The push for alternatives to petroleum fuels has forced researchers to look for highly productive, renewable, non-food resources. The advantages of using microalgae instead of traditional oil crops for biofuel production include high oil yields, rapid reproductive rates, and versatile growing requirements. In order to reduce the cost of producing microalgae based biofuels, wastewater has been used as a nutrient source instead of specialized plant nutrients. The purpose of this study was to compare the relative effectiveness of different combinations of microalgae strain and dairy wastewater for increasing biomass. The methods for monitoring growth included optical density, cell counting, biomass estimation by chlorophyll-a, and volatile suspended solids. The analyses compared four concentrations of wastewater media as well as four strain treatments: Chlorella vulgaris, Tetraselmis sp., mixed freshwater culture and mixed saltwater culture. Optimum wastewater concentrations for microalgae growth were approximately 0% and 25% for most strain treatments. The results of the wastewater treatments concluded that dairy wastewater could serve as an effective nutrient substitute for plant food at concentrations approximately 25%. Chlorella vulgaris and Tetraselmis sp. prevailed over the mixed cultures for biomass production. Nitrate was the most limiting nutrient and exhibited the greatest reductions, sometimes in excess of 90%. The regression equations derived from the volatile suspended solids data achieved high R2 values and determined that total nitrogen, ammonium, and nitrate were significant in the model. In those equations, increasing either ammonium or nitrate yielded an increase in volatile suspended solids. With regards to comparing biomass quantification methods, the two most useful and reliable biomass quantification methods were optical density and volatile suspended solids.

No description available.

In this research a test system was developed that is designed as a tool to evaluate the potential hazard of chemicals to aquatic ecosystems. The system developed is a linear three-trophic level food chain consisting of an alga (Ch/ore/la vulgaris), rotifer (Brachionus calyciflorus), and fish (Pimephales promelas). The chemostat design used for the lower two trophic levels was crucial in being able to supply the top trophic level with sufficient food on a continuous basis. The system was initially evaluated using copper (Cu) and selenium (Se) as toxicants. In the copper experiments, results of a 7 day three-trophic level toxicity test were compared with a series of single species tests. The LOEC was 31.5 µg/L based on a temporary impairment of the algal population growth, with a corresponding NOEC of 16.2 µg/L. The algal population at all initially impaired treatment levels demonstrated recovery to control levels by the end of the test. Single species tests with the same species showed impairment at treatment concentrations lower than the corresponding value from the three-trophic level test. The difference in sensitivity is attributable to the fact that most of the Cu in the single species tests was in the dissolved form (approximately 80 %), whereas in the trophic level test most of the Cu was not ( < 15 % dissolved Cu). The three-trophic level Se experiment lasted for 25 days, with both short-term and long-term impacts evident. At the algal trophic level, growth was not impaired on a daily basis at any of the exposure levels (110.3, 207.7, and 396.1 µg/L Se). However, algal densities were slightly reduced at the 207. 7 and 396.1 µg Sell treatments, although not significantly different when the data was pooled across days. Rotifer populations were impaired at these same levels by day 4, and succumbed to the Se by day 7. Fathead minnow growth was also impaired at these two concentrations by day 7. In addition, sub lethal impairment of rotifer and fish growth was evident at the 110.3 pg/L level after day 20 indicating a more subtle trophic impact. Bioconcentration factors ranged between 100 and 1000 µg/L and were found to be dependent on the species, treatment, and day. / Ph. D.

L'électrocoagulation (EC) est une méthode électrochimique non spécifique couramment utilisée pour le traitement de l'eau et des eaux usées. Dans ce travail, l’EC est d'abord étudiée comme une technique classique de traitement des eaux usées dédiée à l'élimination des protéines de lactosérum de l'eau pour laquelle les mécanismes d'élimination sont expliqués et un modèle est développé. Ensuite, l'utilisation de l’EC est étendue à la séparation et à la purification d’acides gras volatils issus de la fermentation acidogénique. Dans cette deuxième étude, les effets des paramètres opératoires sur l'efficacité et le coût de l’EC sont discutés. En outre, l’EC est utilisée pour la récolte de deux espèces de microalgues de leur milieu de culture. En ce qui concerne la récolte de Chlamydomonas reinhardtii, la méthodologie de la surface de réponse est utilisée et deux modèles permettant de prédire respectivement l'efficacité de la récupération et le coût opératoire sont développés. La récolte d’une autre espèce de microalgues, Chlorella vulgaris, est étudiée en utilisant l’EC respectivement en mode discontinu et continu. En mode discontinu, les effets des principaux paramètres de fonctionnement sur l'efficacité du processus sont expliqués et les mécanismes de récupération sont discutés. Dans l'étude en mode continu, la méthodologie de la surface de réponse est utilisée et un modèle permettant de prédire l’efficacité de récupération des microalgues est développé. Enfin, la comparaison des performances de l'EC en mode continu avec et sans échange de polarité aux performances de l'EC en mode discontinu est effectuée. / Electrocoagulation (EC) is a non-specific electrochemical method usually used for water and wastewater treatment. In this work, EC is firstly investigated as a conventional wastewater treatment technique for the removal of whey proteins from water, where the mechanisms of removal are explained and a model on whey proteins elimination is developed. Then, EC use is extended for the separation and purification of volatile fatty acids issued from acidogenic fermentation. In this second study, the effects of operating parameters on EC efficiency and cost are discussed. Moreover, EC is used for the harvesting of two microalgae species from their culture medium. In the study that concerns recovering Chlamydomonas reinhardtii, response surface methodology (RSM) is employed and two models for predicting recovery efficiency and operating cost are developed. The harvesting of the other microalgae species Chlorella vulgaris is studied using EC in the batch and continuous modes. In the batch mode, the effects of the main operating parameters on the process effectiveness are explained along with discussing the mechanisms of recovery. In the continuous mode study, response surface methodology (RSM) is applied and a model for predicting microalgae recovery is developed. Finally, comparison of EC performance in continuous mode with and without polarity exchange (PE) to EC performance in batch mode is carried out.

In our pervious study, the ethanol extracts from Eupatorium fortunei Turcz at concentrations of 200 ÷ 500 mg L-1 significantly inhibited the growth of Microcystis aeruginosa, which is the most common species, responsible for toxic cyanobacteria blooming in fresh water. o-Coumaric acid (or 2-hydroxy-cinnamic acid) isolated from E. fortunei was tested its growth-inhibitory effect on M. aeruginosa and Chlorella vulgaris at the concentrations of 1.0, 10.0 and 100.0 mg L-1 in the 96- hour experiment by the optical density and the analytical method of chlorophyll a concentration. Results indicated that the compound strongly affected towards M. aeruginosa at the concentration of 100.0 mg L-1 with the inhibition efficiency (IE) values of 76.76 % and 84.66 %, respectively while those for C. vulgaris were lower just of 60.59%, and 74.53 %, respectively. The obtained data demonstrated that two methods were highly consistent and o- coumaric acid was more toxic to M. aeruginosa than C. vulgaris at all tested concentrations (p<0.05). The images of M. aeruginosa and C. vulgaris cells under the light microscope clearly showed the damage of these cells under the attck of o-coumaric acid. Although o-coumaric compound was widely demonstrated antibacterial properties in previous reports, to the best of our knowledge, our study was the first report about effect of o- coumaric acid on the growth of M. aeruginosa and C. vulgaris. / Những nghiên cứu trước đây đã chỉ ra rằng cao chiết etanol từ cây Mần tưới Eupatorium fortune Turcz tại dải nồng độ 200 ÷ 500 μg mL-1 ức chế mạnh sinh trưởng của Microcystis aeruginosa, - loài phổ biến nhất gây nên sự bùng nổ tảo độc trong hệ sinh thái nước ngọt. o-Coumaric axit (hay 2-hydroxy-cinnamic axit) phân lập từ E. fortune được tiến hành đánh giá ảnh hưởng lên sinh trưởng của hai loài M. aeruginosa và Chlorella vulgaris tại ba nồng độ là 1.0, 10.0 and 100.0 mg L-1 trong thời gian 96 giờ thực nghiệm theo phương pháp đo mật độ quang và phân tích hàm lượng chlorophyll a. Kết quả nghiên cứu cho thấy sau 96 giờ phơi nhiễm tại nồng độ 100 mg L-1 hoạt chất ức chế mạnh tới M. aeruginosa với giá trị ức chế sinh trưởng (IE) tương ứng là 76.76 và 84.66%. Giá trị IE đối với C.vulgaris ghi nhận thấp hơn chỉ là 60.65 và 74.53%, tương ứng. Hai phương pháp phân tích trên có tính nhất quán cao và o-coumaric ức chế sinh trưởng lên loài M.aeruginosa mạnh hơn so với loài C.vulgaris tại tất cả các nồng độ nghiên cứu (p<0.05). Ảnh chụp các tế bào M.aeruginosa và C.vulgaris dưới kính hiển vi điện tử đã chứng minh những tổn thương của tế bào dưới tác động của o-coumaric axit. Mặc dù o- coumaric cho thấy đặc tính chống khuẩn cao trong các công bố trước đây, nhưng theo hiểu biết của chúng tôi đây là nghiên cứu đầu tiên công bố về ảnh hưởng của hoạt chất o-coumaric axit lên sinh trưởng của M. aeruginosa và C. vulgaris.

The use of microalgae culture to convert CO2 from power plant flue gases into biomass that are readily converted into biofuels offers a new frame of opportunities to enhance, compliment or replace fossil-fuel-use. Apart from being renewable, microalgae also have the capacity to utilise materials from a variety of wastewater and the ability to yield both liquid and gaseous biofuels. However, the processes of cultivation, incorporation of a production system for power plant waste flue gas use, algae harvesting, and oil extraction from the biomass have many challenges. Using SimaPro software, Life cycle Assessment (LCA) of the challenges limiting the microalgae (Chlorella vulgaris) biofuel production process was performed to study algae-based pathway for producing biofuels. Attention was paid to material use, energy consumed and the environmental burdens associated with the production processes. The goal was to determine the weak spots within the production system and identify changes in particular data-set that can lead to and lower material use, energy consumption and lower environmental impacts than the baseline microalgae biofuel production system. The analysis considered a hypothetical transesterification and Anaerobic Digestion (AD) transformation of algae-to- biofuel process. Life cycle Inventory (LCI) characterisation results of the baseline biodiesel (BD) transesterification scenario indicates that heating to get the biomass to 90% DWB accounts for 64% of the total input energy, while electrical energy and fertilizer obligations represents 19% and 16% respectively. Also, Life Cycle Impact Assessment (LCIA) results of the baseline BD production scenario show high proportional contribution of electricity and heat energy obligations for most impact categories considered relative to other resources. This is attributed to the concentration/drying requirement of algae biomass in order to ease downstream processes of lipid extraction and subsequent transesterification of extracted lipids into BD. Thus, four prospective alternative production scenarios were successfully characterised to evaluate the extent of their impact scenarios on the production system with regards to lowering material use, lower energy consumption and lower environmental burdens than the standard algae biofuel production system. A 55.3% reduction in mineral use obligation was evaluated as the most significant impact reduction due to the integration of 100% recycling of production harvest water for the AD production system. Recycling also saw water demand reduced from 3726 kg (freshwater).kgBD- 1 to 591kg (freshwater).kgBD- 1 after accounting for evaporative losses/biomass drying for the BD transesterification production process. Also, the use of wastewater/sea water as alternative growth media for the BD production system, indicated potential savings of: 4.2 MJ (11.8%) in electricity/heat obligation, 10.7% reductions for climate change impact, and 87% offset in mineral use requirement relative to the baseline production system. Likewise, LCIA characterisation comparison results comparing the baseline production scenarios with that of a set-up with co-product economic allocation consideration show very interesting outcomes. Indicating -12 MJ surplus (-33%) reductions for fossil fuels resource use impact category, 52.7% impact reductions for mineral use impact and 56.6% reductions for land use impact categories relative to the baseline BD production process model. These results show the importance of allocation consideration to LCA as a decision support tool. Overall, process improvements that are needed to optimise economic viability also improve the life cycle environmental impacts or sustainability of the production systems. Results obtained have been observed to agree reasonably with Monte Carlo sensitivity analysis, with the production scenario proposing the exploitation of wastewater/sea water to culture algae biomass offering the best result outcome. This study may have implications for additional resources such as production facility and its construction process, feedstock processing logistics and transport infrastructure which are excluded. Future LCA study will require extensive consideration of these additional resources such as: facility size and its construction, better engineering data for water transfer, combined heat and power plant efficiency estimates and the fate of long-term emissions such as organic nitrogen in the AD digestate. Conclusions were drawn and suggestions proffered for further study.

Orientador: Marcela Aparecida Guerreiro Machado / Resumo: A microalga Chlorella possui ácidos graxos poli-insaturados, vitaminas e alto conteúdo proteico. Desse modo, estudos recentes têm explorado o uso de microalgas para obtenção de lipídios, principalmente os de maior valor comercial como o ácido ɣ-linolênico. Estre trabalho objetivou propor um método de cultivo para a microalga Chlorella vulgaris e extração do óleo. Os experimentos foram realizados em duplicata de acordo com o arranjo ortogonal de Taguchi, a partir da qual foram organizadas duas etapas: na primeira foram viabilizados cultivos nos quais os fatores de interesse pudessem ser avaliados em dois níveis de operação: Aeração (1,67 e 3,33L/min), NO3 (0,25 e 0,50 g/L), PO4 -3 (0,35 e 0,65 g/L), NaHCO3 (0,25 e 0,50 g/L), intensidade de luz (0,85 e 14,50 K luz) e fotoperíodo (12 e 24 h). Em tal etapa correu também a colheita, floculação, secagem e moagem da biomassa. Na segunda etapa foram realizadas as extrações lipídicas de acordo com e uso de solventes como o clorofórmio e metanol, utilizou-se também o banho de ultrassom para as extrações dos teores lipídicos. Obteve melhor resultado a concentração de biomassa algal, a qual atingiu a concentração de nitrato (0,50 g/L), concentração de bicarbonato de sódio (0,50 g/L), fosfato (0,65 g/L) e fotoperíodo de 12 em 12hs. O melhor resultado para a extração lipídica ocorreu conforme a metodologia de Zorn (2017), com aproximadamente 2,5% mais eficiente e obteve o seguinte resultado para os fatores, no nível alto são: aeração (3,33... (Resumo completo, clicar acesso eletrônico abaixo) / Abstract: The micro-algae Chlorella has polyunsaturated fatty acids, vitamins and high protein content. Thus, recent studies have explored the use of microalgae to obtain lipids, especially those with higher commercial value such as β-linolenic acid. The objective of this work was to propose a method of cultivation for the microalga Chlorella vulgaris and extraction of the oil. The experiments were carried out in duplicate according to Taguchi's orthogonal arrangement, from which two stages were organized: in the first, cultures were feasible in which the factors of interest could be evaluated at two levels of operation: aeration (1.67 e 3.33L/min), PO4 -3 (0.35 and 0.65 g / L), NaHCO 3 (0.25 and 0.50 g / L), NO 3 (0.25 and 0.50 g / L) , light intensity (0.85 and 14.50 K light) and photoperiod (12 and 24 h). In this stage also the harvest, flocculation, drying and milling of the biomass took place. In the second stage, the lipid extractions were performed according to the use of solvents such as chloroform and methanol, and the ultrasonic bath was used to extract the lipid contents. The best results were the algal biomass concentration, which reached the concentration of nitrate (0.50 g / L), sodium bicarbonate (0.50 g / L), phosphate (0.65 g / L) and photoperiod every 12 hours The best result for the lipid extraction occurred according to the Zorn (2017) methodology, with approximately 2.5% more efficient and obtained the following result for the factors, at the high level are: aerati... (Complete abstract click electronic access below) / Mestre

With greenhouse gas emissions (of which CO2 is the major component) being a major environmental concern, mitigation of those emissions is becoming increasingly imperative. The ability to use a fast growing, photosynthetic organism like microalgae that can survive primarily on nutrients such as sunlight and air (with increased CO2 levels) makes it a desirable agent for CO2 sequestration. The primary goal of this project is the engineering of the sequestration of CO2 using the cultivation of the microalgae species <i>Chlorella vulgaris</i>. Secondary goals of the project are the exploration and development of valuable by-products of the cultivation and the determination of whether utilizing microalgae to capture CO2 could be integrated economically into an industrial facility.<p> The batch growth kinetics of the photosynthetic algal species <i>C. vulgaris</i> were investigated using a well-mixed stirred bioreactor. The growth rate was found to increase as the dissolved CO2 increased to 150 mg/L (10% CO2 by volume in the gas), but fell dramatically at higher concentrations. Increasing the radiant flux also increased growth rate. With a radiant flux of 32.3 mW falling directly on the 500 mL culture media, the growth rate reached up to 3.6 mg of cells/L-h. Both pH variation (5.5 - 7.0) and mass transfer rate of CO2 (KLa between 6 h-1 and 17 h-1) had little effect on growth rate.<p> The operation of continuously stirred tank bioreactors (CSTBs) at minimum cost is a major concern for operators. In this work, a CSTB design strategy is presented where impeller stirring speed and aeration rate are optimized to meet the oxygen demand of growing cells, simultaneously minimizing the capital and operating cost. The effect of microbial species, ions in the culture medium, impeller style, as well as changing CSTB size and biomass input density on the optimum operating conditions, is examined. A study of the effects of various parameters on the CSTB design is shown.<p> Using the kinetic data collected in the batch growth study, a novel external loop airlift photobioreactor (ELAPB) was designed and tested. A model was developed for <i>C. vulgaris</i> growth in the ELAPB that incorporated growth behaviour, light attenuation, mass transfer, and fluid dynamics. The model predicts biomass accumulation, light penetration, and transient CO2 concentrations, and compares predictions to experimental data for radiant fluxes of 0.075 1.15 W/m2 and 0 20% CO2 enrichment of feed air, with a 10% average error. The effect of radiant flux and CO2 concentration is presented with discussion of radial and vertical profiles along the column. For a fed-batch culture at a biomass density of 170 mg/L, the penetration of the radiant flux was found to decrease by 50% within the first 1 cm, and 75% at 2 cm. Theoretical optimum growth conditions are determined to be 0.30 W/m2 and 6% CO2 enrichment of inlet feed air.<p> The algal culture was observed to be a workable electron acceptor in a cathodic half cell. A net potential difference of 70 mV was achieved between the growing <i>C. vulgaris</i> culture acting as a cathode and a 0.02 M potassium ferrocyanide anodic half cell. Surge current and power levels of 1.0 µA/mg of cell dry weight and 2.7 mW/m2 of cathode surface area were measured between these two half cells. The recently developed photosynthetic cathode was also coupled to a fermentative anode to produce a completely microbial fuel cell. Loading effects and the effect of changing culture conditions on fuel cell operation are reported. The maximum power output measured was 0.95 mW/ m2 at 90 V and 5000 ohms. A significant increase in this output is achieved with the addition of supplemental glucose to the anodic half cell and the enrichment of the feed air bubbled into the cathodic half cell with 10% CO2.<p> Two economic feasibility studies were performed on the integration of ELAPBs into an industrial facility. These integration studies operated the ELAPBs continuously as biocathodes in coupled microbial fuel cells (MFCs) that capture CO2 from an existing 130 million L/yr bioethanol plant, while generating electrical power and yielding oil for biodiesel to provide operational revenue to offset costs. The anodes for the coupled MFCs are the existing yeast batch fermentors, and the CO2 to be sequestered comes from the existing bioethanol production. Two different design schemes were evaluated, in both cases the maximum profit was achieved with the maximum number of tall columns operated in parallel. The first design evaluated a batch bioethanol facility with off-site oil processing, and the economic feasibility is demonstrated by the positive Net Present Worth achieved over the 20 year life of the plant, at a 10% rate of return on investment. The second design, for a continuous bioethanol operation, processes both oil and algae biomass on-site, but the economics of this second process are only positive (Internal Rate of Return 9.93%.) if the government provides financial assistance in the form of generous carbon credits (a speculative $100 per tonne of CO2 not yet attained) and a 25% capital equipment grant.

With greenhouse gas emissions (of which CO2 is the major component) being a major environmental concern, mitigation of those emissions is becoming increasingly imperative. The ability to use a fast growing, photosynthetic organism like microalgae that can survive primarily on nutrients such as sunlight and air (with increased CO2 levels) makes it a desirable agent for CO2 sequestration. The primary goal of this project is the engineering of the sequestration of CO2 using the cultivation of the microalgae species <i>Chlorella vulgaris</i>. Secondary goals of the project are the exploration and development of valuable by-products of the cultivation and the determination of whether utilizing microalgae to capture CO2 could be integrated economically into an industrial facility.<p> The batch growth kinetics of the photosynthetic algal species <i>C. vulgaris</i> were investigated using a well-mixed stirred bioreactor. The growth rate was found to increase as the dissolved CO2 increased to 150 mg/L (10% CO2 by volume in the gas), but fell dramatically at higher concentrations. Increasing the radiant flux also increased growth rate. With a radiant flux of 32.3 mW falling directly on the 500 mL culture media, the growth rate reached up to 3.6 mg of cells/L-h. Both pH variation (5.5 - 7.0) and mass transfer rate of CO2 (KLa between 6 h-1 and 17 h-1) had little effect on growth rate.<p> The operation of continuously stirred tank bioreactors (CSTBs) at minimum cost is a major concern for operators. In this work, a CSTB design strategy is presented where impeller stirring speed and aeration rate are optimized to meet the oxygen demand of growing cells, simultaneously minimizing the capital and operating cost. The effect of microbial species, ions in the culture medium, impeller style, as well as changing CSTB size and biomass input density on the optimum operating conditions, is examined. A study of the effects of various parameters on the CSTB design is shown.<p> Using the kinetic data collected in the batch growth study, a novel external loop airlift photobioreactor (ELAPB) was designed and tested. A model was developed for <i>C. vulgaris</i> growth in the ELAPB that incorporated growth behaviour, light attenuation, mass transfer, and fluid dynamics. The model predicts biomass accumulation, light penetration, and transient CO2 concentrations, and compares predictions to experimental data for radiant fluxes of 0.075 1.15 W/m2 and 0 20% CO2 enrichment of feed air, with a 10% average error. The effect of radiant flux and CO2 concentration is presented with discussion of radial and vertical profiles along the column. For a fed-batch culture at a biomass density of 170 mg/L, the penetration of the radiant flux was found to decrease by 50% within the first 1 cm, and 75% at 2 cm. Theoretical optimum growth conditions are determined to be 0.30 W/m2 and 6% CO2 enrichment of inlet feed air.<p> The algal culture was observed to be a workable electron acceptor in a cathodic half cell. A net potential difference of 70 mV was achieved between the growing <i>C. vulgaris</i> culture acting as a cathode and a 0.02 M potassium ferrocyanide anodic half cell. Surge current and power levels of 1.0 µA/mg of cell dry weight and 2.7 mW/m2 of cathode surface area were measured between these two half cells. The recently developed photosynthetic cathode was also coupled to a fermentative anode to produce a completely microbial fuel cell. Loading effects and the effect of changing culture conditions on fuel cell operation are reported. The maximum power output measured was 0.95 mW/ m2 at 90 V and 5000 ohms. A significant increase in this output is achieved with the addition of supplemental glucose to the anodic half cell and the enrichment of the feed air bubbled into the cathodic half cell with 10% CO2.<p> Two economic feasibility studies were performed on the integration of ELAPBs into an industrial facility. These integration studies operated the ELAPBs continuously as biocathodes in coupled microbial fuel cells (MFCs) that capture CO2 from an existing 130 million L/yr bioethanol plant, while generating electrical power and yielding oil for biodiesel to provide operational revenue to offset costs. The anodes for the coupled MFCs are the existing yeast batch fermentors, and the CO2 to be sequestered comes from the existing bioethanol production. Two different design schemes were evaluated, in both cases the maximum profit was achieved with the maximum number of tall columns operated in parallel. The first design evaluated a batch bioethanol facility with off-site oil processing, and the economic feasibility is demonstrated by the positive Net Present Worth achieved over the 20 year life of the plant, at a 10% rate of return on investment. The second design, for a continuous bioethanol operation, processes both oil and algae biomass on-site, but the economics of this second process are only positive (Internal Rate of Return 9.93%.) if the government provides financial assistance in the form of generous carbon credits (a speculative $100 per tonne of CO2 not yet attained) and a 25% capital equipment grant.

The use of microalgae culture to convert CO2 from power plant flue gases into biomass that are readily converted into biofuels offers a new frame of opportunities to enhance, compliment or replace fossil-fuel-use. Apart from being renewable, microalgae also have the capacity to utilise materials from a variety of wastewater and the ability to yield both liquid and gaseous biofuels. However, the processes of cultivation, incorporation of a production system for power plant waste flue gas use, algae harvesting, and oil extraction from the biomass have many challenges. Using SimaPro software, Life cycle Assessment (LCA) of the challenges limiting the microalgae (Chlorella vulgaris) biofuel production process was performed to study algae-based pathway for producing biofuels. Attention was paid to material use, energy consumed and the environmental burdens associated with the production processes. The goal was to determine the weak spots within the production system and identify changes in particular data-set that can lead to and lower material use, energy consumption and lower environmental impacts than the baseline microalgae biofuel production system. The analysis considered a hypothetical transesterification and Anaerobic Digestion (AD) transformation of algae-to- biofuel process. Life cycle Inventory (LCI) characterisation results of the baseline biodiesel (BD) transesterification scenario indicates that heating to get the biomass to 90% DWB accounts for 64% of the total input energy, while electrical energy and fertilizer obligations represents 19% and 16% respectively. Also, Life Cycle Impact Assessment (LCIA) results of the baseline BD production scenario show high proportional contribution of electricity and heat energy obligations for most impact categories considered relative to other resources. This is attributed to the concentration/drying requirement of algae biomass in order to ease downstream processes of lipid extraction and subsequent transesterification of extracted lipids into BD. Thus, four prospective alternative production scenarios were successfully characterised to evaluate the extent of their impact scenarios on the production system with regards to lowering material use, lower energy consumption and lower environmental burdens than the standard algae biofuel production system. A 55.3% reduction in mineral use obligation was evaluated as the most significant impact reduction due to the integration of 100% recycling of production harvest water for the AD production system. Recycling also saw water demand reduced from 3726 kg (freshwater).kgBD- 1 to 591kg (freshwater).kgBD- 1 after accounting for evaporative losses/biomass drying for the BD transesterification production process. Also, the use of wastewater/sea water as alternative growth media for the BD production system, indicated potential savings of: 4.2 MJ (11.8%) in electricity/heat obligation, 10.7% reductions for climate change impact, and 87% offset in mineral use requirement relative to the baseline production system. Likewise, LCIA characterisation comparison results comparing the baseline production scenarios with that of a set-up with co-product economic allocation consideration show very interesting outcomes. Indicating -12 MJ surplus (-33%) reductions for fossil fuels resource use impact category, 52.7% impact reductions for mineral use impact and 56.6% reductions for land use impact categories relative to the baseline BD production process model. These results show the importance of allocation consideration to LCA as a decision support tool. Overall, process improvements that are needed to optimise economic viability also improve the life cycle environmental impacts or sustainability of the production systems. Results obtained have been observed to agree reasonably with Monte Carlo sensitivity analysis, with the production scenario proposing the exploitation of wastewater/sea water to culture algae biomass offering the best result outcome. This study may have implications for additional resources such as production facility and its construction process, feedstock processing logistics and transport infrastructure which are excluded. Future LCA study will require extensive consideration of these additional resources such as: facility size and its construction, better engineering data for water transfer, combined heat and power plant efficiency estimates and the fate of long-term emissions such as organic nitrogen in the AD digestate. Conclusions were drawn and suggestions proffered for further study.