Sustainability is a key principle in natural resource management, and it involves operational efficiency, minimisation of environmental impact and socio-economic considerations; all of which are interdependent. It has become increasingly obvious that continued reliance on fossil fuel energy resources is unsustainable, owing to both depleting world reserves and the green house gas emissions associated with their use. Therefore, there are vigorous research initiatives aimed at developing alternative renewable and potentially carbon neutral solid, liquid and gaseous biofuels as alternative energy resources. However, alternate energy resources akin to first generation biofuels derived from terrestrial crops such as sugarcane, sugar beet, maize and rapeseed place an enormous strain on world food markets, contribute to water shortages and precipitate the destruction of the world's forests. Second generation biofuels derived from lignocellulosic agriculture and forest residues and from non-food crop feedstocks address some of the above problems; however there is concern over competing land use or required land use changes. Therefore, based on current knowledge and technology projections, third generation biofuels specifically derived from microalgae are considered to be a technically viable alternative energy resource that is devoid of the major drawbacks associated with first and second generation biofuels. Microalgae are photosynthetic microorganisms with simple growing requirements (light, sugars, CO 2 , N, P, and K) that can produce lipids, proteins and carbohydrates in large amounts over short periods of time. These products can be processed into both biofuels and valuable co-products. This study reviewed the technologies underpinning microalgae-to-biofuels systems, focusing on the biomass production, harvesting, conversion technologies, and the extraction of useful co-products. It also reviewed the synergistic coupling of microalgae propagation with carbon sequestration and wastewater treatment potential for mitigation of environmental impacts associated with energy conversion and utilisation. It was found that, whereas there are outstanding issues related to photosynthetic efficiencies and biomass output, microalgae-derived biofuels could progressively substitute a significant proportion of the fossil fuels required to meet the growing energy demand.

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Biofuels from microalgae—A review of technologies for production, processing, and extractions of biofuels and co-products

The use of fossil fuels is now widely accepted as unsustainable due to depleting resources and the accumulation of greenhouse gases in the environment that have already exceeded the “dangerously high” threshold of 450 ppm CO2-e. To achieve environmental and economic sustainability, fuel production processes are required that are not only renewable, but also capable of sequestering atmospheric CO2. Currently, nearly all renewable energy sources (e.g. hydroelectric, solar, wind, tidal, geothermal) target the electricity market, while fuels make up a much larger share of the global energy demand (∼66%). Biofuels are therefore rapidly being developed. Second generation microalgal systems have the advantage that they can produce a wide range of feedstocks for the production of biodiesel, bioethanol, biomethane and biohydrogen. Biodiesel is currently produced from oil synthesized by conventional fuel crops that harvest the sun’s energy and store it as chemical energy. This presents a route for renewable and carbon-neutral fuel production. However, current supplies from oil crops and animal fats account for only approximately 0.3% of the current demand for transport fuels. Increasing biofuel production on arable land could have severe consequences for global food supply. In contrast, producing biodiesel from algae is widely regarded as one of the most efficient ways of generating biofuels and also appears to represent the only current renewable source of oil that could meet the global demand for transport fuels. The main advantages of second generation microalgal systems are that they: (1) Have a higher photon conversion efficiency (as evidenced by increased biomass yields per hectare): (2) Can be harvested batch-wise nearly all-year-round, providing a reliable and continuous supply of oil: (3) Can utilize salt and waste water streams, thereby greatly reducing freshwater use: (4) Can couple CO2-neutral fuel production with CO2 sequestration: (5) Produce non-toxic and highly biodegradable biofuels. Current limitations exist mainly in the harvesting process and in the supply of CO2 for high efficiency production. This review provides a brief overview of second generation biodiesel production systems using microalgae.

https://www.springer.com/cda/content/document/cda_downloaddocument/BioEnergyResearch_Second+Generation+Biofuels+High-Efficiency+Microalgae+for+Biodiesel+Production.pdf?SGWID=0-0-45-1347846-0

Second generation biofuels: high-efficiency microalgae for biodiesel production

Cultivation, photobioreactor design and harvesting of microalgae for biodiesel production: A critical review

Photobioreactors for mass cultivation of algae.

Microalgae are a diverse group of prokaryotic and eukaryotic photosynthetic microorganisms that grow rapidly due to their simple structure. They can potentially be employed for the production of biofuels in an economically effective and environmentally sustainable manner. Microalgae have been investigated for the production of a number of different biofuels including biodiesel, bio-oil, bio-syngas, and bio-hydrogen. The production of these biofuels can be coupled with flue gas CO2 mitigation, wastewater treatment, and the production of high-value chemicals. Microalgal farming can also be carried out with seawater using marine microalgal species as the producers. Developments in microalgal cultivation and downstream processing (e.g., harvesting, drying, and thermochemical processing) are expected to further enhance the cost-effectiveness of the biofuel from microalgae strategy.

https://aiche.onlinelibrary.wiley.com/doi/pdf/10.1021/bp070371k

Biofuels from microalgae.

A vertical alveolar panel (VAP) for outdoor mass cultivation of microalgae and cyanobacteria

A photobioreactor in the form of a 245-m-long loop made of plexiglass tubes having an inner diameter of 2.6 cm was designed and constructed for outdoor culture of Spirulina. The loop was arranged in two planes, with 15 8-m-long tubes in each plane. In the upper plane, the tubes were placed in the vacant space between the ones of the lower plane. The culture recycle was performed either with two airlifts, one per plane, or with two peristaltic pumps. The power required for water recycle in the tubular photobioreactor, with a Reynolds number of 4000, was 3.93 x 10(-2) W m(-2). The photobioreactor contained 145 L of culture and covered an overall area of 7.8 m(2). The photobioreactor operation was computer controlled. Viscosity measurements performed on Spirulina cultures having different biomass concentrations showed non-Newtonian behavior displaying decreasing viscosity with an increasing shear rate. The performance of the two-plane photobioreactor was tested under the climatic conditions of central Italy (latitude 43.8 degrees N, longitude 11.3 degrees E). A biomass concentration of 3.5 g L(-1) was found to be adequate for outdoor culture of Spirulina. With a biomass concentration of 6.3 g L(-1), the biomass output rate significantly decreased. The net biomass output rate reached a mean value of 27.8 g m(-2) d(-1) in July; this corresponded to a net photosynthetic efficiency of 6.6% (based on visible irradiance).

A two-plane tubular photobioreactor for outdoor culture of Spirulina.

Biomass production and studies on Rhodopseudomonas palustris grown in an outdoor, temperature controlled, underwater tubular photobioreactor.

Efficient utilization of solar radiation for the photoautotrophic production of cyanobacterium biomass was achieved, using small pipes (ID = 0.01 m) arranged in rows in two photobioreactors facing south–north. A high Arthrospira yield of 47.7 g m−2 (installation area) d−1 was attained under outdoor conditions in a tubular undulating row photobioreactor (TURP-10r). During the summer, under a semicontinuous culture regime, the optimal biomass concentration (OBC) in TURP-5r was 6.0 g L−1: it was 5.0 g L−1 in TURP-10r. These OBCs made it possible to produce a biomass output rate of 2.7 ± 0.2 g L−1 d−1 in the former and 2.1 ± 0.1 g L−1 d−1 in the latter. When Arthrospira was grown at a preset dilution rate (0.3 d−1), sunrise cell density (SrCD) variations were not proportional to the drop of solar radiation. The SrCD was comparatively high at high solar radiation and decreased abruptly with decreasing solar radiation. There was a tendency to stabilize at low solar radiation. In both photobioreactors, the chlorophyll content of the Arthrospira biomass (% of the dry weight) was higher at sunrise than at sunset. A comparison of the chlorophyll biomass content in the TURPs showed no significant differences. Night biomass losses were very high (> 30% of the daylight productivity) when the culture temperature was kept constant at 31 ± 1.0°C: these losses fell to < 20% of the daylight productivity, when the night temperature of the cultures decreased according to the environmental temperature. Dilution of solar radiation was carried out using two quasi-laminated bioreactors. The rows of S–N facing bioreactors showed a very high growth yield in TURP-10r [about 2.1g (d.w.) MJ−1]. In TURP-10r, the high photic ratio (Rf = 6), the high surface-to-volume ratio (Sill/V = 400 m−1) and the S–N facing of the rows (better than an E–W orientation) allowed for good results. © 2003 Wiley Periodicals, Inc. Biotechnol Bioeng 81: 305–315, 2003.

Dilution of solar radiation through “culture” lamination in photobioreactor rows facing south–north: A way to improve the efficiency of light utilization by cyanobacteria (Arthrospira platensis)

An inexpensive and simple solar device was constructed and monitored for drying microalgal biomass with 90% moisture content. The drier is capable of producing about 140g dry biomass per sq.m of collector area in 3–5 hours. The dried biomass contains less than 10% moisture and is biologically of good quality. The experiments are done with two microalgae - Spirulina and Scenedesmus.

Pietro Carlozzi

Papers

A vertical alveolar panel (VAP) for outdoor mass cultivation of microalgae and cyanobacteria

A two-plane tubular photobioreactor for outdoor culture of Spirulina.

Biomass production and studies on Rhodopseudomonas palustris grown in an outdoor, temperature controlled, underwater tubular photobioreactor.

Dilution of solar radiation through “culture” lamination in photobioreactor rows facing south–north: A way to improve the efficiency of light utilization by cyanobacteria (Arthrospira platensis)

Microalgal biomass drying by a simple solar device