5.3. Effect of Light Intensity and Wavelength
Light is one of the most important environmental factors for microalgal growth. Previous studies have shown that high light intensity can significantly increase lipid accumulation in microalgae. The TAG content increased and the polar phospholipid composition decreased as the light intensity was increased in
Cladophora sp.
[64].
Nannochloropsis sp. cultivated under low light intensity (35 µmol m
−2 s
−1) had a lipid composition of 26% TAG and 40% galactolipid. A unicellular alga,
Scenedesmus sp., accumulates a significant amount of lipid content when cultivated under light conditions of 250–400 µmol m
−2 s
−1 [65]. The total lipid content of
Dunaliella salina,
Isochrysis galbana, and
Nannochloropsis oculata increases when the light intensity is increased to 150 µmol m
−2 s
−1 [66]. Microalgae grown under red light showed higher lipid accumulation than those grown under yellow or white light. Microalgae cultivated under green light had lower lipid accumulation than those grown under red light. For example, exposing a unicellular microalga
Chlorella sp. to red light resulted in increased growth and lipid content
[67].
Another technique for improving microalgal growth and lipid accumulation is to use chemical dyes to change the light spectrum
[68]. For example, organic dyes such as rhodamine 101 and 9,10-diphenylanthracene have been used to convert unused and/or harmful portions of incident sunlight into usable photons for microalgae cultivation, thereby increasing the productivity of biomass and lipids. The lipid yield of
Chlorella vulgaris can be improved by cultivating it in a medium containing these chemical dyes
[68]. Red paint produced the highest biomass output, while blue paint produced the maximum lipid content of 30% dry weight
[69]. The lipid composition of microalgae is significantly affected by photoperiod. The effect of light intensity on the lipid composition of microalgae has been investigated in a variety of ways, and it has been found that PUFA levels decrease as light intensity increases
[70]. Microalgae grown under high light intensity and long light periods had higher saturated fatty acids (SFAs) levels and lower MUFAs and PUFAs levels
[71].
5.4. Effect of Temperature
Temperature changes influence not only lipid synthesis but also lipid content in the microalgae. In most microalgae, a decrease in temperature resulted in an increase in polar lipid content, while an increase in temperature resulted in an accumulation of non-polar lipids
[72]. Exposing
Acutodesmus dimorphus to temperature stress at 35 °C led to a 22.7% increase in lipid yield and a 59.9% increase in neutral lipid accumulation
[73]. A decrease in temperature from 30 to 25 °C in
Chlorella vulgaris has been shown to increase lipid content by 2.5-fold, without any change in growth rate
[74]. Low temperatures simultaneously stimulate lipid content and reduce growth in
Chlorella sorokiniana [75].
Although most studies focus on total lipid content, few have investigated the impact of temperature on specific lipid classes. Microalgae cultivated at low temperatures have a high content of PUFAs, which are important for survival in harsh conditions. When the temperature was decreased from 25 to 10 °C,
Isochrysis galbana showed a significant increase in PUFA content
[76].
Phaeodactylum tricornutum also showed a similar increase in PUFA content when the temperature was decreased from 25 to 10 °C
[77].
5.5. Effect of Salinity
In response to salt stress, microalgae typically undergo biochemical changes that regulate lipid production. However, the salinity tolerance of different microalgae strains varies.
Dunaliella sp. is an example of a microalga that can withstand high salt concentrations.
Dunaliella salina is a well-studied microalga because it can use salt stress to increase both biomass productivity and lipid yield.
Dunaliella tertiolecta exhibited an increase in both total lipid content and a notable percentage of TAGs when the amount of NaCl was increased
[78].
Scenedesmus sp., when subjected to salinity stress of 400 mM during a biphasic cultivation process, resulted in a lipid content of 34.77%
[79]. The lipid content of various microalgae, including
Scenedesmus sp.,
Chlorella vulgaris, and
Chlamydomonas mexicana, increases under salt stress conditions
[19][79][80]. In most microalgae, the lipid content peaks at a certain salt concentration, and then declines significantly beyond this concentration. In
Chlorella minutissima, salt stress affects both biomass production and lipid content
[81].
5.6. Effect of pH
The pH affects the photosynthetic process, the solubility of inorganic nutrients, the rate of lipid accumulation, and the activity of enzymes in the cell. For microalgal growth, a certain pH range is required, which is limited and strain-specific. Microalgae are able to accumulate higher lipid content within a pH range of 7 to 9.5.
Chlorella sp. showed an increase in lipid content up to 23% at pH 8, and
Tetraselmis suecica showed a similar trend at pH 7.5. A study of the impact of various pH values (6, 7, 8, 9, and 10) on the biomass and lipid content of
Nannochloropsis salina found that
N. salina exhibited optimal growth rates and lipid content at pH 8 and 9
[82].
The relationship between CO
2 and pH for microalgal cultivation is intricately linked through a process known as carbon dioxide dissolution or carbonic acid equilibrium. pH is important for microalgal growth because it affects the solubility of CO
2 in the culture medium. As the pH increases, the solubility of CO
2 decreases. This means that there is less CO
2 available for microalgae to use. The optimal pH range for microalgal growth varies depending on the species of microalgae. However, most microalgae grow best in a pH range of 6.5 to 8.5
[24]. At pH levels below 6.5, the solubility of CO
2 is too low, and at pH levels above 8.5, the toxicity of CO
2 increases. When CO
2 dissolves in water, it forms carbonic acid (H
2CO
3).
The relationship between CO
2 and pH is complex. As microalgae grow, they take up CO
2 from the medium, which causes the pH to increase. This can be counteracted by injecting CO
2 into the culture, or by adding a buffer to the medium. The amount of CO
2 that needs to be added or the amount of buffer that needs to be added depends on the pH of the medium, the species of microalgae, and the growth rate of the culture. As CO
2 dissolves in the culture medium where microalgae are cultivated, it decreases the pH of the medium. This means that as more CO
2 is added to the culture, the pH of the medium becomes more acidic due to the formation of carbonic acid. Conversely, when CO
2 is removed from the medium (for instance, through microalgal photosynthesis), the pH tends to increase, becoming more alkaline. This pH fluctuation is essential to monitor and control in microalgal cultivation systems because microalgae have specific pH preferences for optimal growth.
5.7. Effect of Metal
The lipid content of microalgae is affected by the presence of trace metals, and the amount of lipids produced depends on the concentration of these metals in the growth medium. Heavy metals, including copper, zinc, and cadmium has been shown to increase lipid yield in some microalgae. Iron stands out as particularly effective in enhancing photosynthetic enzyme activities. For example, the overall lipid content of
Chlorella vulgaris increases by approximately 3 to 7 times when it is exposed to FeCl
3 [83].
5.8. Effect of Sulfur Starvation
Algae require sulfur in the form of sulfate as an essential nutrient for their growth. Sulfur limitation in the growth medium can induce lipid accumulation in algae. In response to sulfur limitation, algae may alter their metabolic pathways to prioritize lipid synthesis as a way to cope with the stress. For example, under sulfur starvation,
Chromochloris zofngiensis and
Scenedesmus acuminatus exhibit high lipid accumulation
[84][85]. Sulfur stress can also change the fatty acid profile of algal lipids. This could lead to changes in the proportion of saturated to unsaturated fatty acids and the length of fatty acid chains
[85]. Sulfur stress can alter the regulation of key enzymes involved in lipid biosynthesis pathways.
5.9. Effect of Phytohormones
To stimulate lipid accumulation in microalgae, it is important to use both traditional abiotic stress conditions and innovative techniques. This is necessary because there is a reciprocal relationship between biomass and lipid accumulation under abiotic stress
[86]. The effects of phytohormones on microalgal metabolism, especially in relation to lipid production, are still not fully clear. However, it has been noted that auxins, a type of phytohormone, can promote the growth of
Scenedesmus sp. This growth regulator has been found to increase the content of TAGs and MUFAs, while simultaneously reducing the content of PUFAs
[87]. The combination of indole-3-butyric acid (IBA) at a level of 10 mg/L and 6-benzylaminopurine (BAP) at a level of 5 mg/L exhibited a synergistic effect. The synergistic effect led to a 2.34 g/L increase in biomass production and a 42.43% increase in lipid content
[88]. Similar findings were reported in
Chlorella sp., where the application of IBA promoted maximum growth and lipid yield
[89].
Fluvic acid, an additional phytohormone, has been used to enhance lipid yield in microalgae. This effect was achieved by modulating gene expression and the actions of principal enzymes such as phosphoenolpyruvate carboxylase and acetyl-CoA carboxylase
[90]. The application of salicylic acid (SA) at a concentration of 10 ppm resulted in a substantial increase in lipid, reaching 475 mg/L in the early stationary growth phase. The application of salicylic acid (SA) was found to be crucial for the formation of omega-3 fatty acids, specifically eicosapentaenoic acid (EPA, C20:5)
[91]. Higher concentrations of methyl jasmonate (MeJA) were found to promote the formation of MUFAs, especially oleic acid (C18:1). Most phytohormones have demonstrated the ability to enhance biomass production, and some have also shown promise in improving lipid yield and modifying lipid composition.
6. Microalgal Biorefinery for Biofuels Production
A microalgal biorefinery is a specialized facility designed to harness the full potential of microalgae for the production of biofuels and various other valuable products. Microalgal biomass can be processed into an extensive array of products, including proteins, carbohydrates, lipids, pigments, polyunsaturated fatty acids, antioxidants, nutraceuticals, vitamins, biofertilizers, animal feed, biosurfactants, and bioenergy products (
Figure 3). A microalgal biorefinery, in combination with other processes, has the potential to solve the current bioeconomic problem by producing multiple high-value products
[92]. Microalgae are an efficient feedstock for generating various types of biofuels, depending on the chosen generation route (
Figure 3). Microbial biomass conversion to biofuels is an alternative approach to the increasing demand for fossil fuels. Microalgal biorefineries hold promise as a sustainable and versatile solution for biofuel production, offering the potential to address energy needs while promoting environmental sustainability and economic diversification
[93][94].
Figure 3. Various types of biofuels and value-added products produced by microalgae biomass depending on the specific methods.
The zero-waste principle represents a fundamental shift in the paradigm of microalgal biorefinery, emphasizing the efficient utilization of all components within microalgal biomass to minimize waste generation
[95][96]. In traditional microalgal cultivation and processing, there is often a focus on extracting a single high-value product, such as lipids for biodiesel production, while the remaining biomass and by-products are discarded. However, the zero-waste approach recognizes the intrinsic value of every constituent within microalgae and seeks to extract and utilize multiple valuable products from a single biomass source. The zero-waste principle endeavors to achieve the highest degree of resource efficiency by extracting, separating, and valorizing all components of microalgae. This entails not only the extraction of lipids but also proteins, carbohydrates, pigments, and other bioactive compounds
[97]. For instance, after lipid extraction, the residual biomass can be processed to recover proteins suitable for food and feed applications, pigments for cosmetics, or carbohydrates for bioethanol production
[98][99]. This comprehensive utilization optimizes resource efficiency, minimizes waste, and reduces the environmental footprint of microalgal biorefineries. Moreover, it helps diversify revenue streams by generating multiple valuable products from the same starting biomass, thereby enhancing economic viability.
Industry examples showcase the practical implementation of the zero-waste principle in microalgal biorefineries. One such instance is the production of omega-3 fatty acids and astaxanthin from microalgae
[100][101]. Omega-3 fatty acids are highly valued for their health benefits and are used in dietary supplements and functional foods. Meanwhile, astaxanthin, a potent antioxidant and pigment, finds applications in nutraceuticals, cosmetics, and aquaculture feeds
[102]. By cultivating microalgae for these high-value compounds, the zero-waste approach ensures that the residual biomass, which still contains valuable proteins, carbohydrates, and pigments, is put to use, reducing waste and enhancing the economic feasibility of the entire process.
Embracing the zero-waste principle in microalgal biorefinery aligns with broader sustainability objectives and the transition towards a circular bioeconomy. It reduces the environmental impact associated with waste disposal and provides an environmentally responsible alternative to resource-intensive practices. Furthermore, by efficiently utilizing microalgal biomass, the zero-waste approach contributes to the development of a sustainable and circular bioeconomy, where resources are conserved, reused, and repurposed
[101]. This not only helps mitigate environmental pressures but also fosters economic resilience and innovation in the microalgal industry.
Further, microalgae biorefinery has emerged as a promising approach for sustainable and diversified bioproduct production, driven by the concept of multi-product valorization. Traditionally, the focus in microalgal cultivation has primarily been on a single high-value product, such as biofuels or nutraceuticals. However, the realization of the full potential of microalgae lies in their ability to yield multiple valuable products simultaneously. One compelling example of multi-product production in the microalgal industry is the cultivation of
Haematococcus pluvialis. This microalga is renowned for its ability to accumulate astaxanthin, a potent antioxidant and red pigment used in nutraceuticals and cosmetics
[103]. While astaxanthin is a high-value product, the residual biomass still contains valuable components, including proteins and carbohydrates. In response, some companies have developed integrated biorefinery processes to simultaneously extract astaxanthin, proteins, and carbohydrates from
H. pluvialis, thus diversifying their product portfolios and reducing waste.
Another compelling instance involves the production of value-added nutraceuticals from microalgae. Companies have successfully cultivated microalgae such as
Chlorella sp. and
Spirulina sp. to produce not only lipids for biofuels but also high-protein biomass suitable for dietary supplements
[104][105]. The versatility of microalgae enables the simultaneous production of lipids for biofuel and proteins for nutraceuticals, underscoring the potential for multi-product production in microalgal biorefineries. This approach enhances economic viability by tapping into multiple markets and revenue streams.
Additionally, some microalgal species, such as
Nannochloropsis and
Schizochytrium, offer the unique advantage of co-producing biodiesel and omega-3 fatty acids. While
Nannochloropsis is known for its lipid-rich biomass suitable for biodiesel production, it also produces valuable long-chain omega-3 fatty acids such as eicosapentaenoic acid (EPA)
[106]. Similarly,
Schizochytrium produces docosahexaenoic acid (DHA), another omega-3 fatty acid, alongside lipids
[107]. The co-production of biodiesel and omega-3 fatty acids exemplifies the potential for microalgae to serve multiple industries, including biofuels and nutraceuticals. Embracing the concept of multi-product production in microalgae biorefineries not only enhance economic feasibility but also aligns with the broader goals of sustainability, resource efficiency, and circular bioeconomy development. Here are some of the biofuels that are commonly produced using biorefineries.