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Review

A Review on Synchronous Microalgal Lipid Enhancement and Wastewater Treatment

Department of Civil and Environmental Engineering, University of North Carolina at Charlotte (UNCC), Charlotte, NC 28223, USA
*
Author to whom correspondence should be addressed.
Energies 2021, 14(22), 7687; https://doi.org/10.3390/en14227687
Submission received: 6 October 2021 / Revised: 3 November 2021 / Accepted: 10 November 2021 / Published: 17 November 2021
(This article belongs to the Special Issue Water and Wastewater Treatment- Energy Efficiency)

Abstract

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Microalgae are unicellular photosynthetic eukaryotes that can treat wastewater and provide us with biofuel. Microalgae cultivation utilizing wastewater is a promising approach for synchronous wastewater treatment and biofuel production. However, previous studies suggest that high microalgae biomass production reduces lipid production and vice versa. For cost-effective biofuel production from microalgae, synchronous lipid and biomass enhancement utilizing wastewater is necessary. Therefore, this study brings forth a comprehensive review of synchronous microalgal lipid and biomass enhancement strategies for biofuel production and wastewater treatment. The review emphasizes the appropriate synergy of the microalgae species, culture media, and synchronous lipid and biomass enhancement conditions as a sustainable, efficient solution.

1. Introduction

Day by day, humankind creates many aspects of environmental pollution, mostly due to urbanization and industrialization. Fossil fuel depletion and the release of untreated wastewater are among the two most severe problems in recent times contributing to air and water pollution. Fossil fuel depletion increases the level of greenhouse gases in the environment. At the same time, untreated wastewater contains heavy metals, excess nutrients, and pathogens. Thus, both fossil fuel depletion and the release of untreated wastewater threatens human and ecological well-being. The rapidly growing pollution level has led to a call for desperate sustainable alternatives to be considered. Otherwise, an unpredictable climate and environmental changes may be activated, causing brutal health and ecological disruptions and, consequently, triggering the requirement of clean, sustainable energy resources and wastewater treatment at the same time.
Biological treatment seems to be a clean, sustainable alternative for environmental pollution mitigation. Microalgae are attributed with the distinct ability to offer ecological services and react to the sustainability challenges concurrently. In recent times, microalgae have gained attention worldwide for their significant potential in biofuel production and wastewater treatment besides mitigating atmospheric CO2. Microalgae can grow in nutrient-rich wastewater and reduce pollutants in the water bodies [1,2]. Microalgal bioremediation (phycoremediation) of wastewater also provides biofuels or high-value biomass yield for biofuel production simultaneously [3]. Pittman et al. [4] concluded that microalgae cultivation for biofuel devoid of wastewater is expensive with no positive energy return. Lundquist et al. [5] studied various microalgae-based wastewater treatments combined with biofuel production. They observed that the studies that utilized wastewater for microalgae cultivation could produce cost-effective biofuel, especially on a large scale.
Many previous studies have been reported on the phycoremediation of wastewater [6] and microalgae-based fuel production [7,8] (Table 1). Additionally, various studies have wastewater treatment combined with microalgae biofuel production. Min et al. [9] studied algal biomass production for biofuel while treating swine manure-based wastewater. They observed that the nutrient removal rate from the wastewater significantly correlated to the algal biomass productivity. The NH₃-N, TN, PO₄-P, and COD reduction rates were observed to be 2.65, 3.19, 0.067, and 7.21 g/m2 × day, respectively, and the algal biomass productivity ranged from 8.08–14.59 and 19.15–23.19 g/m2 × day. However, a very low lipid content of 1.77–3.55% was observed for the harvested algal biomass. Mar et al. [10] studied the growth of Desmodesmus sp. S1 in oil refinery wastewater. Efficient wastewater treatment was achieved with 82% COD removal, 53% total phosphorous removal, metal ions (Fe3+, Al3+, Mn2+, Zn2+) removal, and pungent smell removal, whereas in Desmodesmus sp. S1, biomass and lipid contents were 2.98 g/L and 21.95%, respectively. Daneshvar et al. [11] reported the biomass productivity of 187 mg/L/d and lipid content of 9.07% for Chlorella vulgaris in pulp and aquaculture wastewater. They witnessed efficient wastewater treatment showcasing 75.5% COD removal, 76.5% total nitrogen removal, and 92.7% total phosphorous removal. Thus, from most previous studies, it was observed that microalgae are efficient for wastewater treatment, but biomass production and lipid content are inversely related. This inverse relation of microalgae biomass production in wastewater and lipid content might be a bottleneck. High biomass production and high lipid content using wastewater as a culture media is a cost-effective, sustainable option. It is also feasible to stock up lipids in microalgae to a considerable amount by changing physio-chemical factors.
There are many review papers available that focus on using microalgae for wastewater treatment, biofuel production, or even integration of both processes. However, this review paper emphasizes the microalgae lipid enhancement strategies by not compromising the biomass productivity and utilizing wastewater as the growth media. Challenges such as high prices can be reduced by coupling wastewater treatment with high biomass and lipid productivity for biofuels. As the review was on synchronous microalgae lipid enhancement and wastewater treatment, the major keywords utilized for identifying literatures were microalgae, wastewater, lipid enhancement, and biofuel. The time frame for sorting the literature search was from 2002 to 2021.

2. Functioning of Microalgae

Microalgae are photosynthetic organisms functioning in presence of nutrients, light, and CO2 to grow (Figure 1). Besides nutrients, light, and CO2, many other environmental factors (temperature, pH) determine their growth rate. As microalgae uptake nutrients for growth, many studies have utilized microalgae for nutrient removal from wastewater. This process of excess nutrient removal from water bodies by microalgae is known as phycoremediation. Microalgae have also found their usage in biofuel production as they are rich in lipids.

2.1. Wastewater Treatment

Microalgae cultivation for wastewater treatment is an old practice. Microalgae are capable of producing oxygen (O2) through photosynthesis during cultivation. The produced oxygen can be used to degrade organic contaminants and phycoremediate inorganic compounds available in the wastewater. Thus, photosynthetic oxygen eradicates the necessity to supply air through the conventional aeration process, decreasing the cost drastically. To reduce the probability of eutrophication, microalgal ponds were designed to treat the secondary effluent before release in aquatic bodies. Microalgae can also eliminate the nutrients (N, K) more proficiently in wastewater than conventional treatment routes.

2.2. Biofuel Production

Microalgae can convert atmospheric CO2 into carbohydrates and lipids [7]. Lipids produced by microalgae can be divided into polar lipids (glycerophospholipids), which have an important role in cell structure, and non-polar lipids (triacylglycerols, TAGs) mainly responsible for energy storage. Lipids are stocked up in microalgae in diverse ways based on the species, growth phase, and environmental conditions. When photosynthesis occurs in microalgae, non-polar lipids such as TAGs accumulate in the cells [23]. TAGs are modified into fatty acid methyl esters by trans-esterification for biofuel production [8].
Microalgal lipid production is around 15–300 times more than the oil-bearing crops (palm, corn, soybean, and sunflower) [24]. Microalgae are competent and preferable to produce biofuels as they do not require land and freshwater for cultivation. The best way to produce high amounts of these lipids is to sustain global energy demands through high microalgal biomass productivity. Previous studies have reported that accomplishing both factors synchronously is very difficult [25]. Although there are many challenges for microalgal biofuel production, researchers believe that microalgal biofuel is still a promising alternative for fossil fuel. A new focus in microalgal biofuel research is to optimize an ideal condition to achieve a high growth rate of microalgae while producing high lipid content under a stressful environment. Therefore, various approaches to enhance the lipid production rate in microalgae have been investigated.

3. Strategies for Lipid Enhancement

This section may be divided by subheadings. It should provide a concise and precise description of the experimental results, their interpretation, as well as the experimental conclusions that can be drawn.

3.1. Selection of Proper Microalgae Species or Strain

In various kinds of literature, altering the culture condition has been mentioned as a strategy for lipid enhancement in microalgae. However, biofuel production’s primary drawback cannot be conquered if the microalgae species/strain is not suitable for the purpose. Microalgae have been under the limelight for their lipid-producing capability [26]. Lipid content and growth rate in microalgae vary from species to species. Lipid production by microalgae for commercial purposes undergoes tough challenges as microalgae display two different traits, either low lipid accumulation with high biomass production or vice versa. The microalgae Botryococcus braunii has a lipid content of 25–75% but a low growth rate, Chlorella vulgaris has a lipid content of 28–58% and a very high growth rate, Dunaliella salina has a low lipid content of 6–25% and a moderate growth rate, and Nannochloropsis oculata has a lipid content of 23–30% and a high growth rate [27]. Although lipid production in microalgae is species-specific, sometimes it is also strain-specific. The same microalgal species of a different strain can vary in lipid composition as well. Yamaguchi et al. [28] studied two different B. braunii strains under the same culture conditions and media. They reported that the lipid composition is different for both the strains, although biomass and lipid yields are similar. Growth characteristics and lipid production can vary for the same species/strain based on the growth media composition and other physio-chemical factors (light, carbon dioxide, temperature, salinity) [29]. Ruangsomboon [30] chronologically changed growth conditions (nitrogen, phosphorus, iron, light, salinity, and cultivation time) for B. braunii (KMITL2) in chlorella medium. At 25 °C, 222 mg/L phosphorus concentration and continuous illumination of 200 μE m−2 s−1, the maximum lipid yield of 0.48 mg/L and biomass yield of 0.8 g/L was obtained. When phosphorus concentration was increased to 444 mg/L, lipid yield (0.45 g/L) and biomass concentration (1.91 ± 0.03 g/L) were also enhanced.
Hence, the first step for the microalgae cultivations is to determine or engineer the proper species/strain for the specific function and intention. As enhancing lipid productivity is hindered by swapping between lipid accumulation and cell growth, numerous endeavors are being made to decipher these bottlenecks, from choosing oleaginous species, strain development, and strain acclimation, to diverse cultivation media and conditions [31].

3.2. Selection of Proper Growth Media

The growth of microalgae necessitates the need for light, carbon dioxide, water, and nutrients, nitrogen and phosphorus being the chief nutrients required for their growth. For phototrophic culture, BG-11 and Chu 13 are the most used growth media with CO2 supplementation [32,33,34,35], as BG-11 and Chu 13 contain all the significant nutrients necessary for the growth of microalgae, whereas for mixotrophic culture, synthetic media with organic carbon sources are mostly utilized [36]. Yeh and Chang [37] investigated the growth and lipid productivity of Chlorella vulgaris ESP-31 in different media (Basal medium and Modified Bristol’s medium) and cultivation conditions. At phototrophic, photoheterotrophic, and mixotrophic conditions, C. vulgaris ESP-31 obtained a biomass concentration of 2–5 g/L in nitrogen-rich media. C. vulgaris ESP-31 growth on nitrogen limiting media exhibited enhanced lipid build-up (20–53%) with a slower growth rate. When all the culture media were utilized at mixotrophic conditions, enhanced lipid content (40–53%) and enhanced lipid productivity (67–144 mg/L/d) were achieved. Hence, growth media and cultivation conditions influence microalgal growth and lipid accumulation to a great extent.
A huge quantity of water is essential for the microalgae cultivation process. Yang et al. [38] assessed that to generate 1 kg of microalgal biofuel, 3726 kg of water is necessary, and this prerequisite can be reduced by 90% via wastewater utilization. Saranya and Shanthakumar [39] investigated the performance of Chlorella vulgaris (NRMCF0128) and Pseudochlorella pringsheimii (VIT_SDSS) using combined sewage and tannery effluent at varying dilution. At a higher dilution (up to 30%) of tannery effluent both the species exhibited a drop in pollutant concentration: >65% for NH3-N, 100% for PO4-P, >63% for COD, and >80% for total chromium. They observed the maximum biomass yield of 3.51 g/L for Chlorella vulgaris at 30% tannery effluent, whereas it was for Pseudochlorella pringsheimii 2.84 g/L at for 20% tannery effluent. Additionally, P. pringsheimii exhibited an enhanced lipid accumulation of 25.4%, which was greater than that of Chlorella vulgaris (9.3%). They also reported that at 20% dilution, the lipid accumulation of P. pringsheimii was 5 times and 1.5 times more than undiluted sewage- and BG11-grown microalgae. Hence, it is evident that Pseudochlorella pringsheimii when grown in 20% tannery effluent assists in biomass growth, lipid enhancement, and treatment of wastewater.
Utilization of post-fermentation leachate from biogas plants, including the wastewater after the initial stage of anaerobic digestion, is a favorable route for microalgae biomass production and wastewater treatment. The post-fermentation wastewater comprises a high content of nitrogen and phosphorus, significant amounts of dissolved carbon dioxide, and low organics. A. prothecoides when cultivated in post-fermentation wastewater reported 79.45% nitrogen removal, 78.4% phosphorus removal, and the maximum lipid content of 44.65% [40].
Wastewater can serve as an excellent medium for microalgae cultivation as it contains the nutrients necessary for its growth. The utilization of wastewater as a growth medium for microalgae is an economical step as wastewater is easily available in plenty and there is no need to add nutrients as a supplement. The addition of nutrients for microalgae growth can be expensive if required in huge quantities. Wastewater utilization reduces the surplus cost of nutrient addition, especially in large-scale cultivation [41]. Furthermore, using wastewater as a growth medium for microalgae induces wastewater treatment. Therefore, wastewater utilization for microalgae growth is an economical and sustainable alternative.

3.3. Selection of Proper Stress Condition

Microalgae tend to stock up a substantial amount of lipids under stress. However, the stressful culture condition where lipid (TAGs) synthesis takes place simultaneously stimulates protein biodegradation, compromising on cell growth and biomass productivity. There are quite a few physio-chemical stress factors that perk up the stimulation of lipid accumulation such as light, temperature, CO2, nutrients, and salinity (Table 2). Diverse microalgae species/strains respond differently to different stress conditions, thereby producing different quantities and composition of lipids in different microalgae species/strains. This alteration in the microalgae lipid metabolism can enhance the lipid basal level.

3.3.1. Effect of Light

Light is one of the most indispensable factors for the production of microalgal biomass. Light provides energy for the process of photosynthesis and microbial growth. The intensity of light and its wavelength can drastically modify microalgal growth and lipid accumulation (Table 3). Wahidin et al. [52] in Nannochloropsis sp (marine microalga) noticed an enhanced lipid accumulation of up to 31.3% after 8-day cultivation under 100 µmol m−2 s−1 light intensity and a photoperiod of 18 h light: 6 h dark cycle. They also observed a gradual decline in cell density and growth rate during the 24 h photoperiod cycle. Zhu et al. [8] reported that extreme light intensities affected the lipid content by photo-inhibition and photo-oxidation. Generally, microalgae encompass a light saturation limit of 600 ft. candles approximately. Exposure of microalgae to light intensity more than the light saturation limit causes oxidative stress [52]. Excessive photo-assimilation causes lipid stock up as a self-defense mechanism to prevent photo-oxidative damage, thus transforming the surplus light energy into chemical energy [53,54]. For Chlorella sp. L1, the high light intensity of 400 µmol photon m−2 s−1 exhibited neutral lipid productivity of 51.4 mg L−1 d−1 by He et al. [55]. Ruangsomboon [30] reported that Botryococcus braunii KMITL 2 exposed to high light intensities of 200 and 538 μE −2 s−1 stocked up more lipid than those grown at lower light intensity (87.5 μE m−2 s−1). On the other hand, Phaeodactylum tricornutum at a low light intensity of 60 µmol photons m−2 s−1 exhibited the highest TAG yield of 112 mg molph−1 [31] This indicates that the light intensity, which may be low for few microalgae species, can be high for some other microalgae species. The microalgae Nannochloropsis sp. produces the enhanced lipid content (47% of dry weight) at a light intensity of 700 μmol photons/m2/s [56]. Liu et al. [57] reported that lipid accumulation in Scenedesmus sp. enhanced 11-fold at a light intensity of 400 μmol photons/m2/s, whereas at a light intensity of 600 μmol photons/m2/s, microalgae species C. sorokiniana, C. viscosa, C. emersonii, C. vulgaris, P. beijerinckii, and P. kessleri CCALA255, NIES-2152, and NIES-2159 produced enhanced lipids [58]. Liao et al. [59] confirmed that Chlorella vulgaris at a high light intensity of 560 μE m−2 s−1 exhibited a 92.89% enhanced lipid yield, greater than the lower intensity of 160 μE m−2 s−1. In some microalgae species such as Scenedesmus obliquus, lipid content remained the same when light intensity changed from 200 to 1500 μmol photons/m2/s [60].
Besides light intensity, previous studies are reporting the influence of varying light wavelengths on microalgae growth and metabolism. The microalgae chlorophyll has an absorption band (630–675 nm) in red and blue (450–475 nm) spectral region [61]. The phenomenon of microalgae using light energy obtainable within the wavelength of 400–700 nm is known as photosynthetically active radiation (PAR). Das et al. [62] exposed Nannochloropsis sp. to different light wavelengths (red, green, blue, and white). They reported the highest fatty acid methyl esters (FAME) content under green LED (550 nm). Nevertheless, the maximum volumetric FAME yield was achieved under blue LED (470 nm) owing to maximum biomass productivity at this wavelength. Hultberg et al. [63] observed that Chlorella vulgaris exposed to light at green wavelengths illustrated enhanced polyunsaturated fatty acids (C16:3 and C18:3). According to Rai et al. [64], the best growth and the highest lipid accumulation for Chlorella sp. were obtained in red light, whereas green light demonstrated weak biomass growth and less lipid production. Wong et al. [65] demonstrated that Chlorella vulgaris grown in wastewater using blue light achieved the highest lipid content (34.06%) after 10 days of 18:6 light/dark periods, with an initial cell number of 106 cells/mL. Severes et al. [66] reported that a combination of red (600–700 nm) and blue (400–500 nm) light wavelength for a culture of Chlorella sp. increases biomass production. They also observed that red light wavelength doubled the dry weight of lipids in Chlorella cells during the growth period.
Microalgae seem to produce more polar lipids during low light intensity due to enhanced chloroplast membrane synthesis. A gradual increase in light intensity tends to stock up more neutral lipids without hampering the biomass yield. Both low and extremely high light intensity leads to adverse growth and responses in cells. Therefore, determining the ideal intensity of light helps acquire optimal microalgal growth and enhanced lipid production [53,67]. However, the intensity of light required to attain the maximum growth, and lipid content varies from species to species. Hence, complementing irradiation of the light bands for the constitutive pigments (chlorophyll, phycobilins, and carotenoids) can increase the photosynthetic rate and lipid productivity with reduced energy consumption.

3.3.2. Effect of Temperature

The temperature has a vital effect on microalgae growth and lipid production (Table 4). Temperature can operate as a stress factor that can bump up the reactive oxygen species level and stimulate neutral lipids, i.e., TAGs [68]. Biochemical pathways for lipid synthesis and stock up are regulated by enzymes that are very sensitive to thermal variations [69]. Converti et al. [42] investigated thermal variation (20 to 25 °C) with respect to lipid content for N. oculata and C. vulgaris. They observed that a rise in temperature leads to a drop in lipid content in C. vulgaris and vice versa, whereas for N. oculata a rise in temperature led to enhanced lipid production by 2-fold (7.90–14.92%). Subhash et al. [70] observed a 5-fold rise in neutral lipid at a high temperature of 30 °C in a mixed microalgae culture for wastewater treatment. Bohnenberger and Crossetti [71] reported that for Monoraphidium consortiums and Desmodesmus quadricauda, a lower temperature of 13 °C aids in lipid accumulation. Freire et al. [72] observed the highest growth and lipid productivity for Nannochloropsis limnetica at 22 °C, whereas for Heterochlorella luteoviridis, Menegol et al. [73] observed 40.7% of PUFAs at a temperature of 22 °C, whereas the percentage of saturated fatty acids was increased (52.9%) at 27 °C. Xin et al. [43] reported enhanced lipid build-up at lower temperatures of 10–20 °C than at 25 °C for Scenedesmus sp. LX1. Wei et al. [74] reported that the optimal temperature for lipid stock up for Tetraselmis subcordiformis was 20 °C and for N. oculata 30 °C. Xin et al. [68] reported that almost all of the fatty acids and long-chain species (C16–C18) were saturated at a high temperature of 30 °C for Scenedesmus sp. LX1. Analogous results were also reported by Renaud et al. [75] for the microalgae Rhodomonas sp., Cryptomonas sp., and Prymnesiophyte NT19, respectively.
Although the optimal temperature for microalgae growth and lipid production differs from species to species, still, in many microalgae species, high temperature favors saturated fatty acid formation, which is maneuvered by the cell membrane fluidization. The fluidity of phospholipid bilayers is enhanced when the number of double bonds increases [76]. Furthermore, the fatty acid composition of microalgae is also influenced by temperature.

3.3.3. Effect of Carbon Dioxide (CO2)

Atmospheric CO2 is another essential component for microalgal growth. CO2 is a source of carbon for microalgae cell development. Microalgae capture the atmospheric CO2 in the presence of sunlight to produce biomass and chemical compounds of interest (Table 5). Zhu et al. [8] stated an optimum range of CO2 necessary for the growth, lipid production, and accumulation within the microalgae. A high concentration of CO2 helped Nannochloropsis species, but for some microalgae species, a high concentration of CO2 is toxic [77]. Chiu et al. [78] reported lipid productivity of 142 and 82 mg L−1 d−1 for N. oculata when aerated with 2% and 15% CO2, respectively. Jiang et al. [14] for Nannochloropsis sp. observed an increase in biomass productivity (0.39–1.43 gL−1) and growth rate (0.33–0.52 d−1) at 15% CO2 concentration. Ettlia sp. YC001 at 10% CO2 achieved 3.1 g L−1 cell density and 80.0 mg L−1 d−1 lipid productivity, after 16-days of cultivation [79]. Montoya et al. [80] reported a high concentration of fatty acids and lipid productivity (29.5 mg/L/day) for C. vulgaris at a CO2 concentration of 8% (v/v). Nakanishi et al. [81] obtained maximum lipid productivity of 169.1 mg/L/day for Chlamydomonas sp. JSC4 strain at 4% (v/v) CO2 concentration, whereas for the species D. salina, growth inhibition was observed at 0.02 mol CO2/L concentration or higher for Dunaliella salina. Bagchi and Mallick [82] reported that at 15% (v/v) of CO2 concentration, Scenedesmus Obliquus (Turpin) Kützing GA 45 stocked up 850 mg/L of lipid in 16 days. Hui et al. [83] observed a trend of reduced lipid productivity with increased CO2 concentration while studying the effect of varying CO2 concentration (0.03–20%) in Tribonema minus. At 2% CO2 aeration, maximum total lipid content was attained, and at 20% CO2, total lipid content was at its least. However, the culture aerated at 0.03% CO2 illustrated the second-lowest lipid content, signifying photosynthesis restraints due to the medium’s shortage of carbon sources. Kao et al. [84] cultivated Chlorella sp. in synthetic media by aerating with industrial gaseous effluents rich in CO2. A maximum specific growth rate of 0.827 d−1 and lipid production of 0.961 g L−1 was obtained. Thus, gaseous effluents can be utilized to enhance biomass and lipid production as well as for CO2 biofixation.
Ying et al. [85] studied pH changes at different CO2 concentrations, leading to drastic pH changes which destroy enzymes involved in photosynthesis. The availability of a high level of H2CO3, transformed from the unused CO2, lowered the media’s pH, creating a hostile condition for the growth of microalgae. Additionally, the lowered pH hinders lipid synthesis’s carbon assimilation due to the lowered bicarbonate concentration [8]. pH changes in microalgae cause diverse biochemical responses. In Chlorella, high pH hindered the cell division cycle, provoked the discharge of autospores and initiated TAG utilization [86].
CO2 concentration for microalgal growth and lipid accumulation is species-specific. In short, the increase in CO2 could help in the production and stock up of lipids in the microalgae for some species, but it might not be the same for other microalgae species. Supplying additional CO2 during phycoremediation of wastewater helps in lipid content enhancement [87]. In addition to CO2 concentration, it is crucial to estimate the optimum pH range for optimal biomass growth and lipid stock up in microalgae. When microalgae are provided with high CO2 concentration, a portion of the carbon is utilized for photosynthesis, whereas the remaining carbon is transformed into carbonic acid (H2CO3). H2CO3 causes acidification changing metabolic pathways.

3.3.4. Effect of Nutrients

Microalgae require nutrients (nitrogen, phosphorus, iron, magnesium, sulfur, and silicon) for photosynthesis, respiration, cell division, intracellular transportation, and protein synthesis. Microalgae tend to stock up lipids during nutrient stress (Table 6). Tran et el. [88] investigated the effect of nitrogen deficiency in Chlorella vulgaris. They observed that Chlorella vulgaris accumulates a higher amount of lipids (TAGs). Converti et al. [42] reported that under nitrogen deficiency, the lipid yield enhanced to 15.31% for Nannochloropsis oculata and 16.41% for Chlorella vulgaris. Nitrogen deficiency in Nannochloropsis sp. can synthesize more TAGs and reduce polar lipids [89]. Nannochloropsis sp. F&M-M24 illustrated maximum lipid productivity of 204 mg L−1 d−1 at nitrogen-deficient condition [90], whereas N. oceanica DUT01 illustrated maximum lipid productivity of 31 mg L−1 d−1 under nitrogen-rich conditions [45]. Other studies conducted by Hsieh and Wu [91], Praveenkumar et al. [92] and Li et al. [93] also reported similar results for various species of microalgae. Many previous studies examined that in most microalgae species nitrogen deficiency enhanced lipid accumulation (30–70%) within 7–20 days [94]. Nitrogen deficiency for 9 days helped Monallantus salina to attain the maximum lipid concentration of 72%. Botryococcus braunii attained 61.4%, Chlorella vulgaris attained 57.9% and Nannochloropsis sp. attained 55% lipid production during their lifetime, whereas Scenedesmus sp. and Chlorella sorokiniana could not attain maximum lipid content even after 7 and 14 days. Adams et al. [95] demonstrated that Chlorella vulgaris and Chlorella oleofaciens have more potential as biofuel feedstock species than Chlorella sorokiniana, Neochloris oleoabundans, Scenedesmus dimorphus, and S. naegleii as they react to slight stress, thus growing and accumulating lipids simultaneously. Lin and Lin [96] reported the highest biomass productivity in Scenedesmus rubescens by a mixture of urea and sodium nitrate.
Tao et al. [97] observed differences in lipid content and fatty acid composition for the microalgae species Chlorococcum ellipsoideum, Chlorococcum nivale, Chlorococcum tatrense, and Scenedesmus deserticola due to nitrate and urea deficiency. Yang et al. [98] demonstrated a significant increase in fatty acid yield for Chlamydomonas reinhardtii when the growth media were deficient in phosphorus or nitrogen. Phosphorus deficiency displays minor effects on the photosynthetic physiology and protein content of Chlamydomonas reinhardtii compared with nitrogen deficiency, and microalgae lessen the number of ribosomes to uphold the protein synthesis or polyphosphates storage [99]. Cordeiro et al. [100] studied the effects of phosphorus and nitrogen levels on the growth of species of Microcystis panniformis and Microcystis novacekii. They reported that the lipid accumulation had an inverse and direct correlation with nitrogen (35.8%) and phosphorus concentration (31.7%) for Microcystis panniformis and Microcystis novacekii, respectively. At the same time, Mata et al. [101] observed that increasing the nitrogen concentration up to 10-fold led to increased lipid productivity (47.4 mg/L/day) and content (33.5%) for Dunaliella tertiolecta. Xin et al. [68] in Scenedesmus sp. reported maximum lipid accumulation of 53% under phosphate deficiency (0.1 mg L−1). Microalgae stock up phosphorus as polyphosphate during adequate nutrient conditions, which is then used up during nutrient-deficient conditions.
Microalgae have verified their efficiency and effectiveness in enduring a high concentration of micronutrients. Various studies have demonstrated the increase in the lipid content of some microalgae species due to micronutrients stress. Liu et al. [102] demonstrated 3–7 folds enhanced lipid accumulation in Chlorella vulgaris under higher iron concentration than the control. Baky et al. [103] found enhanced lipid yield (28.12%) with an increase in FeCl3 concentration of 20 mg L−1 when Scenedesmus obliquus was cultivated in N-9 medium. Singh et al. [46] observed that a low iron concentration of 3 mg L−1 decreased the lipid content and productivity of Ankistrodesmus falcatus, whereas enhanced lipid content and productivity were observed when iron concentration (6 mg L−1) increased. Ren et al. [104] studied the effect of Fe3+ (0–0.12 g/L), Mg2+ (0–0.73 g/L), and Ca2+ (0–0.98 g/L) on lipid accumulation in Scenedesmus sp. They reported that the addition of EDTA (0–1 mg/L) during cultivation increased total lipid content up to 28.2% and lipid productivity up to 29.7%. Gorain et al. [105] observed enhanced lipid content (1.44-fold) when 100 mg L−1 magnesium was added in the media. Battah et al. [94], using manganese chloride (MnCl2) at a concentration of 2 μM, 10 μM, and 12 μM, evaluated the effect of Mn2+ and Co2+ on the lipid content of C. vulgaris. They observed that MnCl2 at 2 μM, 10 μM, and 12 μM concentration increased lipid content significantly by 14%, 16%, and 15%, respectively. In addition to that, Battah et al. [106] reported a 25% increase in lipid content when cobalt nitrate was added in varying concentrations. Liu et al. [102] reported a 56.6% increase in the total lipid content in C. vulgaris at five varying Fe3+ concentrations.
Nutrient stress is a practical and promising strategy exploited by researchers and industries to modify and regulate the biochemical pathways for lipid production and accumulation in microalgae [107]. During the early stages of microalgal growth, nutrient-rich media lead to enhanced biomass productivity. However, deficiency of nutrients during the later stages of growth has detrimental effects, leading to the lipid stock up. During nitrogen deficiency, most microalgae exhibit enhanced lipid synthesis (TAGs) and protein biodegradation. The lipid enhancement mechanism induced by nutrient stress is not understood properly. Yet, nitrogen deficiency stimulates acyl hydrolase and phospholipid hydrolysis, demonstrating a reduction in the cellular content of thylakoid membranes and protein synthesis, ultimately reducing cell growth [108,109], thereby compromising the microalgal growth, biomass yield, and consequently affecting the lipid productivity [110]. Many studies investigated different species of microalgae for various nutrient deficiencies. In the growth media, nitrogen may be supplied in the form of nitrates, urea, and ammonium salts. The utilization of these nitrogen forms by microalgae might differ. Ammonia can be directly converted to amino acids, thus microalgae use it more efficiently than the other forms of nitrogen [43,111]. Changing the nitrogen source might cause a change in the amount of lipid accumulation and fatty acid composition. Metal ions also have numerous physiological functions influencing the metabolism and lipid accumulation of microalgae. Ca2+ is engaged in the signaling of environmental and developmental stimuli. Mg2+ is involved in triggering and mediating various biochemical reactions, i.e., regulating carbon fixation in chloroplasts in the Calvin cycle. Increasing Mg2+ can help Acetyl-CoA carboxylase, the key regulator of fatty acid synthesis, to enhance the neutral lipid content in microalgae.
Table 6. Different microalgae responses to nutrient stress.
Table 6. Different microalgae responses to nutrient stress.
MicroalgaeStress ConditionResultReference
Nannochloropsis oculata
Chlorella vulgaris
Nitrogen deficiency15.31% lipid yield for N. oculata and 16.41% for C. vulgaris[42]
Nannochloropsis sp. F&M-M24Nitrogen-deficient conditionLipid productivity of 204 mg L−1 d−1[90]
N.oceanica
DUT01
Nitrogen-rich condition31 mg L−1 d−1 lipid productivity[45]
Microcystis panniformis
Microcystis novacekii
Phosphorus and nitrogenLipid accumulation had an inverse and direct correlation with nitrogen and phosphorus concentration[100]
Dunaliella tertiolectaNitrogen10 folds increased nitrogen led to lipid productivity of 47.4 mg L−1 d−1 and content of 33.5%[101]
Chlorella vulgarisHigh iron3–7 folds enhanced lipid accumulation[102]
Ankistrodesmus falcatus3–6 mg L−1 iron3 mg L−1 decreased the lipid content and productivity whereas 6 mg L−1 enhanced lipid content and productivity[46]

3.3.5. Effect of Salinity Stress

Salinity stress in microalgae causes a difference in osmotic pressure, generating a stress response that alters their metabolic activity [112]. Different microalgae’s response to salinity stress has been summarized in Table 7. Rao et al. [113] illustrated a 1.7–2.25-fold increase in palmitic acid’s relative quantity and a 2-fold increase in oleic acid at high salinity concentration (34 mM and 85 mM) for Botrycococcus braunii. Sharma et al. [114] reported that varying salt concentration in the microalgal growth medium increases the total lipid content and alters the lipid composition. Bartley et al. [115] studied the effect of salinity stress on the growth of Nannochloropsis salina. They examined it at a salt concentration of 34, 46, and 58 PSU. They reported the highest total fatty acid content of 36% dry tissue mass at 34 PSU. Salama et al. [44] observed the maximum lipid content of 37% and 34% for Chlamydomonas Mexicana and Scenedesmus obliquus, respectively, at a 25 mM NaCl concentration. They also reported the dominant fraction of fatty acids as linoleic acids (41%) and oleic acids (41%). Figler et al. [116] reported on the halotolerant species Coelastrum morus, which could thrive at 1000 mg L−1 NaCl and remove a significant amount of nitrate in media with different N:P ratios and salt concentrations, although the growth of the species was negatively affected.
Pandit et al. [117] reported that the maximum amount of lipids was 49% and 43% for C. vulgaris and Acutodesmus obliquus, respectively, at a concentration of 0.4 M NaCl, whereas Chokshi et al. [118] observed 33.40 ± 2.29% lipid accumulation at 200 mM NaCl for Acutodesmus dimorphus, which enhanced up to 43% when salinity stress extended up to 3 days. Srivastava et al. [119] studied the effect of lipid accumulation in microalgae with different salts (NaCl, KCl, MgCl2 and CaCl2). They reported that CaCl2 had the maximum effect on lipid production, improving up to 40.02% and 44.97% in Chlorella sorokiniana CG12(KR905186) and Desmodesmus GS12(KR905187), respectively, thereby indicating that Ca2+ demonstrates an authoritative function in cell signaling under salinity stress leading to an enhancement in lipid synthesis.
Hence, the addition of salts is a simple, efficient strategy to enhance lipid accumulation while reducing non-target microalgae invasion, as salts perform a vital function in the physiological and biochemical pathways of growth and fatty acid metabolism in microalgae.

4. Integration of Wastewater Treatment, Enhanced Biomass, and Lipid Production Strategies

Microalgae cultivation for simultaneous lipid production and wastewater treatment is a sustainable and economical route (Figure 2). Various sources of wastewater are utilized for the cultivation of microalgae. The various sources of wastewater include but are not limited to; domestic wastewater [120], industrial and agro-industrial wastes [121], swine wastewater [122], and stabilization lagoon from sanitation facilities [123]. Several previous studies have demonstrated either biomass productivity or enhanced lipid productivity in addition to wastewater treatment. Nevertheless, many studies now integrate wastewater treatment and enhanced biomass and lipid production strategies. Fields et al. [124] stated that high lipid productivity could be attained by a high concentration of inorganic carbon and nutrient stress. When light is sufficient, and nitrogen is deficient, photosynthetic carbon fixation continues while growth ceases. This, consequently, enhances the C:N ratio and TAG productivity.
Zhou et al. [125] identified different microalgae capable of growing in concentrated municipal wastewater at a light intensity of 50 μmol m−2 s−1. They observed that Chlorella sp., Heynigia sp., Hindakia sp., Micractinium sp. and Scenedesmus sp. could adapt to the concentrated municipal wastewater. Additionally, high growth rates (231–275 mg/L/d) and higher lipid content (28.9–33.5%) compared with other species were witnessed. They concluded that the microalgae that showed high biomass productivity and lipid content could acclimatize themselves to the concentrated municipal wastewater and lighting conditions provided for their growth, lipid enhancement, and nutrient removal. In another study, Li et al. [126] investigated the effect of light intensity on biomass accumulation, wastewater treatment, and biodiesel productivity for Chlorella kessleri and Chlorella protothecoide. The optimum light intensity for C. kessleri and C. protothecoide was 120 µmol m−2 s−1 and 30 µmol m−2 s−1, respectively. They reported the highest biodiesel content of 24.19% and 19.48% C. kessleri and C. protothecoide, respectively, with the main components being 16-C and 18-C FAME.
Cabanelas et al. [127] evaluated the growth of microalgae using domestic wastewater amended with glycerol. The best results were attained with the highest glycerol supplementation (50 mM) when aerated with 2.5% CO2, photoperiod of 12:12 light/dark cycles, the luminance of 174 μE/m2/s and incubation at 25 ± 1 °C. At this condition, Chlorella vulgaris and Botryococcus terribilis showed biomass productivity of 118 and 282 mg L−1 d−1, which produced about 18 and 35 mg L−1 d−1 lipids, respectively.
Aketo et al. [29] observed the lipid productivity of various microalgal strains in municipal wastewater. They reported Parachlorella kessleri NKG021201 removed 99% nitrogen and 82% phosphorous from the wastewater along with 101 ± 1 mg/L/d biomass productivity and 39 ± 1% lipid content. P. kessleri NKG021201 was cultured again at optimal culture conditions in municipal wastewater to further enhance the biomass productivity and lipid content. The biomass productivity and lipid content enhanced to 147 ± 1 mg/L/d and 56 ± 1 mg/L/d, respectively, when the culture condition was changed to 1% NaCl, 0.8 L/L/min aeration with 4% CO2, 30 °C and continuous illumination at 200 μmol/m2/s. Singh and Ummalyma [128] observed enhanced biomass (450 mg L−1) and lipid yield of 129 mg L−1 (28%) when Chlorococcum sp. SL7B was grown in river water contaminated with pharmaceutical effluent. The Chlorococcum sp. SL7B was maintained at 26 ± 2 °C, 40.5 μmol photons m−2 s−1 at a light/dark cycle of 14:10 h. They concluded that microalgae grown on polluted river water exhibited enhanced biomass and lipid production along with organic pollutant removal.
The utilization of microalgae for the treatment of wastewater is known as phycoremediation. Usually, the wastewater stream has a high content of nutrients and organic matter, but wastewater sources have varying nutrient concentrations which may be toxic to microalgae. Collos and Harrison [129] examined the effect of nitrogen concentration from ammonia on six microalgae classes. For Chlorophyceae they exhibited an optimal concentration of 7600 μM and toxic concentration of 39,000 μM. Improvement in nutrient tolerance can be achieved by strains acclimation in culture media. Moreover, they concluded that further research is necessary as ammonium and ammonia toxicity can vary with other parameters (light, pH, temperature). Silambarasan et al. [21] reported that for the consortium of Chlorella sp. and Scenedesmus sp. when grown in 75% diluted wastewater, the highest biomass of 1.78 g L−1 and lipid content of 34.83% dry cell weight were obtained. The reported algal consortium was proficient in removing 96% nitrate removal, 98% ammonium, 95% phosphate, and 94% total nitrogen from the 75% diluted wastewater. Han et al. [22] observed that 0.33–0.38 g L−1 of total lipid was yielded by Scenedesmus obliquus when cultivated in municipal wastewater along with 98.9–99.8% of nitrogen removal and 83.1–97.6% of phosphorus removal. Scenedesmus obliquus was supplied with 14,500 lx light intensity, 97 mg L−1 nitrogen, 11 mg L−1 phosphorus, and 9.8% CO2.
Several studies used pretreated or raw industrial wastewater for microalgae growth [123,130]. However, a few studies also suggested that microalgae may be utilized as a tertiary treatment to eliminate residual organic and inorganic effluent contamination [131]. Either way, both wastewater treatment and lipid concentration in microalgae can be obtained.
Microalgae biorefineries corresponds to an effective green strategy for synchronous wastewater treatment and bioenergy production [132,133,134]. Silkina et al. [135] developed a bio-refinery approach cultivating up to 1.5 m3 Nannochloropsis oceanica biomass in pilot scale where they witnessed 99% of nitrogen and phosphorus uptake by microalgal cultures. A similar pilot scale biorefinery approach was conducted with Nephroselmis sp. KGE8, Acutodesmus obliquus KGE 17 and Acutodesmus obliquus KGE32 microalgae [136]. In a pilot scale study of integrated biofuel production and wastewater treatment, the process simulation provided an estimated 82.77–140.58 tons/ha/year CO2 sequestration with 63–107 tons/ha/year potential biomass production. The integrated process was reported to significantly enhance the energy balance and economics of the wastewater treatment plant [137].
Therefore, it can be concluded that a proper microalgae strain should be acclimated in wastewater integrated with the favorable lipid enhancement strategies and culture conditions to simultaneously treat wastewater and enhance biomass and lipid productivity for biofuel production.

5. Conclusions and Future Recommendation

Microalgae are efficient organisms for wastewater treatment, and when combined with proper culture conditions, humankind can reap benefits such as high biomass and lipid productivity. Diverse microalgae have diverse optimal culture conditions. It is essential to comprehend the intricacies and flexibilities of the culture condition. Synchronizing the culture condition can facilitate maximizing biomass production and lipid accumulation in conjunction with wastewater treatment. It is crucial to adopt a less expensive and efficient sustainable culture media to reduce cultivation costs. Thus, this review provided insight on the influence of culture media and conditions to address synchronous microalgae biomass and lipid enhancement and phycoremediation. Most of the reviewed studies presented are investigations either on lipid enhancement or wastewater treatment by microalgae; there are very few studies available on synchronous microalgal lipid enhancement and wastewater treatment. Laboratory and pilot scale examinations and economic feasibility analyses to address synchronous microalgae biomass and lipid enhancement are essential to substantiate its application.

Author Contributions

Conceptualization, M.M. and V.B.B.; writing—original draft preparation, V.B.B.; writing—review and editing, V.B.B. and M.M. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Institutional Review Board Statement

Not applicable

Informed Consent Statement

Not applicable

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Pictorial representation of the functioning of microalgae for wastewater treatment and biofuel production.
Figure 1. Pictorial representation of the functioning of microalgae for wastewater treatment and biofuel production.
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Figure 2. Showing the stepwise selection of proper conditions for enhanced biomass and lipid productivity.
Figure 2. Showing the stepwise selection of proper conditions for enhanced biomass and lipid productivity.
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Table 1. Previous studies on microalgae cultivated in wastewater.
Table 1. Previous studies on microalgae cultivated in wastewater.
MicroalgaeWastewaterResultsReference
Chlorella sp. UMN271Swine manure-basedBiomass productivity ranged from 8.08–14.59 g/m2 × day and lipid content of 1.77–3.55%[9]
Desmodesmus sp. S1Oil refineryBiomass and lipid content were found to be 2.98 g/L and 21.95%, respectively[10]
Chlorella vulgarisPulp and aquacultureBiomass productivity of 187 mg/L/d and lipid content of 9.07%[11]
Mix consortiumCarpet mill treatedBiomass productivity of 41 mg/L/d and
lipid content of 12.2%
[12]
Chlorella pyrenoidosaSoybean processingBiomass productivity of 0.64 g/L/d[13]
Chlorella vulgarisTertiary-treated domesticBiomass productivity of 197 gL−1 and lipid productivity of 0.164 gL−1[14]
Scenedesmus bijuga6% effluent from poultry litter anaerobic
digestion
Biomass productivity of 31–76 mg/L/d[15]
Chlamydomonas sp.
TAI-2
Untreated industrialBiomass yield of 1.5 g/L[16]
Desmodesmus sp.MunicipalBiomass productivity of 500 mg/L/d and lipid content of 3.3%[17]
C. sorokinianaDomestic wastewater with urea
supplementation
Biomass productivity of 200 mg/L/d and lipid content of 61.52%[18]
Scenedesmus obliquus
Chlorella sorokiniana
Ankistrodesmus falcatus
AquacultureA. falcatus showed the highest biomass productivity (160.79 mg L−1 d−1) and lipid productivity (57.72 mg L−1 d−1)[19]
Desmodesmus spp.
S. obliquus
Municipal wastewater with different leachate33% increase in lipid content[20]
Chlorella sp.Municipal wastewaterLipid content of 34.83%[21]
Scenedesmus obliquusMunicipal wastewater0.33–0.38 g L−1 of total lipid[22]
Table 2. Different microalgae responses to various stress conditions.
Table 2. Different microalgae responses to various stress conditions.
MicroalgaeMediaStress ConditionResultReference
Desmodesmus spp.Municipal wastewater with leachateIntensity of 53 µmol/m2/s and light cycles of 12:12.
High ammonia concentration (≥167 mg/L)
Biomass productivity of 1.95 g/L and lipid content of 20%[20]
P.kessleri NKG021201Municipal wastewaterIllumination at 40 mmol/m2/s at 25
°C
Biomass productivity of 125 ± 8 mg/L/d and lipid content of 38 ± 1%[29]
Nannochloropsis oculate
Chlorella vulgaris
Bold’s Basal Medium for C. vulgari
f2 for N. oculata
20 °C for N. oculata and 30 °C for C. vulgaris
Nitrogen deficiency
CO2 contained in air (about 300 ppm)
Lipid yield enhanced to 15.31% for N. oculata and 16.41% for C. vulgaris[42]
Scenedesmus sp.BG11Light intensity of 55–60 μmol photon·m−2 s−1, light/dark ratio of 14:10 at 25 °C
Phosphate
deficiency
Lipid accumulation of 53%[43]
C. mexicana GU73240
S. obliquus HM103382
Bold basal mediumIllumination at 40 μmol (photon)/m2s at
27 °C for 20 days
Increased NaCl dose
Highest dry weight (0.8 and 0.65 g/L) and lipid content (37 and 34%) of C. mexicana and S. obliquus repectively[44]
N. oceanica
DUT01
f/2 seawater
BG 11
14/10 h light/dark cycle under an intensity of 60 μmol m−2 s−1 at 25 °C
2% CO2
Nitrogen rich
Lipid productivity of 31 mg L−1 d−1[45]
Ankistrodesmus falcatusBlue-Green (BG11) mediumPhoton flux of 120 μmol m−2 s−1, under a 16 h:8 h light dark cycle at 25 °C
Iron sufficient
and deficient
At 3 mg L−1 the lipid content and productivity decreased whereas lipid content and productivity enhanced at 6 mg L−1 iron concentration[46]
Chlorella vulgaris
Chlorella kessleri
Scenedesmus obliquus
Secondary treated urban wastewaterIllumination of 143 μmol·m−2·s−1 and 14/10 light/dark cycle at 20 ± 1 °C
4% CO2
Scenedesmus obliquus yielded the highest biomass concentration (1.4 g/L) and lipid content (36.75%)
C. vulgaris reached the highest biomass productivity (0.107 g/L·d) followed by S.obliquus (4.4 mg Total N/L·d)
[47]
Mixed consortium mainly consisted ofChlorella sp.Mixed waste streams (liquid digestate obtained after the filtration of the compost, liquid coming from the septic system sludge treatment plant and an effluent coming from the wastewater treatment plant)Photoperiod of 12:12 h at 20 °C
CO2 supplemented at a rate of 0.2 volume of air per volume of medium per minute (vvm).
Biomass productivity (105.2 mg⋅L−1⋅d−1) was negatively affected by CO2 addition and positively affected by light intensity.
Higher lipid contents (17.2%) were found at low light intensity
[48]
C. protothecoides
UTEX-256
Pretreated dairy wastewater5% CO2 was supplied
light intensity was 150 μmol m−2 s−1 for 9 days
40% pretreated whey was most productive for biomass and lipid fractions, respectively, 4.54 and 1.80 gl−1 with daily productivities 0.50 and 0.20 gl−1d−1[49]
Chlorella vulgarisChicken waste compost mixed with tap water1 day of nutrient starvation with 6 g/L of salinity stress at darkLipid content was recorded at 40.28%[50]
Chlorella vulgarisBG11 mediumIllumination at 135 μmol photon m−2 s−1 at 25 °C
low concentration of Cr(VI)
Biomass productivity of 28.3–35.9 mg L−1 d−1[51]
Table 3. Different microalgae responses to light conditions.
Table 3. Different microalgae responses to light conditions.
MicroalgaeStress ConditionResultReference
Botryococcus braunii KMITL 2Light intensities of 200 and 538 μE −2 s−1More lipid accumulation than lower light intensity of 87.5 μE m−2 s−1[30]
Phaeodactylum tricornutumLight intensity of 60 µmol photons m−2 s−1TAG yield of 112 mg molph−1[31]
Nannochloropsis sp.100 µmol m−2 s−1 light intensity photoperiod of 18 h light: 6 h dark cycleEnhanced lipid accumulation of up to 31.3%[52]
Chlorella sp. L1400 µmol photon m−2 s−1 light intensity51.4 mg L−1 d−1 lipid productivity[55]
Nannochloropsis sp.Light intensity of 700 μmol photons/m2/sEnhanced lipid content (47% of dry weight)[56]
Scenedesmus sp.143 μmol·m−2·s−1 and 14/10 light/dark cycle at 20 ± 1 °CLipid accumulation enhanced[57]
Chlorella vulgarisLight intensity of 560 μE m−2 s−192.89% enhanced lipid yield[59]
Scenedesmus obliquus200–1500 μmol photons/m2/s light intensityLipid content remained the same[60]
Table 4. Different microalgae responses to the effect of temperature.
Table 4. Different microalgae responses to the effect of temperature.
MicroalgaeStress ConditionResultReference
N. oculata
C. vulgaris
20–25 °CIncreased temperature decreases lipid content in C. vulgaris and increases lipid production for N.oculata[42]
Mixed microalgae culture30 °C5-fold rise in neutral lipid[70]
Monoraphidium consortiums
Desmodesmus quadricauda
13 °CAids in lipid accumulation[71]
Nannochloropsis limnetica22 °Chighest growth and lipid productivity was observed[72]
Heterochlorella luteoviridis22–27 °C40.7% of PUFAs at a temperature of 22 °C, whereas 52.9% saturated fatty acids increased at 27 °C[73]
Scenedesmus sp. LX1.10–25 °CEnhanced lipid build-up at low temperature[43]
Scenedesmus sp. LX130 °CMost of the fatty acids saturated[68]
Table 5. Different microalgae’s response to varying CO2 concentration.
Table 5. Different microalgae’s response to varying CO2 concentration.
MicroalgaeStress ConditionResultReference
N. oculata2% and 15% CO2Lipid productivity of 142 and 82 mg L−1 d−1[78]
Nannochloropsis sp.15% CO2Increased biomass productivity (0.39–1.43 gL−1) and growth rate (0.33–0.52 d−1)[14]
Ettlia sp. YC00110% CO23.1 g L−1 cell density and 80.0 mg L−1 d−1 lipid productivity[79]
C. vulgaris8% CO229.5 mg L−1 d−1 lipid productivity[80]
Chlamydomonas sp.
JSC4
4% CO2169.1 mg L−1 d−1 lipid productivity[81]
Scenedesmus Obliquus15% CO2850 mg/L of lipid in 16 days[82]
Tribonema
minus
(0.03–20%) CO2Reduced lipid productivity with increased CO2[83]
Table 7. Different microalgae responses to salinity.
Table 7. Different microalgae responses to salinity.
MicroalgaeStress ConditionResponseReference
Botrycococcus braunii
N. oculata
Salinity concentration of 34 mM and 85 mM1.7–2.25-fold increase in palmitic acid and 2-fold increase in oleic acid at 34 mM and 85 mM for B. braunii. For N. exican, rise in temperature led to an enhanced lipid production by 2-fold[113]
Nannochloropsis salinaSalt concentration of 34, 46, and 58 PSUHighest total fatty acids content of 36% dry tissue mass at 34 PSU[115]
Chlamydomonas mexicana Scenedesmus obliquus25 mM NaClMaximum lipid content of 37% and 34% for C. mexicana and S. obliquus[44]
C. vulgaris
Acutodesmus obliquus
0.4 M NaClHighest growth and lipid productivity was observed[117]
Acutodesmus dimorphus200 mM NaCl33.40 ± 2.29% lipid accumulation[118]
Chlorella sorokiniana CG12(KR905186)
Desmodesmus GS12(KR905187)
NaCl, KCl, MgCl2 and CaCl2CaCl2 improved up to 40.02–44.97% in Chlorella sorokiniana CG12(KR905186) and Desmodesmus GS12(KR905187)[43]
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Barua, V.B.; Munir, M. A Review on Synchronous Microalgal Lipid Enhancement and Wastewater Treatment. Energies 2021, 14, 7687. https://doi.org/10.3390/en14227687

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Barua VB, Munir M. A Review on Synchronous Microalgal Lipid Enhancement and Wastewater Treatment. Energies. 2021; 14(22):7687. https://doi.org/10.3390/en14227687

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Barua, Visva Bharati, and Mariya Munir. 2021. "A Review on Synchronous Microalgal Lipid Enhancement and Wastewater Treatment" Energies 14, no. 22: 7687. https://doi.org/10.3390/en14227687

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Barua, V. B., & Munir, M. (2021). A Review on Synchronous Microalgal Lipid Enhancement and Wastewater Treatment. Energies, 14(22), 7687. https://doi.org/10.3390/en14227687

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