methane during anaerobic digestion has been studied by many researchers in recent years. In this study, optimization of methane composition during chemical oxygen demand removal was observed in a multi-stage Anaerobic Bioreactor. Synthetic glucose was used a...
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| Format: | Article |
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Taylor and Francis Inc.
2016
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| _version_ | 1796861776042655744 |
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| author | Shahperi, R. Din, M. F. M. Chelliapan, S. Aris, M. A. M. Selvam, S. B. Abdullah, N. Yuzir, M. A. M. |
| author_facet | Shahperi, R. Din, M. F. M. Chelliapan, S. Aris, M. A. M. Selvam, S. B. Abdullah, N. Yuzir, M. A. M. |
| author_sort | Shahperi, R. |
| collection | ePrints |
| description | The biological conversion of biomass into methane during anaerobic digestion has been studied by many researchers in recent years. In this study, optimization of methane composition during chemical oxygen demand removal was observed in a multi-stage Anaerobic Bioreactor. Synthetic glucose was used as a feed substrate, and the reactor was operated at a hydraulic retention time (HRT) of 1–4 d. Complementary experimental and theoretical test procedures were evaluated for methane optimization. The theoretical methane was recorded as 50.13, 50.02, 50.16, and 50.22% for an HRT of 4, 3, 2, and 1 d, respectively. However, the quantity of methane determined experimentally was significantly lower than the theoretical predictions; this was likely due to the microorganism activity in the reactor that may have interfered with the efficiency of the biogas generation. Experimental data showed a decrease in the methane composition (35.4, 21.2, 19.8, and 18.4% for HRT of 4, 3, 2, and 1 d, respectively) in the reactor system. Thus, the theoretical formula and experimental data together provide an alternative method for the evaluation of bioenergy potential in anaerobic digestion. |
| first_indexed | 2024-03-05T20:01:32Z |
| format | Article |
| id | utm.eprints-71507 |
| institution | Universiti Teknologi Malaysia - ePrints |
| last_indexed | 2024-03-05T20:01:32Z |
| publishDate | 2016 |
| publisher | Taylor and Francis Inc. |
| record_format | dspace |
| spelling | utm.eprints-715072017-11-15T03:38:46Z http://eprints.utm.my/71507/ Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor Shahperi, R. Din, M. F. M. Chelliapan, S. Aris, M. A. M. Selvam, S. B. Abdullah, N. Yuzir, M. A. M. TA Engineering (General). Civil engineering (General) The biological conversion of biomass into methane during anaerobic digestion has been studied by many researchers in recent years. In this study, optimization of methane composition during chemical oxygen demand removal was observed in a multi-stage Anaerobic Bioreactor. Synthetic glucose was used as a feed substrate, and the reactor was operated at a hydraulic retention time (HRT) of 1–4 d. Complementary experimental and theoretical test procedures were evaluated for methane optimization. The theoretical methane was recorded as 50.13, 50.02, 50.16, and 50.22% for an HRT of 4, 3, 2, and 1 d, respectively. However, the quantity of methane determined experimentally was significantly lower than the theoretical predictions; this was likely due to the microorganism activity in the reactor that may have interfered with the efficiency of the biogas generation. Experimental data showed a decrease in the methane composition (35.4, 21.2, 19.8, and 18.4% for HRT of 4, 3, 2, and 1 d, respectively) in the reactor system. Thus, the theoretical formula and experimental data together provide an alternative method for the evaluation of bioenergy potential in anaerobic digestion. Taylor and Francis Inc. 2016 Article PeerReviewed Shahperi, R. and Din, M. F. M. and Chelliapan, S. and Aris, M. A. M. and Selvam, S. B. and Abdullah, N. and Yuzir, M. A. M. (2016) Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor. Desalination and Water Treatment, 57 (60). pp. 29168-29177. ISSN 1944-3994 https://www.scopus.com/inward/record.uri?eid=2-s2.0-84975223576&doi=10.1080%2f19443994.2016.1189705&partnerID=40&md5=2e714d9dc7c5e4257a20cddaf81dfd8f |
| spellingShingle | TA Engineering (General). Civil engineering (General) Shahperi, R. Din, M. F. M. Chelliapan, S. Aris, M. A. M. Selvam, S. B. Abdullah, N. Yuzir, M. A. M. Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor |
| title | Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor |
| title_full | Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor |
| title_fullStr | Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor |
| title_full_unstemmed | Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor |
| title_short | Optimization of methane production process from synthetic glucose feed in a multi-stage anaerobic bioreactor |
| title_sort | optimization of methane production process from synthetic glucose feed in a multi stage anaerobic bioreactor |
| topic | TA Engineering (General). Civil engineering (General) |
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