Microalgae are the principal primary producers of oxygen in the world and exhibit enormous potential for biotechnological industries. Microalgae cultivation is an efficient option for wastewater bioremediation, and these microorganisms are particularly efficient at recovering high levels of nitrogen, inorganic phosphorus, and heavy metals from effluent. Furthermore, microalgae are responsible for the reduction of CO2 from gaseous effluent and from the atmosphere. In general, the microalgae biomass can be used for the production of pigments, lipids, foods, and renewable energy .
Much of the biotechnological potential of microalgae is derived from the production of important compounds from their biomass. The biodiversity of the compounds derived from these microorganisms permits the development of new research and future technological advances that will produce as yet unknown benefits .
Microalgae grow in open systems (turf scrubber system, raceways, and tanks) and in closed systems (vertical (bubble column) or horizontal tubular photobioreactors, flat panels, biocoils, and bags). The closed systems favor the efficient control of the growth of these microorganisms because they allow for improved monitoring of the growth parameters [3-4].
Because microalgae contain a large amount of lipids, another important application of microalgae is biodiesel production . In addition, after hydrolysis, the residual biomass can potentially be used for bioethanol production . These options for microalgae uses are promising for reducing the environmental impact of a number of industries; however, there is a need for optimizing a number of parameters, such as increasing the lipid fraction and the availability of nutrients .
The productivity per unit area of microalgae is high compared to conventional processes for the production of raw materials for biofuels, and microalgae represent an important reserve of oil, carbohydrates, proteins, and other cellular substances that can be technologically exploited [2,11]. According to Brown
An advantage of culturing algae is that the application of pesticides is not required. Furthermore, after the extraction of the oil, by-products, such as proteins and the residual biomass, can be used as fertilizer . Alternatively, the residual biomass can be fermented to produce bioethanol and biomethane . Other applications include burning the biomass to produce energy .
The cultivation of microalgae does not compete with other cropsfor space in agricultural areas, which immediately excludes them from the "biofuels versus food" controversy. Similar to other oil crops, microalgae exhibit a high oil productivity potential, which can reach up to 100,000 L he-1. This productivity is excellent compared to more productive crops, such as palm, which yield 5,959 L he-1 and thus contribute to the alleviation of the environmental and economic problems associated with this industry.
Although the productivity of microalgae for biofuel production is lower than traditional methods, there is increasing interest and initiatives regarding the potential production of microalgae in conjunction with wastewater treatment, and a number of experts favor this option for microalgae production as the most plausible for commercial application in the short term .
2. Wastewater microalgae production
Photosynthetic microorganisms use pollutants as nutritional resources and grow in accordance with environmental conditions, such as light, temperature, pH, salinity, and the presence of inhibitors . The eutrophication process (increases in nitrogen and inorganic phosphorus) of water can be used as a biological treatment when the microalgae grow in a controlled system. Furthermore, these microorganisms facilitate the removal of heavy metals and other organic contaminants from water [19-22].
In general, the use of microalgae can be combined with other treatment processes or as an additional step in the process to increase efficiency. Therefore, microalgae are an option for wastewater treatments that use processes such as oxidation , coagulation and flocculation , filtration , ozonation , chlorination , and reverse osmosis , among others. Treatments using these methods separately often prove efficient for the removal of pollutants; however, methods that are more practical, environmentally friendly, and produce less waste are desirable. In this case, the combination of traditional methods with microalgae bioremediation is promising . The bioremediation process promoted by open systems, such as high rate algal ponds, combines microalgae production with wastewater treatment. In addition, the control of microalgae species, parasites, and natural biofloculation is important for cost reduction during the production of the microorganism [20, 30].
Many microalgae species grow under inhospitable conditions and present several possibilities for wastewater treatments. All microalgae production generates biomass, which must be used in a suitable manner [31-32].
Microalgae are typically cultivated in photobioreactors, such as open systems (turf scrubbers, open ponds, raceway ponds, and tanks) or closed system (tubular photobioreactors, flat panels, and coil systems). The closed systems allow for increased control of the environmental variables and are more effective at controlling the growth conditions. Therefore, the specific cultivation and input of CO2 are more successful. However, open systems can be more efficient when using wastewater, and low energy costs are achieved for many microalgae species grown in effluents in open systems [33-35]. Because of the necessity for renewable energy and the constant search for efficient wastewater treatment systems at a low cost, the use of microalgae offers a system that combines wastewater bioremediation, CO2 recovery, and biofuel production.
In turf scrubber systems, high rates of nutrient (phosphorus and nitrogen) removal are observed. This phenomenon was observed in the biomass retained in the prototype turf scrubber system used in three rivers in Chesapeake Bay, USA. The time of year was crucial for the bioremediation of excess nutrients in the river water, and the best results demonstrated the removal of 65% of the total nitrogen and up to 55% of the total phosphorus, both of which were fixed in the biomass .
Compared to other systems, such as tanks and photobioreactors (Fig. 2), the algae turf scrubber system is an alternative for the final treatment of wastewater. The turf scrubber system offers numerous advantageous characteristics, such as temperature control in regions with high solar incidence and the development of a microorganism community using microalgae, other bacteria, and fungi that promote nutrient removal. Under these conditions, it is possible to obtain biomass with the potential for producing biofuels. However, sufficient levels of oil in the biomass are an important consideration for the production of other biofuels, such as bioethanol, bio-oil, and biogas, among others, which would achieve the complete exploitation of the biomass.
Considering the possibility of using all the biomass, photobioreactors can be used to produce feedstock for biofuel, such as biodiesel and bioethanol, because the oil level of the biomass produced in closed systems is greater than in open systems. Table 1 shows the results obtained using a mixed system and a similar tubular photobioreactor with microalgae
|Maximum Cell Division (x106 cell mL-1)||25.48 ± 0.02||26.97 ± 0.21||8.49 ± 1.02||25.98± 1.57|
|Average Cell Division (K)||0.29 ± 0.48||0.16 ± 0.33||-0.12 ± 0.60||0.34 ± 0.40|
|Biomass (g L-1)||0.62 ± 0.11||0.72 ± 0.15||0.18 ± 5.65||1.41 ± 1.40|
|Lipids (%)||1.36 ± 0.29||6.07 ± 0.12||18.73 ± 0.25||12.00 ± 0.28|
The removal of nutrients from the effluent produced excellent results using the genus
The cultivation of the diatom
The cultivation of microalgae
Therefore, microalgae can produce 3-10 times more energy per hectare than other land cultures and are associated with CO2 mitigation and wastewater depollution . Microalgae production is a promising alternative to land plants for reducing environmental impacts; however, the optimization of a number of the production parameters that are important for the viability of the process must be considered, such as the increase in lipid production .
The bioremediation of wastewater using microalgae is a promising option because it reduces the application of the chemical compounds required in conventional mechanical methods, such as centrifugation, gravity settling, flotation, and tangential filtration .
The feasibility of using microalgae for bioremediation is directly related to the production of biofuels because of the high oil content. Without the high oil levels, using other bacteria for this purpose would be more advantageous because there are limitations to the removal of organic matter by microalgae. In the literature, emphasis is placed on the ability of microalgae to remove heavy metals from industrial effluents .
The term biofuel refers to solid, liquid, or gaseous fuels derived from renewable raw materials. The use of microalgal biomass for the production of energy involves the same procedures used for terrestrial biomass. Among the factors that influence the choice of the conversion process are the type and amount of raw material biomass, the type of energy desired, and the desired economic return from the product .
Microalgae have been investigated for the production of numerous biofuels including biodiesel, which is obtained by the extraction and transformation of the lipid material, bioethanol, which is produced from the sugars, starch, and carbohydrate residues in general, biogas, and bio-hydrogen, among others (Fig. 3) .
Between 1978 and 1996, the Office of Fuels Development at the U.S. Department of Energy developed extensive research programs to produce renewable fuels from algae. The main objective of the program, known as The Aquatic Species Program (ASP), was to produce biodiesel from algae with a high lipid content grown in tanks that utilize CO2 waste from coal-based power plants. After nearly two decades, many advances have been made in manipulating the metabolism of algae and the engineering of microalgae production systems. The study included consideration of the production of fuels, such as methane gas, ethanol and biodiesel, and the direct burning of the algal biomass to produce steam or electricity .
The choice of raw material is a critical factor contributing to the final cost of biodiesel andaccounts for 50-85% of the total cost of the fuel. Therefore, to minimize the cost of this biofuel, it is important to assess the raw material in terms of yield, quality, and the utilization of the by-products [49-50].
A positive aspect of the production of biodiesel from microalgae is the area of land needed for production. For example, to supply 50% of the fuel used by the transportation sector in the U.S. using palm oil, which is derived from a plant with a high oil yield per hectare, would require 24% of the total agricultural area available in the country. In contrast, if the oil from microalgae grown in photobioreactors was used, it would require only 1-3% of the total cultivation area .
The biochemical composition of the algal biomass can be manipulated through variations in the growth conditions, which can significantly alter the oil content and composition of the microorganism . Biodiesel produced from microalgae has a fatty acid composition (14 to 22 carbon atoms) that is similar to the vegetable oils used for biodiesel production [51-52].
The biodiesel produced from microalgae contains unsaturated fatty acids , and when the biomass is obtained from wastewater and is composed of a mixture of microalgae genera, it can exhibit various fatty acids profiles. Bjerk  produced biodiesel using a mixed system containing the microalgae genera
In this mixed system, a difference between the fatty acid profiles of the biomass obtained in the photobioreactor compared to the biomass obtained on the screen was observed. The biomass from the screen contained the filamentous algae genera, and the oil did not contain linoleic acid.
This observation is important for biodiesel production because the oil produced was less unsaturated. The iodine index reflects this trend; oils from species such as
The composition and proportion of fatty acids in the microalgae oil depends on the species used, the nutritional composition of the medium, and other cultivation conditions .
Table 4 shows the microalgae commonly used for oil production. The literature lacks information regarding the iodine index or the composition of saturated and unsaturated fatty acids, which could help identify the appropriate microalgae species for biodiesel production. Information on numerous parameters is important, such as the oil unsaturation levels, the productivity of the microalgae in the respective effluents, the growth rate, and the total biomass composition. Using this information, a decision can be made regarding the economic and environmental feasibility of producing biodiesel and adequately allocating the waste.
|Linoleic (C 18:2)||15.12||9.51||-|
|Oleic (C 18:1n-9)||26.60||39.94||20.19|
|Estearic (C 18:0)||9.75||9.69||12.16|
|Araquidic (C 20:0)||0.70||1.43||1.72|
|Saturated and unsaturated not identified**||13.6||9.97||25.84|
Among the microalgae shown in Table 4 that have an oil content that makes them competitive with land crops, twelve species (
Bioethanol production from microalgae has received remarkable attention because of the high photosynthetic rates, the large biodiversity and variability of their biochemical composition, and the rapid biomass production exhibited by these microorganisms .
Furthermore, bioethanol derived from microalgae biomass is an option that demonstrates the greatest potential. John
Traditionally, bioethanol is produced through the fermentation of sugar and starch, which are produced from different sources, such as sugarcane, maize, or a number of other grains .
After the oil extraction, the residual biomass contains carbohydrates that can be used for bioethanol production. This process represents a second-generation bioethanol and may be an alternative to the sugar cane ethanol produced in Brazil and corn or beet ethanol produced in other countries. The process requires pretreatment with a hydrolysis step before fermentation [63-65].
In bioethanol production, the processes vary depending on the type of biomass and involve the pretreatment of the biomass, saccharification, fermentation, and recovery of the product. The pretreatment of the biomass is a critical process because it is essential for the formation of the sugars used in the fermentation process (Table 5). Before the traditional fermentation process, acid hydrolysis is widely used for the conversion of carbohydrates from the cell wall into simple sugars. The acid pretreatment is efficient and involves low energy consumption .
Other techniques, such as enzymatic digestion  or gamma radiation , are interesting alternatives for increasing the chemical hydrolysis to render it more sustainable. Through analysis of the process in terms of energy, mass, and residue generation, it is possible to determine the best route. With enzymatic hydrolysis, the process can be renewable. Another technique for pretreatment of the biomass is hydrolysis mediated by fungi. Bjerk  investigated the
However, it is worth noting the importance of developing a well-designed and efficient system for the cultivation of these microorganisms, which can remove compounds that cause impurities in the final product. In addition, more studies should be undertaken to select strains that are resistant to adverse conditions, especially studies related to genetic engineering.
According to Yoon
3.3. Other biofuels
Several articles describe the thermochemical processing of algal biomass using gasification [63,76] liquefaction , pyrolysis , hydrogenation , and biochemical processing, such as fermentation [80-81]. However, engineering processes have not been investigated as a potential biotechnological method for the production of other biofuels from microalgae.
Currently, the energy derived from biomass is considered one of the best energy sources and can be converted into various forms depending on the need and the technology used, and biogas is chief among the forms of energy produced by biomass. .
Anaerobic digestion for biogas production is a promising energy route because it provides numerous environmental benefits. Biogas is produced through the anaerobic digestion of organic waste, drastically reducing the emission of greenhouse gases. As an added benefit, the by-products of fermentation, which are rich in nutrients, can be recycled for agricultural purposes. Adding anaerobic digestion to the use of biomass waste from which the oil has been removed produces an environmental gain and results in the complete exhaustion of the possible uses for the biomass. This strategy enables biomass waste to be an end-of-pipe technology for industrial processes that generate high amounts of organic matter containing phosphorus and nitrogen. A proposed system for this purpose is shown in Figure 4, which represents a simplification of the work performed by Chen
Therefore, using the residual microalgae biomass as a source of biogas is similar to other agricultural residue uses  in which the organic substrate is converted into biogas through anaerobic digestion, producing a gas mixture containing a higher percentage of carbon dioxide and methane .
The use of microalgae for biomethane production is significant because fermentation exhibits high stability and high conversion rates, which makes the process of bioenergy production more economically viable. For example, Feinberg (1984) (cited in Harun
When considering total biomass use, in addition to biogas, it is possible to produce biohydrogen and bio-oils using enzymatic and chemical processes.
The chemical processes that can be used for hydrogen production include gasification, partial oxidation of oil, and water electrolysis. In the literature, cyanobacteria are primarily used for the production of biohydrogen through a biological method, and the reaction is catalyzed by nitrogenases and hydrogenases . Studies with
Bio-oil can be produced from any biomass, and for microalgae, a number of investigations have been performed using
These initiatives highlight the potential use of hydrothermal liquefaction, which is a process that converts the biomass into bio-oil at a temperature range of 200-350°C and pressures of 15-20 MPa. According to Biller et al. , yields of 27-47% are possible, taking into account that microalgae can be produced using recycled nutrients, providing greater sustainability to the system.
A different bio-oil can be produced using pyrolysis in which the oil composition features compounds exhibiting boiling points lower than the hydrothermal liquefaction product . In pyrolysis, the nitrogen content of the microalgae is converted into NOx during combustion. NOx is an undesirable emission that increases depending on the microalgae and their protein content; however, NOx emissions can be reduced by 42% using a hydrothermal pre-treatment process.
In terms of waste recovery, the use of
Therefore, in addition to producing microalgae in urban or industrial effluents, it is possible that after the extraction of the oil for biodiesel production and the production of bioethanol from carbohydrates, biogas or bio-oil can be produced from the waste material.
This chapter reviews the initiatives for biofuel production from microalgae cultivated in wastewaters. The exploitation of the total microalgae biomass was considered, and the potential for biodiesel and bioethanol production was explored.
The various systems for microalgae production using wastewater and the consequences for biodiesel and bioethanol production were discussed in detail.
Microalgae have been used to produce biodiesel and bioethanol with excellent results; however, the use of microalgae must be expanded to include bioremediation combined with biofuel production. The commercial initiatives for this purpose will depend on the composition and volume of the effluent, on the selected microalgae species, and on the temperature and light conditions of the region. The initiatives will also depend on the particular biofuel of interest to the region or that required for local consumption. Therefore, each situation must be analyzed on an individual basis, and there is no single model; however, because of the wide biodiversity of microalgae and the extensive ongoing research capacity of many countries, it is likely that a conditions for viable microalgae production can be achieved anywhere.
Finally, it should be noted that microalgae that are adapted to the environment could produce biomass that, depending on the composition of cells, can be used as the raw material for the production of one or more biofuels.
The research and development of microalgae production in urban or industrial effluents involve principles of sustainable development, clean technology, and the ecology of the productive sectors, prioritizing preventive and remediation steps with the decreased use of energy and inputs. Therefore, there is an emphasis on the methods of treatment, the transformation processes, and the biotechnological products (biofuels), prioritizing the use of wastewater for biomass and bioenergy production. These developments will decrease the impact on activities of anthropogenic origin from the industrial, commercial and service sectors, among others.
The National Council of Technological and Scientific Development (Conselho Nacional de Desenvolvimento Científico e Tecnológico, CNPq), the National Council for the Improvement of Higher Education (Coordenação de Aperfeiçoamento de Pessoal de Nível Superior, CAPES) and the University of Santa Cruz do Sul Research Foundation (Fundo de Apoio à Pesquisa da Universidade de Santa Cruz do Sul, FAP/UNISC)
Derner, R. B. et al. Microalgae, products and applications (Microalgas, produtos e aplicações). Ciência Rural 2006; 36(6) 1959-1967. http://dx.doi.org/10.1590/S0103-84782006000600050
Richmond, A. Handbook of microalgal culture: biotechnology and applied phycology. Oxford: Blackwell Science, 2004.
Borowitzka, M. A. Commercial production of microalgae: ponds, tanks, tubes and fermenters. Journal of Biotechnology1999; 70,(1-3) 313-321. http://dx.doi.org/ 10.1016/S0168-1656(99)00083-8
Gressler, P., Schneider, R. C S., Corbellini, V. A., Bjerk T., Souza M. P., Zappe A., Lobo, E. A. Microalgas: aplicações em biorremediação e energia. In English: Microalgae: Aplications in bioremediation na energy. Caderno de Pesquisa, Série Biologia, 2012; 24, 1, 48-67. www.bioline.org.br/pdf?cp12004.
Chisti, Y. Biodiesel from microalgae. Biotechnology Advances, v. 25, n. 3, p. 294-306, http://dx.doi.org/10.1016/j.biotechadv.2007.02.001, 2007.
Harun, R. et al. Microalgal biomass as a cellulosic fermentation feedstock for bioethanol production. Renewable and Sustainable Energy Reviews 2010. http://dx.doi.org/10.1016/j.rser.2010.07.071
Jiang, L. et al. Biomass and lipid production of marine microalgae using municipal wastewater and high concentration of CO2. Applied Energy 2011; 88(10) 3336-3341. http://dx.doi.org/ 10.1016/j.apenergy.2011.03.043
Demirbas, M. F. Biofuels from algae for sustainable development. Applied Energy 2011;88(10) 3473-3480. http://dx.doi.org/10.1016/j.apenergy.2011.01.059
Marques A. E. et al. Biohydrogen production by Anabaena sp. PCC 7120 wild-type and mutants under different conditions: Light, nickel, propane, carbon dioxide and nitrogen. Biomass and Bioenergy 2011;35(10) 4426-4434. http://dx.doi.org/10.1016/j.biombioe.2011.08.014
Shuping, Z. et al. Production and characterization of bio-oil from hydrothermal liquefaction of microalgae Dunaliella tertiolectacake. Energy 2010; 35(12) 5406-5411. http://dx.doi.org/10.1016/j.energy.2010.07.013,
Lopes, E. J. Carbon dioxide sequestration in photobioreactors (Seqüestro de dióxido de carbono em fotobiorreatores). 2007. Thesis. Graduate Program in Chemical Engineering (Programa de Pós-Graduação: Engenharia Química-Mestrado e Doutorado) – School of Chemical Engineering at Campinas State University (Faculdade de Engenharia Química da Universidade Estadual de Campinas), Campinas, 2007.
Brown, M. R. et al. Nutritional aspects of microalgae used in mariculture. Aquaculture 1997;151(1-4) 315-331. http://dx.doi.org/10.1016/S0044-8486(96)01501-3
Spolaore, P. et al. Commercial applications of microalgae. Journal of Bioscience and Bioengineering 2006;101(2) 87-96. http://dx.doi.org/10.1263/jbb.101.87
Hirano, A. et al. Temperature effect on continuous gasiﬁcation of microalgal biomass: theoretical yield of methanol production and its energy balance. Catalysis Today 1998; 45 (1–4) 399–404. http://dx.doi.org/10.1016/S0920-5861(98)00275-2.
Chen C. et al. Thermogravimetric analysis of microalgae combustion under different oxygen supply concentrations. Applied Energy 2011;88(9) 3189-3196.http://dx.doi.org/10.1016/j.apenergy.2011.03.003
Demirbas, A, FatihDemirbas, M. Importance of algae oil as a source of biodiesel. Energy Conversion and Management 2011;52(1)163-170. http://dx.doi.org/10.1016/j.enconman.2010.06.055
Harmelen, Van T, Oonk H. Microalgae bioﬁxation processes: applications and potential contributions to greenhouse gas mitigation options.TNO:Eni Tecnologie;2006. http://www.fluxfarm.com/uploads/3/1/6/8/3168871/biofixation.pdf (accessed 18 July 2012).
Farhadian, M. et al. In situ bioremediation of monoaromatic pollutants in groundwater: a review. Bioresource Technology 2008;99(13) 5296-308. http://dx.doi.org/10.1016/j.biortech.2007.10.025,
Bashan, L. E. e Bashan, Y. Immobilized microalgae for removing pollutants: review of practical aspects. Bioresource Technology 2010;101(6) 1611-27. http://dx.doi.org/10.1016/j.biortech.2009.09.043,
Park, J. B. K. et al. Wastewater treatment high rate algal ponds for biofuel production. Bioresource Technology 2011;102(1) 35-42. http://dx.doi.org/10.1016/j.biortech.2010.06.158
Christenson, L, Sims, R. Production and harvesting of microalgae for wastewater treatment, biofuels, and bioproducts. Biotechnology Advances 2011;29(6) 686-702. http://dx.doi.org/10.1016/j.biotechadv.2011.05.015.
Gattullo, C. E. et al. Removal of bisphenol A by the freshwater green alga Monoraphidiumbraunii and the role of natural organic matter. The Science of the Total Environment 2012; 416, 501-506. http://dx.doi.org/10.1016/j.biotechadv.2011.05.015
Masroor, M. et al. An Overview of the Integration of Advanced Oxidation Technologies and Other Processes for Water and Wastewater Treatment. International Journal of Engineering 2009;3(2)120-146.
Fuchs, W. et al. Influence of standard wastewater parameters and pre-flocculation on the fouling capacity during dead end membrane filtration of wastewater treatment effluents. Separation and Purification Technology2006;52(1)46-52. http://dx.doi.org/10.1016/j.seppur.2006.03.013.
Chang, I.-S, Kim, S.-N. Wastewater treatment using membrane filtration—effect of biosolids concentration on cake resistance. Process Biochemistry 2005; 40(3-4) 1307-1314. http://dx.doi.org/10.1016/j.procbio.2004.06.019
Almeida, E. et al. Industrial effluent treatment via oxidation in the presence of ozone. (Tratamento de efluentes industriais por processos oxidativos na presença de ozônio.) Quim. Nova 2004; 279(5) 818-824. http://dx.doi.org/10.1590/S0100-40422004000500023
Daly, R. I. et al. Effect of chlorination on Microcystisaeruginosa cell integrity and subsequent microcystin release and degradation. Environmental Science & Technology 2007;41(12) 4447-4453.
Caron, D. A et al. Harmful algae and their potential impacts on desalination operations off southern California. Water research 2010,44;(2) 385-416. http://dx.doi.org/10.1016/j.watres.2009.06.051, 2010
Chinnasamy S, Bhatnagar A, Claxton R,. Biomass and bioenergy production potential of microalgae consortium in open and closed bioreactors using untreated carpet industry effluent as growth médium. Bioresource Technology 2010;101(17) 6751–6760. http://dx.doi.org/doi:10.1016/j.biortech.2010.03.094
Brennan, L, Owende, P. Biofuels from microalgae—A review of technologies for production, processing, and extractions of biofuels and co-products. Renewable and Sustainable Energy Reviews 2010;(14)2 557-577. http://dx.doi.org/10.1016/j.rser.2009.10.009
Pittman, J. K. et al. The potential of sustainable algal biofuel production using wastewater resources. Bioresource Technology 2010;102(1) 17-25. http://dx.doi.org/10.1016/j.biortech.2010.06.035
Mulbry, W. et al. Toward scrubbing the bay: Nutrient removal using small algal turf scrubbers on Chesapeake Bay tributaries. Ecological Engineering 2010;36(4), 536-541. http://dx.doi.org/10.1016/j.ecoleng.2009.11.026
Chiu, S.-Y. et al. Reduction of CO2 by a high-density culture of Chlorella sp. in a semicontinuousphotobioreactor. Bioresource Technology 2008;99(9) 3389-3396. http://dx.doi.org/10.1016/j.biortech.2007.08.013
Chiu, S.-Y. et al. The air-lift photobioreactors with flow patterning for high-density cultures of microalgae and carbon dioxide removal. Engineering in Life Sciences 2009;9(3) 254-260. http://dx.doi.org/10.1002/elsc.200800113
Muñoz, R. et al. Biofilm photobioreactors for the treatment of industrial wastewaters. Journal of Hazardous Materials 2009;161(1) 29-34. http://dx.doi.org/10.1016/j.jhazmat.2008.03.018
Bjerk, T. R. Microalgae cultive in fotobiorreator and joint reactor objectiving the bioremediation and production of biofuels (In Portuguese: Cultivo de microalgasemfotobiorreator e reatormistovisando a biorremediação e produção de biocombustíveis). Universidade de Santa Cruz do Sul, Santa Cruz do Sul-Rio Grande do Sul. 2012.
Gressler, P. D. Efficiency Evaluation of the Desmodesmus subspicatus (R. Chodat) E. Hegewald & A. Schmidt (Chlorophyceae) to grown in tubular photobioreactor with effluent from ETE-Unisc for bioremediation and energy generation (In Portuguese: Avaliação da eficiência de Desmodesmus subspicatus (R. Chodat) E. Hegewald & A. Schmidt (Chlorophyceae) cultivada em Fotobiorreator tubular com efluente da ETE-unisc, visando biorremediação e obtenção de energia). Universidade de Santa Cruz do Sul, Santa Cruz do Sul-Rio Grande do Sul. 2011.
Ai, W. et al. Development of a ground-based space micro-algae photo-bioreactor. Advances in Space Research2008;41(5) 742–747. http://dx.doi.org/10.1016/j.asr.2007.06.060.
Krichnavaruk, S. et al. Optimal growth conditions and the cultivation of Chaetoceroscalcitrans in airlift photobioreactor. Chemical Engineering Journal 2005;105(3) 91-98. http://dx.doi.org/10.1016/j.cej.2004.10.002
Vasumathi K.K. et al. Parameters influencing the design of photobioreactor for the growth of microalgae. Renewable and Sustainable Energy Reviews 2012;16(7) 5443-5450. http://dx.doi.org/10.1016/j.rser.2012.06.013
Demirbas, A. Use of algae as biofuel sources. Energy Conversion and Management 2010; 51(12) 2738-2749. http://dx.doi.org/10.1016/j.enconman.2010.06.010.
Xin, L. et al. Lipid accumulation and nutrient removal properties of a newly isolated freshwater microalga, Scenedesmus sp. LX1, growing in secondary effluent. New Biotechnology 2010;27(1) 59-63. http://dx.doi.org/10.1016/j.nbt.2009.11.006
Fierro, S. et al. Nitrate and phosphate removal by chitosan immobilized Scenedesmus. Bioresource Technology 2008;99(5) 1274-1279. http://dx.doi.org/10.1016/j.biortech.2007.02.043
Wu L,F. et al. The feasibility of biodiesel production by microalgae using industrial wastewater. Bioresource Technology 2012, 113 :14-18 .
Ruiz-Marin, A. et al. Growth and nutrient removal in free and immobilized green algae in batch and semi-continuous cultures treating real wastewater. Bioresource Technology 2010;101(1) 58-64. http://dx.doi.org/10.1016/j.biortech.2009.02.076
Martínez, M. E. et al. Nitrogen and phosphorus removal from urban wastewater by the microalga Scenedesmusobliquus. Bioresource Technology 2000;73(3) 263-272. http://dx.doi.org/10.1016/S0960-8524(99)00121-2
Harun R. et al. Bioprocess engineering of microalgae to produce a variety of consumer products. Renewable and Sustainable Energy Reviews 2010; 14(3) 1037–1047. http://dx.doi.org/10.1016/j.rser.2009.11.004.
Sheehan, J. et al. A Look Back at the US Department of Energy’s Aquatic Species Program: biodiesel from algae. US Department of Energy’s, Office of Fuels development: NREL/TP-580-24190.1998. http://www.nrel.gov/docs/legosti/fy98/24190.pdf (accessed 01 august 2012).
Soares, D. Assessmentof cell growthand lipids productivity ofmarine microalgaein differentcroppingsystems (In Portuguese: Avaliação do crescimentocelular e da produtividade de lipideos de microalgasmarinhasemdiferentes regimes de cultivo. 2010). 107 f. Thesis. Graduate Program in Biochemical Sciences. (Curso de Pós-Graduação em Ciências: Bioquímica – Mestrado e Doutorado) – Federal University of Parana (Universidade Federal do Paraná), Curitiba, 2010.
Song, D. et al. Exploitation of oil-bearing microalgae for biodiesel. Chinese Journal of Biotechnology 2008; 24(3) 341-348. http://dx.doi.org/10.1016/S1872-2075(08)60016-3
Qin J. Bio-hydrocarbons from algae—impacts of temperature, light and salinity on algae growth. Barton, Australia: Rural Industries Research and Development Corporation; 2005.
MATA, T. M. et al. Microalgae for biodiesel production and other applications: A review. Renewable and Sustainable Energy Reviews2010;14(1) 217-232. http://dx.doi.org/10.1016/j.rser.2009.07.020
Radmann, E. M., Costa, J. A. V. Lipid content and fatty acid composition of microalgae exposed to CO2, SO2 and NO (Conteúdo lipídico e composição de ácidos graxos de microalgas expostas aos gases CO2, SO2 e NO). Química Nova 2008;31(7) 1609–1612. http://dx.doi.org/10.1590/S0100-40422008000700002.
Bicudo, C., E., M., Menezes, M. Genus of algae from inland waters of Brazil, identification and description key (Gênero de algas de águas continentais do Brasil, chave para identificação e descrição). 2. ed. São Carlos-SP: RIMA, 2006.
Porte A. F, Schneider R. C. S, Kaercher J. A, Klamt R. A, Schmatz W. L, Silva W. L. T, Filho W. A. S. Sunﬂower biodiesel production and application in family farms in Brazil. Fuel 2010; 89(12) 3718–3724. http://dx.doi.org/10.1016/j.fuel.2010.07.025.
Gouveia L, Oliveira A. C. Microalgae as a raw material for biofuels Production. J IndMicrobiolBiotechnol 2009;36 269–274. http://dx.doi.org/ 10.1007/s10295-008-0495-6.
Guschina, I. A , Harwood, J. L. Lipids and lipid metabolism in eukaryotic algae. Progress in Lipid Research 2006;45(2) 160-186. http://dx.doi.org/ 10.1016/j.plipres.2006.01.001, 2006.
Doan, T. T. Y. et al. Screening of marine microalgae for biodiesel feedstock. Biomass and Bioenergy 2011;35(7) 2534-2544. http://dx.doi.org/10.1016/j.biombioe.2011.02.021.
Khan, S. A. et al. Prospects of biodiesel production from microalgae in India. Renewable and Sustainable Energy Reviews 2009;13(9) 2361–2372. http://dx.doi.org/10.1016/j.rser.2009.04.005
Kaiwan-arporn P, Hai P. D, Thu N. T, Annachhatre A. P. Cultivation of cyanobacteria for extraction of lipids. Biomass and Bioenergy 2012; 44 142-149. http://dx.doi.org/10.1016/j.biombioe.2012.04.017
John R. P, Anisha G.S, Nampoothiri K. M, Pandey A. Micro and macroalgal biomass: A renewable source for bioethanol. Bioresource Technology2011; 102(1) 186-193.http://dx.doi.org/10.1016/j.biortech.2010.06.139
Harun, R, Danquah, M. K. Enzymatic hydrolysis of microalgae biomass for bioethanol production. Chemical Engineering Journal 2011b;168(3) 1079-1084. http://dx.doi.org/10.1016/j.cej.2011.01.088.
Harun, R, Danquah, M. K. Influence of acid pre-treatment on microalgal biomass for bioethanol production. Process Biochemistry 2011a;46(1) 304-309. http://dx.doi.org/10.1016/j.procbio.2010.08.027
Balat, M. Production of bioethanol from lignocellulosic materials via the biochemical pathway: A review. Energy Conversion and Management 2010;52(2) 858-875. http://dx.doi.org/10.1016/j.enconman.2010.08.013
Goh, C. S, Lee, K. T. A visionary and conceptual macroalgae-based third-generation bioethanol (TGB) biorefinery in Sabah, Malaysia. as an underlay for renewable and sustainable development. Renewable and Sustainable Energy Reviews 2010;14(2) 842-848. http://dx.doi.org/10.1016/j.rser.2009.10.001
Nguyen MT, Choi SP, Lee J, Lee JH, S. S. Hydrothermal acid pretreatment of Chlamydomonasreinhardtii biomass for ethanol production. J MicrobiolBiotechnol. 2009;19(2) 161-166. http://dx.doi.org/10.4014/jmb.0810.578
Harun, R., Jason, W. S. Y., Cherrington, T., &Danquah, M. K. Exploring alkaline pre-treatment of microalgal biomass for bioethanol production. Applied Energy 2010;88(10) 3464-3467. http://dx.doi.org/10.1016/j.apenergy.2010.10.048
Harun R, Liu B,Danquah M. K. Analysis of Process Configurations for Bioethanol Production from Microalgal Biomass. Progress in Biomass and Bioenergy Production:In Tech;2011. DOI: 10.5772/17468
Yazdani, P., Karimi, K., &Taherzadeh, M. J. Improvement of Enzymatic Hydrolysis of A Marine Macro-Alga by Dilute Acid Hydrolysis Pretreatment. Bioenergy Technology 2011, 186-191. . http://dx.doi.org/10.3384/ecp11057186
Khambhaty, Y., Mody, K., Gandhi, M. R., Thampy, S., Maiti, P., Brahmbhatt, H., Eswaran, K., et al. (). Kappaphycusalvarezii as a source of bioethanol. Bioresource Technology2012;103(1) 180-185. . http://dx.doi.org/10.1016/j.biortech.2011.10.015
Miranda, J. R., Passarinho, P. C., &Gouveia, L. Pre-treatment optimization of Scenedesmusobliquus microalga for bioethanol production. Bioresource Technology 2012;104 342-8. http://dx.doi.org/doi:10.1016/j.biortech.2011.10.059
Eshaq, F. S.; Ali, M. N.; Mohd, M. K. Spirogyra biomass a renewable source for biofuel (bioethanol) production. International Journal of Engineering Science and Technology 2010;2(12)7045-7054.
Mushlihah, S., Sunarto, E., Irvansyah, M. Y., &Utami, R. S. Ethanol Production from Algae Spirogyra with Fermentation by Zymomonasmobilis and Saccharomyces cerevisiae. J. Basic. Appl. Sci. Res 2011;1(7), 589-593.
Chen, R. et al. Use of an algal hydrolysate to improve enzymatic hydrolysis of lignocellulose. Bioresource Technology 2012;108(1) 149-154. http://dx.doi.org/10.1016/j.biortech.2011.12.143
Yoon, M. et al. Improvement of saccharification process for bioethanol production from Undaria sp. by gamma irradiation. Radiation Physics and Chemistry 2012;81(8) 999-1002. http://dx.doi.org/10.1016/j.radphyschem.2011.11.035
Elliott D.C., Sealock Jr. L.J., Chemical processing in high-pressure aqueous environments: Low temperature catalytic gasification. Chemical Engineering Research and Design 1996; 74( 5): 563-566.
Tsukahara K., Sawayama S. Liquid fuel production using microalgae. Jpn Petrol Inst 2005; 48(5) 251–259.
Miao X. et al. Fast pyrolysis of microalgae to produce renewable fuels. J Anal Appl Pyrolysis 2004; 71(2) 855–863.
Amin S. Review on biofuel oil and gas production processes from microalgae. Energy Conversion and Management 2009; 50(7) 1834-1840. http://dx.doi.org/10.1016/j.enconman.2009.03.001.
Bently J.; Derby R. Ethanol. fuel cells: converging paths of opportunity. RenewableFuelsAssociation 2008; http://www.ethanolrfa.org/objects/documents/129/rfa_fuel_cell_white_paper.pdf>. (Accessed 24 July, 2012.
Xu, H. et al. High quality biodiesel production from a microalga Chlorella protothecoides by heterotrophic growth in fermenters. Journal of Biotechnology 2006;126(4) 499–507. http://dx.doi.org/10.1016/j.jbiotec.2006.05.002
Converti, A. et al. Effect of temperature and nitrogen concentration on the growth and lipid content of Nannochloropsisoculata and Chlorella vulgaris for biodiesel production. Chemical Engineering and Processing: Process Intensification 2009;48(6) 1146-1151. http://dx.doi.org/10.1016/j.cep.2009.03.006
Chen S., Chen B., Song D. Life-cycle energy production and emissions mitigation by comprehensive biogas–digestate utilization Bioresource Technology 2012; 114: 357-364. http://dx.doi.org/10.1016/j.biortech.2012.03.084.
Ehimen E.A., Holm-Nielsen J.-B., Poulsen M., Boelsmand J.E. Influence of different pre-treatment routes on the anaerobic digestion of a filamentous algae. Renewable Energy 2013; 50: 476-480. http://dx.doi.org/10.1016/j.renene.2012.06.064.
Bernard, O. Hurdles and challenges for modelling and control of microalgae for CO2 mitigation and biofuel production. Journal of Process Control 2011; 21(10): 1378-1389. doi:10.1016/j.jprocont.2011.07.012
Abdel-Raouf N., Al-Homaidan A.A., Ibraheem I.B.M. Microalgae and wastewater treatment. Saudi Journal of Biological Sciences 2012; 19(3): 257-275. http://dx.doi.org/10.1016/j.sjbs.2012.04.005
Harun, R. et al. Technoeconomic analysis of an integrated microalgae photobioreactor, biodiesel and biogas production facility. Biomass and Bioenergy 2010; 35(1) 741-747. http://dx.doi.org/10.1016/j.biombioe.2010.10.007
Tamagnini P., Leitão E., Oliveira P., Ferreira D., Pinto F., Harris D., Cyanobacterial hydrogenases. Diversity, regulation and applications. FEMS Microbiol Rev 2007; 31:692-720.
Ferreira A.F., Marques A. C., Batista A.P., Marques P. A.S.S., Gouveia L., Silva C. M. Biological hydrogen production by Anabaena sp. e Yield,energy and CO2 analysis including fermentative biomass recovery. International Journal of Hydrogen Energy 2012; 37: 179 -190. doi:10.1016/j.ijhydene.2011.09.056
Bhatnagar A., Chinnasamy S., Singh M., Das K.C., Renewable biomass production by mixotrophic algae in the presence of various carbon sources and wastewaters. Applied Energy 2011; 88 (10): 3425-3431. http://dx.doi.org/10.1016/j.apenergy.2010.12.064
Biller P., Ross A.B., Skill S.C., Lea-Langton A., Balasundaram B., Hall C., Riley R., Llewellyn C.A. Nutrient recycling of aqueous phase for microalgae cultivation from the hydrothermal liquefaction process Algal Research 2012; 1: 70-76. http://dx.doi.org/10.1016/j.algal.2012.02.002
Tsukahara K., Kimura T., Minowa T., Sawayama S., Yagishita T., Inoue S., Hanaoka T., Usui Y., Ogi T., Microalgal cultivation in a solution recovered from the low-temperature catalytic gasification of the microalga. Journal of Bioscience and Bioengineering 2001; 91 (3) 311-313. http://dx.doi.org/10.1016/S1389-1723(01)80140-7
Du Z., Mohr M., Ma X., Cheng Y., Lin X., Liu Y., Zhou W., Chen P., Ruan R. Hydrothermal pretreatment of microalgae for production of pyrolytic bio-oil with a low nitrogen content. Bioresource Technology 2012; 120: 13-18 http://dx.doi.org/10.1016/j.biortech.2012.06.007.
Jena U., Vaidyanathan N., Chinnasamy S., Das K.C., Evaluation of microalgae cultivation using recovered aqueous co-product from thermochemical liquefaction of algal biomass, Bioresource Technology 2011; 102 (3): 3380–3387. doi:10.1016/j.biortech.2010.09.111