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Optimization of mechanical pre-treatment of Laminariaceae spp. biomass-derived biogas
Affiliation:1. Department of Mechanical and Manufacturing Engineering, Dublin City University, Glasnevin, Dublin 9, Ireland;2. Department of Electronic Engineering, Dublin City University, Glasnevin, Dublin 9, Ireland;3. Institute of Energy and Engineering Technology, University of the West of Scotland, Paisley PA1 2BE, Scotland, UK;1. MaREI Centre, Environmental Research Institute, University College Cork, Cork, Ireland;2. Key Laboratory of Low-grade Energy Utilization Technologies and Systems, Chongqing University, Chongqing 400044, China;3. School of Engineering, University College Cork, Cork, Ireland;1. School of Chemical Engineering, University of Queensland, Queensland, Australia;2. School of Civil Engineering, University of Queensland, Queensland, Australia;1. Department of Molecular Biotechnology, Graduate School of Advanced Sciences of Matter, Hiroshima University, 1-3-1 Kagamiyama, Higashi-Hiroshima 739-8530, Japan;2. Division of Energy and Environmental Engineering, Institute of Engineering, Hiroshima University, 1-4-1 Kagamiyama, Higashi-Hiroshima 739-8527, Japan;3. CREST, JST, Japan;1. Department of Mechanical Science and Engineering, Graduate School of Engineering, Hiroshima University, 1-4-1 Kagamiyama, Higashi-Hiroshima, 739-8527, Japan;2. Department of Molecular Biotechnology, Graduate School of Advanced Sciences of Matter, Hiroshima University, 1-3-1 Kagamiyama, Higashi-Hiroshima, 739-8530, Japan;3. Division of Energy and Environmental Engineering, Institute of Engineering, Hiroshima University, 1-4-1 Kagamiyama, Higashi-Hiroshima, 739-8527, Japan;1. Department of Civil Engineering, Regional Campus Anna University, Tirunelveli, India;2. Department of Plant Science, Manonmaniam Sundaranar University, Abishekapatti, Tirunelveli, 627 012, Tamil Nadu, India;3. Graduate School of Water Resources, Sungkyunkwan University, Suwon, Republic of Korea;4. Department of Environmental Energy Engineering, Kyonggi University, Suwon, Republic of Korea;5. Department of Food Science and Biotechnology, Dongguk University-Seoul, Ilsandong-gu, Goyang-si, Gyeonggi-do 10326, Republic of Korea
Abstract:Macroalgae have not met their full potential to date as biomass for the production of energy. One reason is the high cost associated with the pretreatment which breaks the biomass's crystalline structure and better exposes the fermentable sugars to anaerobes. In the attempt to overcome this technological barrier, the performance of a Hollander beater mechanical pretreatment is assessed in this paper. This pretreatment has been applied to a batch of Laminariaceae biomass and inoculated with sludge from a wastewater treatment plant. The derived biogas and methane yields were used as the responses of a complex system in order to identify the optimal system input variables by using the response surface methodology (RSM). The system's inputs considered are the mechanical pretreatment time (5–15 min range), the machine's chopping gap (76–836 μm) and the mesophilic to thermophilic range of temperatures (30–50 °C). The mechanical pretreatment was carried out with the purpose of enhancing the biodegradability of the macroalgal feedstock by increasing the specific surface area available during the anaerobic co-digestion. The pretreatment effects on the two considered responses are estimated, discussed and optimized using the tools provided by the statistical software Design-Expert v.8. The best biogas yield of treated macroalgae was found at 50 °C after 10 min of treatment, providing 52% extra biogas and 53% extra methane yield when compared to untreated samples at the same temperature conditions. The highest biogas rate achieved by treating the biomass was 685 cc gTS?1, which is 430 cc gTS?1 in terms of CH4 yield.
Keywords:Anaerobic co-digestion  Sludge  Mechanical pretreatment  Methane yield  Optimisation  AD"}  {"#name":"keyword"  "$":{"id":"kwrd0045"}  "$$":[{"#name":"text"  "_":"anaerobic digestion  ANOVA"}  {"#name":"keyword"  "$":{"id":"kwrd0055"}  "$$":[{"#name":"text"  "_":"analysis of variance  BBD"}  {"#name":"keyword"  "$":{"id":"kwrd0065"}  "$$":[{"#name":"text"  "_":"Box–Behnken design  BT"}  {"#name":"keyword"  "$":{"id":"kwrd0075"}  "$$":[{"#name":"text"  "_":"beating time  COD"}  {"#name":"keyword"  "$":{"id":"kwrd0085"}  "$$":[{"#name":"text"  "_":"chemical oxygen demand  HRT"}  {"#name":"keyword"  "$":{"id":"kwrd0095"}  "$$":[{"#name":"text"  "_":"hydraulic retention time  MC"}  {"#name":"keyword"  "$":{"id":"kwrd0105"}  "$$":[{"#name":"text"  "_":"moisture content  MG"}  {"#name":"keyword"  "$":{"id":"kwrd0115"}  "$$":[{"#name":"text"  "_":"machine's gap  RSM"}  {"#name":"keyword"  "$":{"id":"kwrd0125"}  "$$":[{"#name":"text"  "_":"response surface methodology  temperature  TS"}  {"#name":"keyword"  "$":{"id":"kwrd0145"}  "$$":[{"#name":"text"  "_":"total solids  VFA"}  {"#name":"keyword"  "$":{"id":"kwrd0155"}  "$$":[{"#name":"text"  "_":"volatile fatty acids  VS"}  {"#name":"keyword"  "$":{"id":"kwrd0165"}  "$$":[{"#name":"text"  "_":"volatile solids
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