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Life cycle analysis of alfalfa stem-based bioethanol production system

Date

2011-10-31

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Degree Level

Masters

Abstract

Alfalfa stem can be a potential feedstock for producing bioethanol. Numerous studies have been carried out to assess the conversion of different feedstocks into bioethanol, although studies related to life cycle assessment (LCA) of feedstocks such as alfalfa are limited. However, LCA does serve to highlight areas where positive and negative impacts can be expected in the overall biomass to ethanol process. This research therefore focuses on investigating and evaluating an alfalfa bioethanol production system in terms of five key life cycle impact categories: abiotic depletion (AD), acidification (A), eutrophication (E), global warming (GW), human toxicity (HT), and energy demand. The study concerns three subsystems: the cultivation subsystem (S1), the baling and pre-processing subsystem (S2), and the ethanol conversion subsystem (S3). Each subsystem could have different scenarios depending on specified input combinations, and SimaPro 7.2 with CML 2 baseline 1990 V2.05 version was used to assess environmental impacts. The results of energy assessment correspond to LCA results, showing that the environmental impact associated with alfalfa-ethanol production increases with increased energy demand. Energy analysis of S1 showed that the energy requirements for producing 1 kg of alfalfa under non-irrigated and irrigated cultivation were between 0.63 MJ to 1.30 MJ and 0.51 MJ to 0.94 MJ, respectively. The best input combination in S1 was inorganic fertilizer with irrigation, for it consumed 0.51 MJ/kg energy and resulted in the least environmental impact. The energy requirements for the postharvest pre-processing of 1 kg of alfalfa biomass were 0.82 MJ to 1.62 MJ under different iii scenarios, with the drum drying requiring the highest energy in S2: 0.197 MJ of electricity and heat per hectare. Considering the three systems (namely S1, S2, and S3) demonstrates that irrigated alfalfa production scenarios revealed lower energy demands in comparison to nonirrigated scenarios; inorganic scenarios showed lower energy demand over organic scenarios. Compared to the use of organic fertilizers, application of inorganic fertilizers has decreased the impact with respect to AD, A, GW, and HT while slightly increasing E in S1, S2, and S3. Therefore, the most favourable scenario was the inorganic irrigated scenario in all subsystems. The LCA results concluded that GW was the most influential impact category for all three subsystems, whereas AD, A, E, and HT had a comparatively lower impact on each system. To produce 1 L of ethanol, 32.78 MJ (minimum) to 38.43 MJ (maximum) of energy input was required for S3 in all production scenarios at 50% water recycling. In S1, S2, and S3, the inorganic irrigated scenarios had lower energy demands than the organic irrigated scenarios. The highest energy consuming process in S3 was ethanol plant heat energy. Overall, the inorganic, irrigated, and 50% water recycling represented the best case scenario for all subsystems (S1, S2, and S3) in terms of energy demand with an average of 7.82 MJ for 1 kg of alfalfa biomass input. Comparing the three subsystems shows that the alfalfa cultivation subsystem (S1) consumed 6.2% to 15.1% of the total energy. The ethanol conversion subsystem (S3) is the highest energy consuming subsystem in this study, falling into the 77.5% - 94.8% range of the total for different scenarios. The baling and pre-processing subsystem (S2) required between 3.5% and iv 4.0% of the total energy. Future studies could assess different allocation methods and coproduct credits for the establishment of a sustainable cellulosic biorefinery.

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Keywords

Life Cycle Analysis (LCA), Alfalfa, Bioethanol, Abiotic depletion, Acidification, Eutrophication, Global warming, Human toxicity, SimaPro 7.2, sustainable cellulosic biorefinery

Citation

Degree

Master of Science (M.Sc.)

Department

Agricultural and Bioresource Engineering

Program

Agricultural and Bioresource Engineering

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