REVIEW article

Front. Bioeng. Biotechnol., 20 August 2024

Sec. Industrial Biotechnology

Volume 12 - 2024 | https://doi.org/10.3389/fbioe.2024.1387519

Usage of Chlorella and diverse microalgae for CO2 capture - towards a bioenergy revolution

  • 1. National Institute of Oceanography and Fisheries (NIOF), Cairo, Egypt

  • 2. Animal and Fish Production Department, College of Agricultural and Food Sciences, King Faisal University, Al-Ahsa, Saudi Arabia

  • 3. Department of Fish and Animal Production, Faculty of Agriculture (Saba Basha), Alexandria University, Alexandria, Egypt

  • 4. Water and Environment Study Center, King Faisal University, Al-Ahsa, Saudi Arabia

  • 5. Department of Botany and microbiology, Faculty of Science, Tanta University, Tanta, Egypt

Abstract

To address climate change threats to ecosystems and the global economy, sustainable solutions for reducing atmospheric carbon dioxide (CO2) levels are crucial. Existing CO2 capture projects face challenges like high costs and environmental risks. This review explores leveraging microalgae, specifically the Chlorella genus, for CO2 capture and conversion into valuable bioenergy products like biohydrogen. The introduction section provides an overview of carbon pathways in microalgal cells and their role in CO2 capture for biomass production. It discusses current carbon credit industries and projects, highlighting the Chlorella genus’s carbon concentration mechanism (CCM) model for efficient CO2 sequestration. Factors influencing microalgal CO2 sequestration are examined, including pretreatment, pH, temperature, irradiation, nutrients, dissolved oxygen, and sources and concentrations of CO2. The review explores microalgae as a feedstock for various bioenergy applications like biodiesel, biooil, bioethanol, biogas and biohydrogen production. Strategies for optimizing biohydrogen yield from Chlorella are highlighted. Outlining the possibilities of further optimizations the review concludes by suggesting that microalgae and Chlorella-based CO2 capture is promising and offers contributions to achieve global climate goals.

1 Introduction

Global warming and greenhouse gas emissions significantly affect world energy, sustainability, and development (Lokuge and Anders, 2022). Climate change is a major threat that hinders the survival of various plants, animals, and human progress, as well as the wellbeing of our planet. The increased emissions of various greenhouse gases (GHGs), such as carbon dioxide (CO2), methane (CH4), nitrous oxide (N2O), sulfur dioxide (SO2), and fluorinated gases have worsened current climate changes, emphasizing the need to reduce CO2 emissions and promote the use of renewable sources, particularly fuels (). Globally, CO2 accounts for 76% of total GHGs, mostly (72%) released by the energy production sector. In 2019, it reached approximately 33 gigatons. In the first quarter of 2020 compared to the first quarter of 2019, global CO2 emissions decreased by 5% due to a decline in the demand for coal, oil, and natural gas (8%, 4.5%, and 2.3%, respectively). This decrease in CO2 emissions in 2020 was largely caused by the COVID-19 pandemic, the largest decline since World War II (Nguyen et al., 2021).

The amount and concentration of CO2 vary depending on the source of the emission. For instance, flue gas of power plants is about 3%–4%, while coal-fired plants emit about 10%–13%. CO2 from bio-refineries can reach up to 80% (Prasad et al., 2021). Globally, atmospheric CO2 has increased from 313 ppm in 1960 to 411 ppm in 2020 and is projected to reach 450 ppm by 2035 (). Some scenarios predict an increase of up to 700 ppm in the future, which would result in a 99% probability of a 2 C rise in global warming and significant damage to the global economy (van Leeuwen et al., 2024). The reduction of CO2 emissions is a top concern for the world. It is essential to develop a plan to lower or stabilize CO2 levels in the atmosphere. Many countries have committed to reducing greenhouse gas emissions through international agreements such as the Kyoto Protocol (1997) and the Paris Agreement (2015). According to a study by Prasad et al. (2021), there are two main approaches to reducing CO2 emissions: i) decreasing the consumption of fossil fuels by increasing the use of renewable energy sources, and ii) capturing and storing CO2 through various biological, chemical, or physical methods. Osman et al. (2021) identified three primary strategies for CO2 capture, storage, and utilization: pre-combustion, post-combustion, and oxyfuel combustion technologies. Although significant research has been conducted on how to reduce CO2 emissions through physical and chemical means, there are numerous limitations, including environmental, technical, and economic factors. It is acknowledged that the scope of Carbon Capture and Utilization (CCU) technologies that directly use captured CO2 in industrial processes is limited and their impact on reducing emissions is minimal (Shreyash et al., 2021). Accordingly, it is essential to find appropriate, sustainable, and profitable approaches for capturing CO2 that reduce atmospheric CO2 levels more effectively than physical and chemical methods (Prasad et al., 2021).

Among CO2 capture, utilization, and storage technologies (CCUS), biological CCUS is the most economical and environmentally friendly option, relying mainly on sunlight and photosynthetic organisms such as aquatic and terrestrial plants (Nunez, 2019). The sun provides nearly infinite energy, with our planet receiving 100,000 terawatts annually compared to our current energy consumption of 15 terawatts, which is expected to increase to 24 TW y−1 by 2030 and 45 terawatts by the end of the century. It is a huge amount of energy compared to our current energy consumption (). Although our current energy consumption is 15 TW y−1, and it is expected to increase to about 24 TW y−1 by 2030, and 45 TW y−1 by the end of this century, the energy received from the sun is more than 2,200 times that of our energy consumption (Gerotto et al., 2020). Photoautotrophic organisms convert CO2 into carbon-based compounds including sugars, proteins, and lipids with the use of water and sunlight (). Worldwide, photoautotrophic organisms, both aquatic and terrestrial plants, can store solar energy at a rate of 120 terawatts every year (). That means that the annual capacity of photoautotrophic organisms to store energy in photosynthetic products exceeds the current global energy demand by 800%. Therefore, the extensive culture of these organisms is an important potential solution to cover a large part of world energy demand (Stephenson et al., 2011).

Among biological CCUS options, microalgae systems have emerged as a particularly promising route for atmospheric CO2 capture due to their high efficiency, scalability, and potential to generate valuable co-products. Through the process of photosynthesis, photoautotrophic organisms consume atmospheric CO2 and convert it into useful biomass, food, and bioactive compounds that are valuable in various industries. Despite their slow growth rate, terrestrial plants’ ability to capture CO2 is estimated to contribute only 3%–6% of fossil fuel emissions (). In contrast, the faster growth rate of microalgae allows them to fix CO2 at a rate 10–50 times higher than that of terrestrial plants (Figure 1).

FIGURE 1

Nunez (2019) identifies various strategies to decrease global CO2 emissions, including widespread microalgae cultivation (especially in photobioreactors), tree planting, preserving grasslands and forests, improving energy efficiency, and boosting clean energy production. The terrestrial plants store energy mainly in the form of lignocellulose, a complex biopolymer that is challenging to utilize as a sustainable renewable feedstock. Aquatic plants, on the other hand, do not contain lignin, which makes it simple to use them in a variety of applications without requiring lengthy processing (Osman et al., 2023a). Additionally, the simultaneous synthesis of beneficial bioproducts such as lipids, proteins, carbohydrates, pigments, vitamins, and polyunsaturated fatty acids is possible in large quantities in aquatic plants. This multi-benefit of microalgae has garnered increasing interest in the field, as highlighted by the growing attention to microalgal CO2 bio-fixation and resource utilization in recent years (Lim et al., 2021). The multifaceted nature of these bio-products underscores the potential for comprehensive and sustainable applications in various industrial sectors.

Fixation of CO2 from the atmosphere by photoautotrophic organisms is achieved through the C3 and C4 pathways. Nevertheless, some microalgae have been found to have a higher capacity for CO2 capture compared to terrestrial C4 plants (Hong, 2022). CO2 capture projects by microalgae are currently viewed as highly attractive to investors for several reasons. According to the statistics report of the Food and Agriculture Organization (), the global microalgae biomass production was 56,465 tons in 2019, with China accounting for 97.16% of the production, followed by Chile (1.6%), France (0.37%), Greece (0.25%), Tunisia (0.25%), Burkina Faso (0.25%), Central African Republic (0.09%), Chad (0.04%), Bulgaria (0.005%), and Spain (0.003%). Spirulina (Arthrospira sp.) represents 96.56% of the global microalgae biomass production, while Haematococcus pluvialis (0.429%), Chlorella vulgaris (0.008%), Tetraselmis sp. (0.003%), and Dunaliella salina (0.0004%) contributed the rest ().

Microalgae contribute more than 90% of the primary production in marine ecosystems and fix about 50 gigatons of CO2 annually (Sommer et al., 2002). According to the study Kadam (2001), a 1,000-ha microalgae open pond (raceway) system could reduce CO2 emissions from flue gases by 50%, or 2,10,000 tons y−1 out of the 4,14,000 tons produced by a 50 megawatts power station. The CO2 absorbed by microalgae is converted into high-nutritional and economically valuable organic bioactive compounds (Zhou et al., 2022). As a result, algae industries have attracted the attention of investors worldwide for the potential use of algae for CO2 fixation and absorption (Zhang and Liu, 2021) and for using its biomass as raw material for various bioindustries, such as aqua-feed, biofertilizers, bioenergy, human food supplements and pharmaceuticals, and wastewater treatment (Mansour et al., 2022a; Mansour et al., 2022b; ; ; ). Microalgae have attractive CO2 capture potential and high biomass productivity. Microalgae have a CO2 capture potential of 1.6–2 tons per year and a biomass productivity of 127–300 tons per hectare per year. The biomass productivity of microalgae can be significantly increased with advanced culture, harvest, and, drying technologies (). The review by Klinthong et al. (2015) concluded that the increasing global interest in microalgae for CO2 capture and the production of various renewable energies is due to several advantages over terrestrial plants. These advantages include 1) high fixation of atmospheric CO2, 2) high conversion rate of the photosynthetic process, 3) rapid growth and production rate, 4) high potential for environmental phytoremediation, 5) capacity to produce various biomass and bioenergy resources, and 6) no competition with food and agricultural products. Thus, these advantages make microalgae a promising solution to reduce atmospheric CO2 levels and produce bioenergy (Klinthong et al., 2015). With microalgae emerging as prime candidates for efficient and scalable biological CO2 capture, ongoing research is quantifying the real-world potential of large-scale microalgae cultivation systems. A recent techno-economic evaluated various cultivation and harvesting scenarios, capturing 102.13 tons CO2/year/ha with operating costs ranging from $4.75–6.55/kg dry biomass (Valdovinos-García et al., 2020).

In alignment with the overarching objective of exploring CO2 mitigation strategies, this review discusses microalgae as a promising renewable feedstock for producing sustainable biofuels and other bioproducts due to their high biomass productivity, ability to utilize CO2, and potential for integration into biorefinery systems. The review will also include research on the usage of microalgae to produce renewable biohydrogen. The allure of biohydrogen lies in its potential as an energy-dense transportation fuel, poised to deliver substantial offsets in CO2 emissions while simultaneously fostering the generation of sustainable energy. As the examination continues, this review also examines current carbon credit projects, providing an overview of their feasibility in achieving global climate goals by 2050. The novelty of this study lies in its focus on utilizing microalgae for renewable bioenergy production, especially biohydrogen, as a sustainable and carbon-neutral energy source, thereby mitigating CO2 emissions and fostering clean energy generation.

2 Carbon pathways in microalgal cells

Microalgae have unique carbon pathways that enable them to take in carbon dioxide and produce oxygen through photosynthesis. Studying these pathways can provide valuable information on the functioning of aquatic plant projects in CO2 capture. Photosynthetic cells exchange CO2 and oxygen (O2) through their cell walls during photosynthesis. To assess the efficacy of capturing atmospheric CO2 into microalgal cells, it is crucial to examine their carbon pathways (Gehl et al., 1987). Microalgae capture approximately 50 gigatons of CO2 from the atmosphere annually, accounting for more than 50% of all photosynthetic activity worldwide. However, microalgae face three challenges in capturing and fixing CO2, as described by the study by Moroney and Ynalvez (2007). First, the enzyme Rubisco, which plays a crucial role in photosynthesis, has a poor CO2 affinity and operates at only 25% of its catalytic capacity due to the lower concentration of dissolved CO2 and the competition with O2 at atmospheric CO2 levels. Secondly, CO2 diffuses much slower in water compared to the atmosphere. Therefore, microalgae greatly benefit from the capacity to scavenge CO2 as soon as it becomes accessible. Lastly, the levels of inorganic carbon (Ci = CO2 + HCO3) and pH in the microalgal environment have a significant impact on the availability of CO2 and HCO3- for photosynthesis. When the pH is acidic, most of the available Ci is in the form of CO2, but when the pH is alkaline, the majority of the Ci is in the form of HCO3 (Gehl et al., 1987).

Microalgae, as single-celled photosynthetic organisms, have evolved a specialized pathway to overcome the challenges associated with capturing and fixing atmospheric CO2 through photosynthesis. This pathway is called the Carbon Concentration Mechanism (CCM), and it resembles the C4 and Crassulacean Acid Metabolism (CAM) pathways found in terrestrial plants. The CCM increases the concentration of inorganic carbon several times over the level found in the surrounding environment, thereby enhancing the photosynthetic output of algal cells. To achieve this, microalgae have a specialized plastid structure called pyrenoid, which elevates the CO2 concentration around the thylakoid membranes. This in turn increases the efficiency of the Rubisco enzyme for carbon sequestration and assimilation. The CCM is a unique and innovative adaptation developed by microalgae to increase their ability to absorb and convert atmospheric CO2 into biomass ().

Interestingly, Carbonic Anhydrase (CA) is a zinc-containing metallic enzyme that has been found to play a significant part in the CCM and assist in the fixation of atmospheric CO2 by catalyzing the reversible hydration of CO2 into bicarbonate and a proton. CA assists CO2 fixation by nucleophilic attack by the hydroxide ion that is bound to a zinc atom. CA plays an important role in CO2 acquisition, capture, ion exchange, and photosynthesis. This reaction is followed by the removal of a proton from the protein surface and the ionization of the water molecule linked to zinc, which regenerates the active site. Therefore, the CA task in the fixation of carbon is to transform bicarbonate into CO2, which serves as the substrate for Rubisco, the main enzyme responsible for fixing carbon (Sayre, 2010).

As reported by the study by Prasad et al. (2021) photorespiration causes a loss of energy and carbon, ultimately lowering the rates of photosynthesis. Atmospheric O2 levels strongly exceed the CO2 concentration thus enhancing Rubisco´s oxigenase activity and the subsequent photorespiration. To combat this condition, microalgae have created CO2 concentration mechanisms (CCMs) to increase the levels of CO2 around Rubisco. Several studies have demonstrated different CCM strategies in several microalgae species.

Microalgae have developed CCMs as an adaption to increase the photosynthetic efficiency at low CO2 (Sayre, 2010; Moroney et al., 2013), thus allowing higher growth rates compared to terrestrial plants. As previously reported by the studies by Sayre, (2010); Giordano et al., (2005); Moroney and Ynalvez, (2007), the CCM is mainly based on the C4 and CAM pathways, in which PEP absorbs CO2 to produce oxalic-acetic acid (OAA). To maximize the capture of CO2, this pathway also enables to capture the CO2 produced during photorespiration (Giordano et al., 2005).

However, the CCM strategies differ among various microalgae species. For instance, Chlorella vulgaris utilizes a relatively simpler CCM compared to species like Chlamydomonas reinhardtii and Nannochloropsis oceanica, which have more complex mechanisms involving multiple carbon fixation pathways (Wei et al., 2019). These differences highlight the diversity in CCM strategies among microalgae and their varying efficiencies in CO2 capture and biomass production (Yu et al., 2020).

In a recent study Treves et al. (2022) investigated the 13CO2in vivo labeling kinetics of the Calvin Benson Cycle and the pathways of organic acid, starch, sugar, amino acid, lipid, and protein synthesis in three green microalgae: Chlorella sorokiniana, Chlorella ohadii, and Chlamydomonas reinhardtii. The study also compared the flow patterns in these algal species with data from the C3 and C4 pathways from terrestrial plants. The findings showed unique flow patterns in these microalgae, which resulted in faster autotrophic growth. Furthermore, some species exhibited faster Rubisco regeneration and increased fluxes through reduced glycolysis and anaplerotic pathways to the tricarboxylic acid cycle, lipid synthesis, and amino acid synthesis compared to terrestrial plants. According to the literature, one of the highly-efficient green microalga, Chlorella vulgaris, demonstrated these enhanced metabolic fluxes. Genome-scale models suggest that during mixotrophic culture, there is increased carbon dioxide transport between the plastid and mitochondria in Chlorella vulgaris, accompanied by a 25% and 60% rise in the activity of carbon metabolism subsystems during mixotrophy and heterotrophy, respectively (Zuñiga et al., 2018). Similarly, Chlorella protothecioides exhibits heightened intracellular metabolite concentrations related to enhanced glycolysis and tricarboxylic acid cycle (TCA) activity during heterotrophy (Wu et al., 2015). These elevated TCA activities are associated with increased synthesis of storage compounds like fatty acids and carbohydrates (Vitova et al., 2015), along with species-specific changes in biochemical profiles (Penhaul Smith et al., 2021). The strain ZJU9000 is a stable mutant culture of Arthrospira platensis, produced through 9 kGy gamma irradiation, and exhibits improved growth compared to the wild-type. The study by investigated differences in gene expression between wild-type and ZJU9000 and found that the robust growth of the mutation was due to higher levels of pigment and vitamin production, which improved photosynthesis and cell development. The study also revealed that ZJU9000 had higher CO2 capture at low concentrations compared to the wild-type, due to its enhanced CCM (). These findings were similar to those of other blue-green species like Anabaena sp. and Microcystis aeruginosa.

Among microalgae, marine diatoms are responsible for about 20% of world CO2 fixation (Khan et al., 2009). Like C4 plants, diatom species contain CCMs that utilize biochemical fixation of bicarbonate, but whether the same type of CCM is present in all diatoms is a subject of debate (Yu et al., 2022). The Phosphoenolpyruvate carboxylase enzyme (PEPcase enzyme, the primary enzyme in C4 and CAM pathways) is detected in marine diatom species in two isoforms, one in the plastids (PEPC1) and the other one in the mitochondria (PEPC2). The study by Yu et al. (2022) used several techniques (Western blots, real-time quantitative polymerase chain reaction, and enzymatic assays) to examine the expression and activities of PEPC1 and PEPC2 in Phaeodactylum tricornutum, under several concentrations of dissolved inorganic carbon (low and high). They generated and analyzed individual cell lines of both PEPC1 and PEPC2 of P. tricornutum and also generated and analyzed a double-knockout strain of PEPC1/2. Their findings implemented that, at least some of the CCM in the marine species P. tricornutum depends on the biochemical fixation of bicarbonate that is performed by the mitochondrial form of PEPC2 (Yu et al., 2022).

Dinoflagellates are significant primary producers and a main reason for harmful-toxic algal blooms in the marine ecosystems (). The capture of carbon by dinoflagellates is still poorly understood, despite its enormous ecological importance (). In the study by Zhang et al. (2021), the pathway of carbon capture in a marine dinoflagellate Prorocentrum donghaiense, including in situ and laboratory-simulated bloom conditions, were examined by using several techniques. They observed rapid capture of dissolved CO2 to produce high biomass during bloom. The genes responsible for CO2 capture were highly expressed at low levels of CO2, concluding that the C4 pathway exists in the blooming cells of P. donghaiense. Finally, they concluded that the C4 pathway in this marine dinoflagellate exhibited an important integrated function to assist the capture of CO2 during the bloom.

As reported in the study by Klinthong et al. (2015), the possible pathways of inorganic carbon in microalgae are: (1) direct CO2 capture through the plasma membrane; (2) the use of HCO3 through activating the CA enzyme that converts HCO3 to CO2, and (3) direct transport of HCO3 through the plasma membrane. The different carbon assimilation pathways in some microalgae species are listed in Table 1.

TABLE 1

Microalgae speciesPathway 1 (Direct CO2 capture)Pathway 2 (CA activation)Pathway 3 (Direct HCO3 capture)References
Chlorella saccharophilaEEERotatore and Colman (1991)
Chlorella ellipsoideaEMERotatore and Colman (1991)
Chlorella kessleriiEME
Chlamydomonas reinhardtiiEFESultemeyer et al. (1989)
Nannochloropsis gaditanaMMEHuertas et al. (2000b)
Nannochloropsis oculataMMEHuertas et al. (2000b)
Nannochloris atomusEMMHuertas et al. (2000a)
Nannochloris maculataEMMHuertas et al. (2000a)
Dunaliella terteolectaEEE
Scenedesmus obliquusEEEPalmqvist et al. (1994)
Isochrysis galbanaEEEHuertas et al. (2002)
Phaeodactylum tricornutumEEE
Navicula pelliculosaEMERotatore and Colman (1992)
Cyclotella spEEERotatore et al. (1995)
Ditylum brightwelliiEMEKorb et al. (1997)
Skeletonema costatumEMEKorb et al. (1997)
Chaetoceros calcitransEMEKorb et al. (1997)
Thalassiosira punctigeraEMNR
Thalassiosira pseudonannaNRME
Porphyridium cruentumEEE
Emiliania huxleyiEENR
Dicrateria inornataEEEHuertas et al. (2002)
Phaeocystis globosaEENR
Vischeria stellataEMEHuertas et al. (2002)
Eremosphaera viridisEMMRotatore and Colman (1992)
Amphidinium carteraeEMMHuertas et al. (2002)
Heterocapsa oceanicaEMMHuertas et al. (2002)
Monodus subterraneusEMMHuertas et al. (2002)

Carbon assimilation pathways as reported for selected microalgaea.

a

E: existing; M: missing; NR: not reported.

3 The role of microalgae in CO2 capture for biomass production

The increasing levels of atmospheric CO2, which are attributed to human activities and have caused a major shift in the global carbon cycle, have become a major global concern and a subject of research in recent years (Mondal et al., 2017). Currently, atmospheric CO2 constitutes approximately 77% of all greenhouse gases, making its capture crucial, even with the presence of other greenhouse gases such as hydrocarbons, sulfur dioxide, methane, and nitrogen oxides (Xu et al., 2021). The capture of atmospheric CO2 by microalgae during the generation of biomass along with other valuable carbon compounds, presents a promising solution to the issue of global warming (Iglina et al., 2022). Microalgae have the potential to capture and reduce atmospheric CO2 10–50 times more effectively than terrestrial plants (Li et al., 2008). They also have several other advantages over terrestrial plants, such as not competing for food and feed for humans and animals, using less land and water, and possibility grow in various types of water (Osman et al., 2023b).

The cost of feedstock media used to grow microalgae is significantly impacted by the high amount of CO2 required, which accounts for over 50% of the cost (). Microalgae can efficiently absorb CO2 from both the atmosphere and from flue gas emissions, with capture rates up to 90% reported in open ponds (Sayre, 2010). A novel spraying absorption tower combined with an open raceway pond has demonstrated improved CO2 fixation efficiency of 50%, compared to 11.17% for traditional bubbling methods (Politaeva et al., 2023). As mentioned previously, microalgae have evolved unique mechanisms, such as C4, CAM, and CCM, to improve their efficiency in capturing carbon (). However, the capture rate varies between species due to differences between the CA enzymes. A study by reported that Synechocystis aquatilis, grown in raceways ponds with a water volume of 4,000 m3 and using sunlight, can absorb approximately 2,200 tons of CO2 y−1. The study by () reported that the highest biomass productivity of Chlorella fusca LEB (25 g m−2 d−1) required 45.8 g CO2 m−2 d−1.

Although microalgae biomass has been commercially cultivated for more than 40 years, its entire global biomass per year was only 93,756, 87,000, and 56,465 tons in 2010, 2018, and 2019, respectively (Hamidi et al., 2023). Several reports have indicated that each 1 ton of microalgae biomass (dry weight) captured about 1.88 tons of atmospheric CO2 (), while Chisti reported it as two tones (). However, it is necessary to mention that each algal strain needs to be studied independently. Based on calculations, the equivalent amounts of CO2 captured by cultured microalgae are around 187,500, 174,000, and 112,900 tons of CO2 in 2010, 2018, and 2019, respectively (Iglina et al., 2022).

There are two systems widely used in microalgae cultivation; open pond (OP) and photobioreactor (PBR). In the open systems, there are many challenges facing supplementation and capture of CO2, due to low fixation efficiency (usually between 10% and 40% vol.), low solubility, high cost, significant loss during culture, and poor tolerance to high CO2 levels (Song et al., 2019). The main advantage of using PBR for the capture of CO2 by microalgae is the increase in productivity according to regulated environmental factors and the optimal volume utilization. As reported in the literature, few microalgae species can tolerate CO2 at high levels of 70% vol. such as Chlorella sp. KR-1 and Chlorella ZY-1, 90% vol. CO2 such as Chlorella vulgaris (Li et al., 2013), while others can tolerate CO2 at 100% vol. CO2 such as Chlorella sp. T-1 (Zhang and Song, 2014).

The first published work on increasing microalgae biomass production by providing external CO2 to microalgae culture media was in the 1960s (Heubeck et al., 2007). From this date, many publications have claimed that using an external source of CO2 to supplement the culture medium significantly increases microalgae biomass (Judd et al., 2017). High levels (99.9%) of CO2 may be injected using high-purity gas cylinders. However, this is an expensive technology that can limit the use of the system, especially in open pond systems (), even if it is appropriate for PBR systems. To minimize costs, CO2 can be added to the ponds in the form of exhaust gases. To reduce the price, it would be appropriate to add CO2 to PBRs in the form of compressed exhaust gases to mitigate the yearly increase in CO2 emissions. As reported previously (Zheng et al., 2018), the possible sources of CO2 supplies are air, pure CO2 (commercial grade or purified), raw flue gas, CO2-containing solvents, and HCO3. Each source has advantages and disadvantages.

Several studies () have claimed that adding more CO2 not only tends to make more carbon available for the growth of microalgae, but also enhances the assimilation of nutrients into their biomass, reducing nitrogen losses from ammonia volatilization and phosphorus precipitation, and preventing pH increases brought on by photosynthetic activity. To utilize purified CO2, flue gas, and solvents that contain CO2, it is necessary to have access to point sources of CO2 and terrestrial facilities appropriate for mass microalgae cultivation. Flue gas is widely available and has limited commercial value. However, it also contains impurities that may inhibit microalgae growth. While having a lower cost and less accessibility than flue gas, purified CO2 is the most efficient solution regarding utilization and transport. The energy required to dispense HCO3 or CO2 -loaded solvents is substantially lower than the energy required for compressing and transporting the gas CO2. Bicarbonates are more expensive and scarcer than flue gas, even if it is purer. Furthermore, not all microalgae species can capture bicarbonates. Co-location of algae production sites with a CO2 collection facilities would be favorable for the use CO2-loaded solvents. reported that since CO2 represents the most expensive input needed for microalgae culture in PBR systems, it is remarkable to use exhaust gases in conjunction with wastewater treatment to achieve lower input costs for microalgae. The use of CO2 from exhaust emissions for the growth of microalgae in PBR systems is less expensive than pure CO2. The cost of CO2 is associated with the installation, and maintenance of the PBR system, and the process of CO2 capture and compression, which was estimated to account for 75% of the total costs among the many expenditures associated with the procedure (Van Den Hende et al., 2012). Table 2 summarizes the advantages and disadvantages of each source of CO2, as reported in the literature.

TABLE 2

AirHCO3Commercial grade CO2Purified grade of pure CO2Raw flue gasCO2-containing solvents
CO2 concentration0.042%0.1–5 g L−1 (NaHCO3)> 95%> 95%4% – 33%0.5 mol CO2/mol solvent (20%)
CO2 volume requiredVery highNoneLowLowModerateNone
AvailabilityUnlimitedModerateLowHighHighModerate
CO2 utilizationVery lowVery highHighHighModerateVery high
CO2 cost ($ per ton)03803–5529–111010–35
Energy for compression and transportationNoneLowModerateModerateHighLow
OP injection energyVery highLowModerateModerateHighLow
PBR injection energyNoneLowVery highVery highVery highHigh

Advantages and disadvantages of several potential CO2 sources for microalgae production as reported in the literature (Kadam, 1997; Metz et al., 2005; ; Xu et al., 2014; Rubin et al., 2015; Nayak et al., 2018).

4 Factors influencing CO2 sequestration on an industrial scale

The factors influencing microalgal CO2 sequestration are summarised in Figure 2 and will be treated in detail in the following chapters.

FIGURE 2

4.1 pH

Most microalgae species including Chlorella sp. grow optimally at a neutral to moderately alkaline pH between 7 and 9. For example, the microalgae Chlorella stigmatophora and Nannochloris sp. achieve peak growth rates at pH 8 and 7, respectively (Galès et al., 2020). During photosynthesis, microalgae take up bicarbonate ions, which in turn raises the pH of the aquatic environments (). This photosynthetic alkalinization hinders the dissolution of CO2 from the air and reduces bioavailability for further carbon fixation (Zhou et al., 2017). Low pH levels below 6–7 can also negatively impact cell metabolism and inhibit the active transport systems that allow microalgae to take up essential ions. A pH dropping too far from the ideal neutral range has been shown to reduce the growth rate of species such as Spirulina platensis (Zeng et al., 2011). Different cultivation strategies, such as autotrophic, mixotrophic, and photoheterotrophic, can influence the effect of pH on carbon fixation and carbohydrate accumulation in C. vulgaris JSC-6 (). Autotrophic cultivation resulted in better carbon assimilation and carbohydrate accumulation, while the assimilation of fatty acids in the mixotrophic and photoheterotrophic modes was influenced by pH. Therefore, monitoring and controlling pH is imperative when cultivating microalgae for carbon sequestration, as pH dictates the rate of photosynthesis and cellular activities that allow CO2 to be effectively utilized. Using species adapted to variable pH or actively managing pH through CO2 sparging and buffer addition enables healthy, productive algal cultures. Overall, maintaining an optimal pH range, such as around 8, can enhance carbon fixation and biomass yield in Chlorella. The specific pH requirements may vary depending on the species and cultivation strategy.

4.2 Temperature

Most microalgae species suited for CO2 capture are mesophilic, with an optimal growth temperature range of 25°C–45°C (Farrelly et al., 2013). Temperatures above this range reduce the solubility of CO2 and alter cellular enzyme functions (Prasad et al., 2021). For Chlorella the optimal temperature range strongly depends on the chosen species and other environmental factors. Generally, temperatures between 25°C and 35°C are considered favorable for the growth and carbon fixation of Chlorella (Politaeva et al., 2023). Specifically, moderate temperatures cause the pivotal carbon fixation enzyme Rubisco to bind oxygen instead of carbon dioxide, resulting in photorespiration that lowers CO2 utilization rates by up to 30% (Zeng et al., 2011). Excessively high temperatures can damage the photosynthetic apparatus and reduce overall carbon fixation efficiency (Politaeva et al., 2023). Heat also alters the activity of other enzymes like carbonic anhydrase which interconverts CO2 and bicarbonate, further limiting inorganic carbon bioavailability (Ighalo et al., 2022). Chlorella has the ability to adapt and acclimate to different temperature conditions. Prolonged exposure to specific temperatures can trigger physiological and biochemical changes in allowing Chlorella to better cope with the prevailing temperature and maintain carbon fixation efficiency (Politaeva et al., 2023). Therefore, the cultivation temperature must be controlled for mesophilic species to ensure adequate CO2 dissolution while preventing enzyme impairment and photorespiration.

4.3 Irradiation

Irradiation conditions play a crucial role in regulating the photosynthetic efficiency and CO2 fixation capacity of microalgae. The intensity of light irradiance has a direct impact on the rate of photosynthesis and biomass productivity (Souliès et al., 2016). While higher light intensities can drive faster growth rates initially, excessive irradiance beyond the saturation point can lead to photoinhibition and decreased CO2 fixation. Similarly, the photoperiod, or the daily light/dark cycle duration, influences the microalgae’s ability to balance light energy absorption and dark respiration phases. Optimal photoperiods vary across species but often range from 12–16 h of light per day for efficient CO2 capture (Shareefdeen et al., 2023). Additionally, the spectral quality or wavelength of light can affect photosynthetic performance, with different microalgal pigments exhibiting peak absorption in specific wavelength ranges like blue, red, and green. Tailoring light sources to match the absorption spectra of the target microalgae strain has been shown to enhance biomass yields and CO2 fixation rates. As such, optimizing irradiation parameters like intensity, photoperiod, and spectral composition is crucial for maximizing the potential of microalgae-based CO2 capture systems (Sero et al., 2020).

The minimum irradiation in the range of 10–30 μmol m-2 s-1 is required for microalgae species to effectively uptake CO2 and convert it into biomass through photosynthesis. Light drives the first stage of carbon fixation, so sufficient photon flux density optimizes the growth rate, biomass, and CO2 sequestration potential of microalgae cultures. Outdoor mass cultivation systems should receive over 880 μmol photons m-2s-1 from sunlight for appreciable productivity (Hosseini et al., 2018). Additionally, the efficiency of light absorption depends on the properties of the microalgae cells themselves. Cells with a greater surface area and higher concentrations of light-harvesting pigments such as chlorophyll can absorb more useful radiation. When light becomes limited, adaptive mechanisms, like increasing pigment production become active, as demonstrated in the freshwater microalgae Scenedesmus obliquus (Wu et al., 2023). Another study showed a microalgal consortium of Chlorella sp., Scenedesmus obliquus, and Ankistrodesmus sp. could tolerate CO2 concentrations up to 7% in a photobioreactor system. The optimal conditions for maximizing CO2 removal and biomass growth were 4,000 lux (74.07 μmol m−2s−1) light intensity with a 16 h light/8 h dark cycle at 30 C. Under these conditions with a 5% CO2 supply, the maximum growth rate reached 0.38 per day. The synergistic action of the three species allowed efficient photosynthetic conversion of the CO2 into biomass. Promising results included 49.02% CO2 removal efficiency, 15.15% CO2 utilization efficiency into biomass, 101.29 gCO2 L-1 h-1 CO2 transfer rate, and 42.02 h-1 CO2 fixation rate. This demonstrates the potential of using optimized microalgal consortia in photobioreactors for effective CO2 mitigation by biological fixation into valuable biomass (Rinanti et al., 2014). Increasing irradiation during the culture of Chlorella resulted in a ∼60% increase in biomass production and a ∼7.0% increase in CO2 fixation ability. It was demonstrated that using bicarbonate (HCO3) as a carbon source significantly affected cultivation, showing non-competitive inhibition under both increasing and constant photon flux density regimes. This inhibition influenced both biomass production and CO2 fixation rates. Another study evaluated microalgal biomass productivity and quality using different colored photobioreactors (white, blue, green) for co-cultivating Chlorella vulgaris, Chlorella sorokiniana, and Scenedesmus sp. on domestic wastewater as medium and nutrients source. The key finding was the white PBR outperformed colored PBRs, increasing microalgae productivity by factor 2.3 to 3.5. The broad spectrum transmitted by the transparent white PBR enhanced photosynthesis, growth, and accumulation of valuable metabolites compared to narrower wavelength ranges from colored reactors under sunlight exposure. Therefore, irradiation intensity, reactor transparency, and cell characteristics interact to determine how effectively microalgae can perform photosynthesis to remove CO2 from the environment (Khalekuzzaman et al., 2021).

4.4 Inorganic nutrients

To achieve optimal growth and CO2 fixation, microalgae require adequate amounts of macronutrients and micronutrients. Macronutrients, such as nitrogen and phosphorus, are essential for the overall growth and development of microalgae, while micronutrients, including vitamins and trace metals, are required in smaller quantities but are equally important for their optimal growth and CO2 fixation (Li et al., 2022). Nitrogen is an essential macronutrient for growth and metabolism. It is a key component of proteins, nucleic acids, and chlorophyll. Adequate nitrogen supply is crucial for optimal carbon fixation and biomass accumulation in microalgae. Nitrogen can be obtained by microalgae from various sources, including nitrate, ammonium, and urea. Nitrate is commonly preferred over ammonium salts for microalgae cultivation as it is more stable and less likely to cause pH shifts (Wang et al., 2024). Ammonia concentrations above 25 μM can be toxic to microalgae. However, nitrogen limitation can reduce biomass production but enhance lipid accumulation. Studies have shown that nitrogen deficiency in Anabaena variabilis and Nostoc muscorum cultures led to decreased growth rates as well as to lower levels of photosynthetic pigments which lead to reduce CO2 sequestration, but simultaneously increased total carbohydrate and lipid contents. Therefore, while higher nitrogen levels favor maximum biomass productivity, nitrogen depletion diverts the metabolic flux towards elevated lipid production in microalgae (Yaakob et al., 2021).

Phosphorus is another essential macronutrient for microalgae. It is a critical component of nucleic acids, ATP (adenosine triphosphate), and phospholipids, which are essential for energy transfer and membrane structure. Phosphorus can be obtained by microalgae from phosphate compounds present in the growth medium. Along with carbon, nitrogen, and phosphorus are primary nutrients needed to build microalgae biomass through photosynthesis and cellular metabolism (). The optimal balance depends on the species, with optimal C: N molar ratios between of 9:1 to 22:1. The molar N:P ratio varies between 1.1 and 45:1 for various microalgae (). Microalgae require certain vitamins for their growth and metabolism. Vitamins, such as thiamine (B1), biotin (B7), and cobalamin (B12), act as cofactors for various enzymatic reactions involved in cellular processes. Microalgae require trace elements such as manganese (Mn), zinc (Zn), copper (Cu), and molybdenum (Mo) for various metabolic processes. These trace elements act as cofactors for enzymes involved in carbon fixation and other biochemical reactions (). Iron is a cofactor for several enzymes involved in photosynthesis and respiration. It is essential for chlorophyll synthesis and electron transport. Adequate iron availability is crucial for efficient carbon fixation and chlorophyll production (). However, exposure to heavy metals potentially present in flue gas supplies can inhibit cultures even at concentrations as low as 1x that of emissions from coal power plants. Polyphosphate accumulation in microalgae cells can protect them from metal toxicity. Polyphosphate can bind to incoming heavy metals like copper (Cu) and cadmium (Cd), forming detoxified complexes. Studies have shown that polyphosphate-rich conditions enabled Chlamydomonas reinhardtii to accumulate and survive the toxic effects of Cu and Cd by sequestering these metals. Therefore, promoting polyphosphate accumulation in microalgae is a potential strategy to mitigate the inhibitory effects of heavy metal contaminants present in industrial flue gas feedstocks. Therefore, while adequate provision of both macronutrients and micronutrients is necessary to sustain healthy, productive microalgae populations for carbon capture, limiting heavy metal contamination is also crucial (Napan et al., 2015).

Microalgae species can utilize diverse waste substrates including agricultural fertilizers, livestock manure, compost extracts, food processing wastewater, anaerobic digestates, and municipal wastewater (; ). These waste streams provide nitrogen, phosphorus, and trace nutrients to sustain biomass growth. Selecting compatible cultivation substrates influences productivity given species-specific nutrient requirements, tolerance to contaminants, and optimal carbon: nitrogen ratios for balanced growth. Using agricultural runoff/wastewater streams as growth media benefits microalgae CO2 fixation through nutrient provision while enabling water bioremediation (). However, high ammonia or salts from fertilizers or livestock waste can inhibit specific microalgae strains (Markou et al., 2014). Thus, the use of low-strength municipal wastewater or anaerobic digestates may improve compatibility for freshwater varieties like Chlorella sp. and Scenedesmus sp. by moderating nitrogen levels (Serejo et al., 2015). Marine and halotolerant algae conversely thrive when cultivated in high-salt substrates or with salinity adjustment using brines.

4.5 Dissolved oxygen

Dissolved oxygen (DO) levels play a critical role in influencing the CO2 fixation efficiency and overall productivity of microalgae cultivation systems. While oxygen is an essential byproduct of photosynthesis, its accumulation beyond optimal levels can have detrimental impacts on microalgal performance. High concentrations of dissolved oxygen above 25 ppm can inhibit CO2 fixation rates in microalgae cultures (Jiménez et al., 2003). As the accumulated DO competes with CO2 for the active sites of Rubisco and other enzymes involved in carbon fixation pathways (Morales et al., 2018). Additionally, DO can cause oxidative damage to cellular components through the formation of reactive oxygen species.

Studies have shown that reducing DO levels can dramatically improve carbon sequestration efficiency, with a 30-fold decrease in DO facilitating a 3-fold increase in CO2 fixation rate in Chlorella sp. (). These studies highlight how dissolved oxygen levels influence Chlorella productivity through mechanisms like photorespiration and photoinhibition, underscoring the importance of optimizing culture conditions to mitigate such detrimental effects. The mechanisms underlying the inhibitory effects of high DO on CO2 fixation are not fully understood but may involve damage to photosynthetic machinery, competition for enzyme active sites, and altered carbon partitioning pathways under oxidative stress conditions.

Therefore, regulating and maintaining optimal dissolved oxygen levels is critically important not only for ensuring the overall health and growth of microalgae cultures but also for maximizing their efficiency of CO2 biofixation productivity and efficiency. Strategies such as controlled aeration, gas sparging, and the selection of microalgae species adapted to high oxygen tolerance can help mitigate the inhibitory effects of elevated DO. However, understanding and managing both DO and CO2 levels is crucial for optimizing microalgal CO2 biofixation rates in carbon capture and utilization (CCU) approaches (Gao et al., 2022).

4.6 CO2 sources and - concentration

The efficacy of CO2 biofixation by microalgae depends substantially on the growth substrates and carbon sources employed in the cultivation system. In addition to inorganic carbon sources such as bicarbonate (HCO3) and CO2 (Politaeva et al., 2023) also organic carbon sources, such as glucose and acetate, can be used by microalgae including Chlorella (Politaeva et al., 2023).

CO2 concentrations in the aeration gas below 0.5% vol. limit microalgal growth and CO2 utilization due to poor solubility in water and low substrate affinity of carbon fixation enzymes such as Rubisco (Mustafa et al., 2020). However, high levels above 6%–12% vol. can also reduce growth by altering the CCM, which converts dissolved CO2 into more bioavailable bicarbonate (HCO3) (Zeng et al., 2021). It has been reported that, elevated CO2 concentrations above 30 g m-3 cause a 30% loss in biomass productivity in Chlorella vulgaris, indicating a negative effect of high dissolved CO2 levels (Kazbar et al., 2019). Specifically, excessive CO2 inhibits the enzyme carbonic anhydrase, which catalyzes the interconversion between CO2 and HCO3, resulting in limited inorganic carbon for fixation (). A comparative study (Koh et al., 2023) analyzed the transcriptomic changes in Chlorella sp. ABC-001 under ambient air and high CO2 conditions. The study aimed to understand the molecular mechanisms driving carbon fixation and lipid accumulation in microalgae. The results revealed significant transcriptional changes in response to different CO2 concentrations, indicating the importance of CO2 availability in regulating pathways such as carbon fixation, photosynthesis, and possibly stress responses. Recent work has also demonstrated that CO2 levels around 15% paired with adequate gas transfer rates maximize carbon fixation in mixotrophic microalgae cultivation (). Another study found carbonic anhydrase enzyme levels nearly diminished in Chlorella cells grown under 15% vol. CO2, indicating direct CO2 permeation into cells without needing the CO2-concentrating mechanism (CCM). The estimated minimum intracellular CO2 concentration required by Rubisco in this strain ranged from 80–192 μM. Bypassing the energy-intensive CCM under high CO2 saved ATP for carbon fixation pathways. Notably, Rubisco gene expression was 16.3 times higher at 15% vol. CO2versus air, while transcript levels of other key carbon fixation genes were also upregulated under elevated CO2, while high CO2 levels over 15% diminished the algal growth at all. Therefore, there is an ideal CO2 dosage range for microalgae lying between substrate limitation and toxicity thresholds where growth and assimilation efficiencies peak (Park et al., 2021).

Flue gases are an important source of CO2. However, their pretreatment is crucial as microalgae are susceptible to damage from contaminants like sulfur oxides (SOx), nitrogen oxides (NOx), and particulates, despite having protective cell walls (Khoo et al., 2020). Desulfurization reduces SOx levels below 60 ppm, which is essential for microalgae growth, while denitrification lowers NOx. De-dusting flue gas by scrubbing particulates is another beneficial pretreatment, especially when using emissions directly from combustion sources like power plants (). Flue gas pretreatment can be achieved through various methods, including wet scrubbing, dry sorbent injection, and catalytic converters. Advanced pretreatment technologies, such as membrane separation and ionic liquids, are also being explored for efficient contaminant removal (Isosaari et al., 2019). Optimal preconditioning methods can make microalgae cultivation systems more productive and cost-effective for biological carbon capture (Thomas et al., 2016).

5 Chlorella as microalga model for biomass production

The green microalga Chlorella sp. is renowned for its remarkably rapid growth rate, making it one of the fastest-growing algae species (). This versatile alga is extensively cultivated and utilized in a wide range of applications, including food and feed production, wastewater treatment, and flue gas remediation (Najm et al., 2017) Chlorella sp. possesses an exceptional ability to thrive under diverse conditions, favoring either the autotrophic, heterotrophic, or mixotrophic growth mode. This adaptability contributes to its widespread utilization across various industries. Several Chlorella species, including C. pyrenoidosa, C. vulgaris, C. lewinii, and C. sorokiniana, exhibit the capacity to accumulate carbohydrates. In addition to biomass production Chlorella can produce high-value by-products such as carotenoids, vitamins, and fatty acids, making them attractive candidates for various industrial applications (Ngangkham et al., 2012). The robustness, high growth rate, and high content of neutral lipids in Chlorella sp. make it a promising candidate for bioenergy production. To reduce costs and enhance the economic viability of algal biomass production, indoor photobioreactor (PBR) systems have been developed for high-density cultivation. These systems offer controlled environmental conditions, optimizing growth and productivity (). The integration of renewable energy sources and carbon capture technologies further contributes to the sustainability and environmental benefits of Chlorella sp. cultivation ().

Chlorella sp. was selected as a model for CO2 capture due to its high biomass productivity and large biochemical profile, which includes various carbon pathways, such as CMM, C4, and CAM. It can tolerate high levels of CO2, up to 70%, 95% (Li et al., 2013), and 100% vol. (Zhang and Song, 2014), and does not require high pH values, making it a suitable option for CO2 capture compared to other species like as Arthrospira platensis () Notable species of Chlorella include Chlorella vulgaris, Chlorella sorokiniana, and Chlorella protothecoides, all of which are recognized for their efficiency in CO2 capture and biomass production. According to the FAO statistics report (), in 2019, Chlorella vulgaris accounted for 0.008% of the world’s total microalgae production, with a production volume of 4.77 tons. This made it the third most produced microalgae species globally. However, it is important to note that this report did not include other species within the Chlorella genus. The Chlorella genus has a multitude of commercial applications, including production of food supplements (), pharmaceuticals (Lamare and Chaurasia, 2022) glycolipids (Yamashita et al., 2022), PUFA (Toumi et al., 2022), biodiesel (Moradi and Saidi, 2022), biohydrogen (Jimenez-Llanos et al., 2020a), and bioplastic (Nanda, 2022). Additionally, Chlorella is used in aquaculture (Ranglová et al., 2022) and, wastewater purification (Kumari et al., 2022). The CO2 capture rate (g L−1 d−1) and removal efficiency (%) of Chlorella species are influenced by various cultivation conditions, such as CO2 volume, temperature, pH, and light intensity, as indicated in Table 3.

TABLE 3

Chlorella speciesBiomassCO2 removal efficiency (%)CO2 capture rate (g L−1 d−1)Cultivation Conditions
CO2 (vol%)Temp (°C)Light intensity (Lux)pHReferences
C. vulgaris23.5 (106 cells m L−1)18303018007.2Sadeghizadeh et al. (2017)
C. vulgaris18.3 (106 cells m L−1)182.22303,783Sadeghizadeh et al. (2017)
C. vulgaris-400.5110–2084,5408.2Sadeghizadeh et al. (2017)
C. vulgaris-0.25–1.70.03186,0008Sadeghizadeh et al. (2017)
Chlorella sp.3.461 (g L−1)10102616,000
Chlorella sp.2.369 (g L−1)50.3555,4007.1
C. vulgaris1.1–1.9 (g L−1)182.6625253,6007–8.2
Chlorella sp.5.77 (g L−1)1010254,0506Yue and Chen (2005)

Reported CO2 removal capacity and capture rate of selected Chlorella species in PPR under different growth conditions.

As with any microalgae species, the methods and conditions for cultivating Chlorella vary based on the intended use of its biomass. Valdovinos-García et al. (2021) conducted a techno-economic study of harvesting and drying Chlorella cultivated in tubular photobioreactors and found a biomass production of 82.45 tons ha−1 y−1 (22.66 g m2 d−1) with estimated CO2 capture of 148.4 148.4 tons ha−1 y−1. In another study (James and Al-Khars, 1990), Chlorella sp. MFD-1 cultured in airlift PBR produced a biomass of 109–264 g m−3 d−1. Another study by Hossain et al. (2019) reported that the biomass productivity of Chlorella was around 56 tones ha−1 y−1, with a capture of 36.3 tons CO2 ha−1 y−1. On the other hand, the study by , and showed that the average biomass production of microalgae cultivated in open ponds was approximately 175, 280, and 300 tons ha−1 y−1, respectively, which could potentially lead to the capture of 329, 525, and 564 tones CO2 ha−1 y−1, respectively. These data suggest that the production of biomass is largely influenced by the cultural technology used. Improved and advanced technologies result in increased biomass. Min et al. (2011) conducted a pilot-scale study on the bioremediation efficiency of Chlorella sp. grown in a 1200 L tubular photobioreactor using wastewater, resulting in a biomass production range of 17.7–34.6 g m−2 d−1. This shows that Chlorella sp. is a promising option for CO2 capture compared to terrestrial plants, taking into account the technologies used for cultivation, harvesting, and drying.

conducted a study on the culture of marine Chlorella sp. in a 750 mL photobioreactor under controlled conditions and a temperature of 26°C, continuous cool-white, fluorescent light (intensity of 300 μmol m−2 s−1), using F/2 medium. The study examined the effect of different CO2 levels (2, 5, 10, and 15% vol.) on average biomass productivity, CO2 capture, and efficiency. The results showed that the average biomass productivity ranged from 0.76 to 0.87 g L−1 after 8 days of cultivation, while the CO2 capture and efficiency ranged from 0.261 g h−1 and 58% to 0.573 g h−1 and 16%, respectively. The study concluded that using an advanced multiple photobioreactor system can increase the efficiency of Chlorella sp. in CO2 capture. Vo et al. (2018) conducted a study on the effect of different N/P ratios (10/1, 15/1, 20/1, and 25/1) on the biomass productivity of Chlorella sp. in a 2-working bubble column photobioreactor with a total volume of 8 L. The study was conducted under controlled conditions of temperature (29°C ± 2°C), continuous irradiation (3,000 Lux), air and air mixture (2 and 4 L min−1), and injected CO2 at a level of 0.2 L min−1. The optimum N/P ratio (15/1) was found to result in biomass productivity of 3.568 g L−1, a CO2 capture efficiency of 28%, and a CO2 removal rate of 68.9 mg L−1 h−1. Table 4 summarizes some published studies on microalgae biomass cultivated under different types of photobioreactors.

TABLE 4

Chlorella speciesPBR TypesBiomass productionReferences
Chlorella spAirlift109–264 g m−3 d−1James and Al-Khars (1990)
C. vulgarisAirlift0.28–0.89 g L−1 d−1Hanagata et al. (1992)
C. vulgarisAirlift0.124 g L−1 d−1
C. vulgarisAirlift460 mg L−1 d−1Ren et al. (2017)
C. pyrenoidosaAirlift0.37 g L−1 d−1Tan et al. (2014)
C. vulgarisLED-based PBR2.11 g L−1 d−1Fu et al. (2012)
C. sorokinianaLight-path-panel PBR2.1 g L−1
C. vulgarisRotating float-plate PBR3.35 g m−2Melo et al. (2018)
C. sorokinianaFlat plate469 mg L−1 d−1
C. zofingiensisFlat plate58.4 mg L−1 day−1Feng et al. (2011)
C. vulgarisFlat plate0.045 g L−1 h−1Satoh et al. (2001)
Chlorella spBubble column3.5 g L−1
C. vulgarisBubble column1.41 g L−1
C. minutissimaBubble column1.65 g L−1Sharma et al. (2016)
C. vulgarisColumn81.67 mg L−1 d−1
C. vulgarisColumn0.28–0.52 g L−1Lam and Lee (2014)
C. sorokinianaColumn10.22 g m−2 d−1
Chlorella spTubular21.5 g m−2 d−1Watanabe and Saiki (1997)
C. pyrenoidosaTubular1.83–2.10 g L−1Tan et al. (2021)
Chlorella spTubular17.7–34.6 g m−2 d−1Min et al. (2011)
Chlorella spTubular22.66 g m−2 d−1Valdovinos-García et al. (2021)

Biomass production of some Chlorella species cultured in different PBR systems.

The production cost of microalgae biomass has significantly decreased due to the utilization of knowledge from granted patents (Mohamed, 2018), along with practical expertise, know-how, and field experiences. These tools simplify the processes of culture, harvesting, drying, and extraction. Our objectives align with the findings of who performed a cost analysis of producing high-value products from S. almeriensis. Over 2 years at a small scale (0.04 ha), S. almeriensis was grown in 10 m3 tubular PBRs. The resulting annual production capacity, photosynthetic efficiency, and production cost were 3.8 tons per year (90 tons ha−1 y−1), 3.6%, and 69 € kg−1, respectively. They concluded that increasing production capacity leads to a decrease in production cost. Furthermore, large projects and facilities have the potential to produce more than 200 tons ha−1 y−1 and they often have lower labor and consumption costs. also suggested using flue gases and wastewater as sources of external CO2 or carbon. In conclusion, they found PBRs to be more attractive and productive than OP systems but recommended reducing the fixed and operational costs to make them more comparable to those of OP systems. They also advised implementing new PBR technologies. However, this study was conducted over a decade ago, and PBR technologies have since advanced, which may have changed the production costs.

6 Microalgae as a feedstock for bioenergy

Through biofixation, being the resulting biomass rich in carbohydrates, lipids, and other compounds can then be converted into sustainable biofuels via various thermo-chemical and biological routes. Biofuels offer several advantages as they are environmentally friendly, non-toxic, and can serve as an alternative to fossil fuels. Current efforts are focused on effectively utilizing various waste streams as feedstocks for commercial biofuel production. With the limitations associated with first and second-generation biofuels from food crops and lignocellulosic biomass, microalgae have emerged as a promising third-generation biofuel source to replace fossil fuels (). Species like Chlorella sp., Botryococcus braunii, Dunaliella primolecta, and Nannochloropsis sp. can produce substantial amounts of hydrocarbons and lipids that can be converted to biofuels, in addition to their biomass. These microalgae also synthesize other commercially valuable compounds such as polysaccharides and carotenoids. Furthermore, microalgae have the ability to grow on diverse media, and their biomass is abundantly available. However, a major challenge in microalgal biofuel production is the inherently low lipid content of the cells and their small size, which makes the harvesting process extremely costly and difficult to implement at a commercial scale. Consequently, developing cost-effective harvesting strategies is one of the critical barriers hindering the widespread marketability and economic viability of microalgae-based biofuel production systems. Furthermore, the combination of highly scalable microalgae productivity coupled with carbon capture, nutrient recycling, and value-added biofuel coproduction makes microalgal biorefinery systems uniquely promising and drives further process advancement (Goh et al., 2019). Figure 2 schematically illustrates overall biofuel production processes.

6.1 Biodiesel production

Microalgae can accumulate significant amounts of lipids, making them a promising feedstock for biodiesel production (). They can synthesize and store lipids, primarily in the form of triacylglycerols (TAGs), which can account for up to 60% of their dry cell weight under certain cultivation conditions. The ability of microalgae to accumulate high levels of lipids is attributed to several factors, including their simple cellular structure, rapid growth rate, and the ability to modulate their metabolism in response to environmental conditions (; Osman et al., 2023b). For example, when subjected to stress conditions such as nutrient deprivation, high light intensity, or temperature changes, some microalgal species can divert their metabolic pathways towards increased lipid biosynthesis and accumulation as a survival mechanism. This lipid-rich biomass can be used as a feedstock for the production of biodiesel through transesterification, a process that converts the TAGs into fatty acid methyl esters (FAMEs), which are the main components of biodiesel. Compared to traditional feedstocks like vegetable oils or animal fats, microalgal lipids offer several advantages, such as higher productivity per unit area, the ability to grow on non-arable land, and the potential to utilize waste streams (e.g., CO2 and wastewater) as nutrient sources ().

Microalgae oil, rich in fatty acids like linoleic (C18:2), linolenic (C18:3), and oleic acid (C18:1) can be extracted and converted to biodiesel through transesterification reactions with alcohols like methanol. Microalgae species, including Nannochloropsis, Chlorella, and Schizochytrium contain 20%–77% lipid that transesterified into monoalkyl esters comparable to conventional petroleum-derived diesel (Okeke et al., 2022). However, the rigid cellulose-containing walls of microalgae resist solvent penetration during extraction. Various pretreatment methods like microwave irradiation, ultrasonication, or chemical disruption using acids/bases permeabilize the cells to improve oil recovery (Malekghasemi et al., 2021). In situ approaches also directly transesterify wet microalgae biomass containing up to 40% moisture into fatty acid methyl esters (FAMEs), overcoming the barrier of high water content that is typically inhibitory to biodiesel synthesis (Nguyen et al., 2020). Integrating biodiesel generation with microalgae cultivation can provide sustainable transportation fuels while recycling carbon emissions into growth substrate.

6.2 Biooil production

Biooil production from algal biomass is an alternative process for converting microalgal biomass into liquid fuel through thermochemical conversion techniques, such as pyrolysis or liquefaction. Unlike biodiesel production, which focuses on extracting and transesterifying the lipids present in microalgae, biooil production aims to convert the entire algal biomass into a complex liquid mixture of oxygenated hydrocarbons, known as biooil or biocrude (Mathimani et al., 2019).

The first method is pyrolysis. Pyrolysis is the thermal decomposition of algal biomass in the absence of oxygen or any other gaseous oxidizing agent. The process involves heating the dried algal biomass to temperatures ranging from 400°C to 600°C, resulting in the formation of biooil, biochar (solid residue), and non-condensable gases. The biooil obtained is a complex mixture of oxygenated hydrocarbons, including phenolic compounds, acids, alcohols, and other organic compounds (Vuppaladadiyam et al., 2023).

The second method is hydrothermal liquefaction (HTL). HTL involves the conversion of algal biomass into biooil through thermochemical reactions in an aqueous environment at elevated temperatures (300°C–350 C) and pressures (5–25 MPa). The high pressure and temperature conditions facilitate the depolymerization and decomposition of the algal biomass, resulting in the formation of biooil, solid residue, and an aqueous phase containing dissolved products. The biooil produced through HTL typically has a higher energy density and lower oxygen content compared to pyrolysis biooil. The biooil obtained from these processes can be upgraded through various techniques, such as catalytic hydrotreating, hydrocracking, or esterification, to improve its quality and stability for use as a transportation fuel or as a feedstock for the production of chemicals and materials (Gollakota et al., 2018).

Bio-oil yields around 75% on a weight basis and contains a complex mixture of oxygenated hydrocarbons like organic acids, aldehydes, ketones, and phenols with promising applications for heat, power, and transportation (). Catalytic pyrolysis augments bio-oil quality through deoxygenation and secondary hydrocarbon reformation mediated by catalysts including zeolites and supported metal catalysts (Li et al., 2021). To potentially improve the viability of the petrochemical sector, hydroprocessing using sulfided Ni- and Co-based catalysts also reduces nitrogen while increasing carbon chains within the algae bio-oil (). Microalgae biooil could ultimately provide a sustainable replacement for fossil oil-derived petrochemicals.

6.3 Bioethanol

Bioethanol production from algal biomass is an alternative approach to utilizing microalgae as a feedstock for biofuel production. Bioethanol is a renewable fuel that can be produced through the fermentation of carbohydrates present in biomass. Microalgae can accumulate significant amounts of carbohydrates, primarily in the form of starch or glycogen, making them a potential source for bioethanol production (Lakatos et al., 2019). Species such as Chlamydomonas reinhardtii and Chlorella vulgaris accumulate high levels of glycogen and starch, while cellulose is abundant in cell walls (Fivga et al., 2019). Chlorella accumulates high levels of starch and other glycans like glucans and mannans in addition to cellulosic cell walls. However, these complex polysaccharides cannot be directly fermented and instead undergo hydrolysis to convert the carbohydrates (e.g., starch, glycogen) into fermentable sugars (e.g., glucose, maltose). This can be achieved through enzymatic hydrolysis using amylases or acid hydrolysis using dilute or concentrated acids. Methods such as microwave or ultrasound pretreatments help break down the Chlorella cell walls, improving accessibility (). Acid or alkaline pretreatments help break down the cell walls, while commercial enzyme cocktails containing amylases, cellulases, and pectinases depolymerize glycans into hexose/pentose sugars like glucose and xylose (Phwan et al., 2018). The released sugars then undergo fermentation by organisms like Saccharomyces cerevisiae or Zymomonas mobilis to produce ethanol (5%–15% v/v). The fermented broth is distilled to separate the bioethanol from the residual biomass and other components. Further purification steps, such as dehydration or molecular sieve adsorption, may be employed to obtain anhydrous bioethanol. Optimizing the processing pathways and genetics of microalgae strains could continue to improve the economic viability of microalgal ethanol production. Chlorella vulgaris can accumulate up to 37% of its dry weight as starch, making it a promising feedstock for bioethanol production after hydrolysis using fungal hydrolysis enzymes (Monjed et al., 2021). Chlamydomonas reinhardtii has been studied extensively for its ability to accumulate starch and produce bioethanol through fermentation (). Arthrospira platensis can accumulate glycogen up to 65% of its dry weight, which can be hydrolyzed and fermented for bioethanol production (Kusmiyati et al., 2020). Scenedesmus obliquus can accumulate significant amounts of carbohydrates (up to 50% of its dry weight) and has been investigated for bioethanol production (Yirgu et al., 2023). It is important to note that the production of bioethanol from microalgae is still in the research and development phase, and various challenges, such as improving the carbohydrate content, optimizing the pretreatment and hydrolysis processes, and reducing production costs, need to be addressed for large-scale commercial viability.

6.4 Biogas

Biogas can be produced from algal biomass through anaerobic digestion, which is a biological process that breaks down organic matter in the absence of oxygen. Algal biomass, particularly after being used for other applications like extracting lipids or carbohydrates, contains a significant amount of residual organic matter that can be utilized for biogas production (). The algal biomass may need to undergo pretreatment processes to improve its biodegradability and accessibility for the anaerobic digestion process. Pretreatment methods can include mechanical (e.g., milling, ultrasound), chemical (e.g., acid, alkali), or biological (e.g., enzymatic) techniques. The pretreated algal biomass is fed into an anaerobic digester, where it is broken down by a consortium of microorganisms in the absence of oxygen. The anaerobic digestion process typically occurs in four stages: hydrolysis, acidogenesis, acetogenesis, and methanogenesis. The end product of anaerobic digestion of microalgae by methanogenic archaea and bacteria produces biogas, which contains 50%–70% methane plus 30%–50% carbon dioxide and trace gases like hydrogen sulfide and ammonia (Pavithra et al., 2020). Hydrolysis first breaks down lipids, proteins, and carbohydrates into simple monomers. Acidogenic bacteria then produce volatile fatty acids that are converted to acetic acid, hydrogen, and CO2. Finally, methanogens like the Archaea bacterium Methanothrix produce methane using the acetyl-CoA pathway coupled with hydrogen oxidation. However, multiple factors influence the methane productivity from microalgae including the distribution of macromolecules for digestion, the molar carbon: nitrogen (C: N) ratio optimally around 20–25:1, as well as rigid cell wall lysis. Applying preprocessing like ultrasonication to fragment cell walls can enhance biogas yields from Chlorella vulgaris and other species by up to 40% (Park et al., 2021).

Biogas production from algal biomass offers several advantages, including, algal biomass residues from other processes can be valorized for biogas production, contributing to a more sustainable and circular biorefinery approach. Furthermore, digested residue (digestate) from the anaerobic digestion process can be used as a nutrient-rich fertilizer or soil amendment, promoting nutrient recycling. However, there are also challenges associated with biogas production from algal biomass, such as the need for efficient pretreatment methods, optimization of the anaerobic digestion process for algal feedstocks, and the potential presence of inhibitory compounds or contaminants that can affect the microbial communities involved in the process. Several studies have investigated the potential of different microalgal species, such as Chlorella, Scenedesmus, and Spirulina, for biogas production through anaerobic digestion (Zabed et al., 2020). Ongoing research aims to improve the efficiency and economics of this process, making it a viable option for valorizing algal biomass and producing renewable energy.

6.5 Biohydrogen

Chlorella demonstrates high potential for biohydrogen production, leveraging existing biomass facilities in countries like the United States, Germany, and Japan. Through co-production of valuable by-products alongside biohydrogen, a flexible biorefinery approach could foster a sustainable bio-economy (Jimenez-Llanos et al., 2020a). Various Chlorella species, including C. fusca, C. homosphaera, C. pyrenoidosa, C. vacuolata, C. vulgaris var. vulgaris, C. lewinii, C. salina, C. sorokiniana, C. protothecoides, and Parachlorella kessleri (formerly C. kessleri), accumulate significant endogenous carbohydrates under nutrient limitation, leading to impressive hydrogen production rates. These species also produce high-value commercial by-products such as vitamins, carotenoids, glycerol, mycosporine-like amino acids, unsaturated fatty acids, lectins, anti-freeze proteins, glycoproteins, butylated hydroxytoluene, specific polysaccharides, and glutathiones (Jimenez-Llanos et al., 2020a).

Chlorella biomass possesses unique characteristics that qualify it for biohydrogen production: a. High biohydrogen production potential: Chlorella biomass, particularly species like Chlorella vulgaris and Chlorella sorokiniana, show significant biohydrogen production potential due to the presence of specific enzymes such as [FeFe]-hydrogenase (Wang et al., 2021). b. Unique H-cluster structure: Chlorella biomass features a distinctive H-cluster structure in its [FeFe]-hydrogenase, enhancing catalytic activity for biohydrogen production compared to other hydrogenases (Wang et al., 2021). c. Efficient photosynthesis: Known for high photosynthetic efficiency, Chlorella efficiently converts solar energy into biomass, crucial for biohydrogen production (Velmozhina et al., 2023). d. Tolerance to adverse conditions: Chlorella cells exhibit resilience to adverse conditions like high light intensity, temperature fluctuations, and nutrient limitations, ensuring consistent growth and biohydrogen production (Velmozhina et al., 2023).

Biohydrogen production from Chlorella spp. can be achieved through various methods including direct biophotolysis, indirect biophotolysis, and dark fermentation. Direct biophotolysis utilizes photosynthesis to split water molecules and generate hydrogen gas. Some Chlorella species split water in photosystem II, transferring excited electrons to Photosystem I where hydrogenase enzymes produce H2, though challenges with oxygen sensitivity limit efficiency (Lam et al., 2019). Indirect biophotolysis: Indirect biophotolysis involves usage of stored energy molecules like starch for hydrogen production, separating oxygenic photosynthesis from anaerobic hydrogen generation to overcome oxygen sensitivity. Dark Fermentation: In dark fermentation, microorganisms convert organic substrates into hydrogen and other by-products in the absence of light. Chlorella spp. can undergo dark fermentation with nitrogen-fixing bacteria like Klebsiella sp. and Clostridium sp., utilizing glycolysis and citric acid pathways to produce hydrogen (; ). Dark fermentation offers advantages including high H2 production rates, utilization of organic substrates, and potential for valuable by-products, making it suitable for wastewater treatment and biofuel production (; ).

7 Conclusion and future perspectives

Mitigating climate change by reducing atmospheric CO2 levels is a critical global challenge. While CO2 capture projects are environmentally beneficial, they are often viewed as low-profit and high-risk ventures requiring substantial investment. To meet 2050 climate goals, the Global CCS Institute estimates around 2,000 commercial CO2 capture projects must be deployed annually at $655–1,280 billion (Rassool, 2021). Encouraging private sector participation through attractive carbon pricing mechanisms like taxes or emissions trading can incentivize investment in CO2 capture technologies. Tax exemptions and low facility costs may also help facilitate commercial viability. Industries with high CO2 emissions could potentially be required to finance and develop capture projects. Microalgae, especially the Chlorella genus reviewed here, are emerging as a crucial tool for CO2 capture and conversion into valuable products like biohydrogen. Their carbon concentrating mechanisms allow 10–50x higher CO2 fixation than terrestrial plants. However, fully realizing microalgae’s potential requires continued scientific, commercial, and technical innovation (Iglina et al., 2022). The capacity of biohydrogen production emphasizes Chlorella’s versatility as an integrated biorefinery feedstock. Combining microalgae’s exceptional growth with waste resource recycling enables sustainable, circular bioeconomy. Overall, this review underscores microalgae-based CO2 capture as a promising solution, but large-scale implementation will require multidisciplinary advances in biological understanding, bioprocess engineering, and supportive policy mechanisms to make these technologies economically viable for achieving climate targets.

Statements

Author contributions

MA: Conceptualization, Data curation, Formal Analysis, Funding acquisition, Investigation, Methodology, Project administration, Resources, Software, Supervision, Validation, Visualization, Writing–original draft, Writing–review and editing. AM: Funding acquisition, Investigation, Resources, Software, Supervision, Validation, Visualization, Writing–review and editing. YA: Funding acquisition, Investigation, Resources, Software, Supervision, Validation, Visualization, Writing–review and editing. ME: Conceptualization, Data curation, Formal Analysis, Funding acquisition, Investigation, Methodology, Resources, Software, Supervision, Validation, Visualization, Writing–original draft, Writing–review and editing.

Funding

The author(s) declare that financial support was received for the research, authorship, and/or publication of this article. This work was supported by the Deanship of Scientific Research, Vice Presidency for Graduate Studies and Scientific Research, King Faisal University, Saudi Arabia (GrantA172).

Conflict of interest

The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

Publisher’s note

All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.

References

  • 1

    AbomohraA.AliS. S.RamadanH.El-AswarE. I.EltawabR.HoS.-H.et al (2023). Microalgae-based wastewater treatment: mechanisms, challenges, recent advances, and future prospects. Environ. Sci. Ecotechnology13, 100205. 10.1016/j.ese.2022.100205

  • 2

    AbomohraA. E.ElshobaryM. (2019). Biodiesel, bioethanol, and biobutanol production from microalgae. Microalgae Biotechnol. Dev. biofuel wastewater Treat., 293321. 10.1007/978-981-13-2264-8_13

  • 3

    AciénF.FernándezJ.MagánJ.MolinaE. (2012). Production cost of a real microalgae production plant and strategies to reduce it. Biotechnol. Adv.30 (6), 13441353. 10.1016/j.biotechadv.2012.02.005

  • 4

    AdamczykM.LasekJ.SkawińskaA. (2016). CO 2 biofixation and growth kinetics of Chlorella vulgaris and Nannochloropsis gaditana. Appl. Biochem. Biotechnol.179, 12481261. 10.1007/s12010-016-2062-3

  • 5

    AdamsJ. C.EngelJ. (2021). “Human-made risks and climate change with global heating,” in Life and its future (Germany: Springer), 117148.

  • 6

    AhnY.ParkS.JiM.-K.HaG.-S.JeonB.-H.ChoiJ. (2022). Biodiesel production potential of microalgae, cultivated in acid mine drainage and livestock wastewater. J. Environ. Manag.314, 115031. 10.1016/j.jenvman.2022.115031

  • 7

    AlprolA. E.MansourA. T.AbdelwahabA. M.AshourM. (2023). Advances in green synthesis of metal oxide nanoparticles by marine algae for wastewater treatment by adsorption and photocatalysis techniques. Catalysts13 (5), 888. 10.3390/catal13050888

  • 8

    AlzateM.MuñozR.RogallaF.Fdz-PolancoF.Pérez-ElviraS. (2014). Biochemical methane potential of microalgae biomass after lipid extraction. Chem. Eng. J.243, 405410. 10.1016/j.cej.2013.07.076

  • 9

    AmaralM. d.S.LouresC. C. A.NavesF. L.BaetaB.SilvaM.PrataA. (2020). Evaluation of cell growth performance of microalgae Chlorella minutissima using an internal light integrated photobioreactor. J. Environ. Chem. Eng.8 (5), 104200. 10.1016/j.jece.2020.104200

  • 10

    AmmarS. H. (2016). Cultivation of microalgae chlorella vulgaris in airlift photobioreactor for biomass production using commercial NPK nutrients. Al-Khwarizmi Eng. J.12 (1), 9099.

  • 11

    AmorosoG.SultemeyerD.ThyssenC.FockH. P. (1998). Uptake of HCO3− and CO2 in cells and chloroplasts from the microalgae Chlamydomonas reinhardtii and Dunaliella tertiolecta. Plant Physiol.116 (1), 193201. 10.1104/pp.116.1.193

  • 12

    AshourM.Al-SoutiA. S.HassanS. M.AmmarG. A. G.GodaA.El-ShenodyR.et al (2023). Commercial seaweed liquid extract as strawberry biostimulants and bioethanol production. Life13 (1), 85. 10.3390/life13010085

  • 13

    AshourM.OmranA. M. M. (2022). Recent advances in marine microalgae production: highlighting human health products from microalgae in view of the coronavirus pandemic (COVID-19). Fermentation8 (9), 466. 10.3390/fermentation8090466

  • 14

    AslamA.RasulS.BahadarA.HossainN.SaleemM.HussainS.et al (2021). Effect of micronutrient and hormone on microalgae growth assessment for biofuel feedstock. Sustainability13 (9), 5035. 10.3390/su13095035

  • 15

    BabatabarM. A.YousefianF.MousaviM. V.HosseiniM.TavasoliA. (2022). Pyrolysis of lignocellulosic and algal biomasses in a fixed‐bed reactor: a comparative study on the composition and application potential of bioproducts. Int. J. Energy Res.46 (7), 98369850. 10.1002/er.7855

  • 16

    BaiA.PoppJ.PetőK.SzőkeI.Harangi-RákosM.GabnaiZ. (2017). The significance of forests and algae in CO2 balance: a Hungarian case study. Sustainability9 (5), 857. 10.3390/su9050857

  • 17

    BambaB. S. B.LozanoP.AdjéF.OuattaraA.VianM. A.TranchantC.et al (2015). Effects of temperature and other operational parameters on Chlorella vulgaris mass cultivation in a simple and low-cost column photobioreactor. Appl. Biochem. Biotechnol.177 (2), 389406. 10.1007/s12010-015-1751-7

  • 18

    BarakatK. M.El-SayedH. S.KhairyH. M.El-SheikhM. A.Al-RashedS. A.ArifI. A.et al (2021). Effects of ocean acidification on the growth and biochemicalcomposition of a green alga (Ulva fasciata) and its associated microbiota. Saudi J. ofBiological Sci.28, 51065114. 10.1016/j.sjbs.2021.05.029

  • 19

    BarrettJ.GirrP.MackinderL. C. (2021). Pyrenoids: CO2-fixing phase separated liquid organelles. Biochimica Biophysica Acta (BBA)-Molecular Cell. Res.1868 (5), 118949. 10.1016/j.bbamcr.2021.118949

  • 20

    BéchetQ.MuñozR.ShiltonA.GuieysseB. (2013). Outdoor cultivation of temperature‐tolerant Chlorella sorokiniana in a column photobioreactor under low power‐input. Biotechnol. Bioeng.110 (1), 118126. 10.1002/bit.24603

  • 21

    BenedettiM.VecchiV.BareraS.Dall’OstoL. (2018). Biomass from microalgae: the potential of domestication towards sustainable biofactories. Microb. Cell. Factories17 (1), 173218. 10.1186/s12934-018-1019-3

  • 22

    BenemannJ. R.OswaldW. J. (1996). Systems and economic analysis of microalgae ponds for conversion of CO {sub 2} to biomass. Final report.

  • 23

    BholaV.SwalahaF.Ranjith KumarR.SinghM.BuxF. (2014). Overview of the potential of microalgae for CO2 sequestration. Int. J. Environ. Sci. Technol.11 (7), 21032118. 10.1007/s13762-013-0487-6

  • 24

    BhushanS.JayakrishnanU.ShreeB.BhattP.EshkabilovS.SimsekH. (2023). Biological pretreatment for algal biomass feedstock for biofuel production. J. Environ. Chem. Eng.11 (3), 109870. 10.1016/j.jece.2023.109870

  • 25

    BirnerB.RödenbeckC.DohnerJ. L.SchwartzmanA.KeelingR. F. (2023). Surprising stability of recent global carbon cycling enables improved fossil fuel emission verification. Nat. Clim. Change13 (9), 961966. 10.1038/s41558-023-01761-x

  • 26

    BouyamS.ChooritW.SirisansaneeyakulS.ChistiY. (2017). Heterotrophic production of Chlorella sp. TISTR 8990—biomass growth and composition under various production conditions. Biotechnol. Prog.33 (6), 15891600. 10.1002/btpr.2518

  • 27

    BozzoG. G.ColmanB.MatsudaY. (2000). Active transport of CO 2 and bicarbonate is induced in response to external CO 2 concentration in the green alga Chlorella kessleri. J. Exp. Bot.51 (349), 13411348. 10.1093/jxb/51.349.1341

  • 28

    BrinckerhoffP. (2011). Accelerating the uptake of CCS: industrial use of captured carbon dioxide, 260. New York: Global CCS Institute.

  • 29

    BuiX.-T.NguyenT.-T.NguyenD. D.DaoT.-S.CaoN. D. T., (2018). RETRACTED: effects of nutrient ratios and carbon dioxide bio-sequestration on biomass growth of Chlorella sp. in bubble column photobioreactor. J. Environ. Manag.219, 18. 10.1016/j.jenvman.2018.04.109

  • 30

    CaiJ.LovatelliA.Aguilar-ManjarrezJ.CornishL.DabbadieL.DesrochersA.et al (2021). Seaweeds and microalgae: an overview for unlocking their potential in global aquaculture development. FAO Fish. Aquac. Circular1229.

  • 31

    CarnicerO.IrwinA. J.FinkelZ. V. (2022). Traits influence dinoflagellate C:N:P. J. Phycol.57, 154165. 10.1080/09670262.2021.1914860

  • 32

    CheahW. Y.ShowP. L.ChangJ.-S.LingT. C.JuanJ. C. (2015). Biosequestration of atmospheric CO2 and flue gas-containing CO2 by microalgae. Bioresour. Technol.184, 190201. 10.1016/j.biortech.2014.11.026

  • 33

    ChenC.YangS. (2021). The energy demand and environmental impacts of oxy-fuel combustion vs. post-combustion capture in China. Energy Strategy Rev.38, 100701. 10.1016/j.esr.2021.100701

  • 34

    ChenW.-H.LinB.-J.HuangM.-Y.ChangJ.-S. (2015). Thermochemical conversion of microalgal biomass into biofuels: a review. Bioresour. Technol.184, 314327. 10.1016/j.biortech.2014.11.050

  • 35

    ChengC.-L.LoY.-C.HuangK.-L.NagarajanD.ChenC.-Y.LeeD.-J.et al (2022). Effect of pH on biomass production and carbohydrate accumulation of Chlorella vulgaris JSC-6 under autotrophic, mixotrophic, and photoheterotrophic cultivation. Bioresour. Technol.351, 127021. 10.1016/j.biortech.2022.127021

  • 36

    ChengJ.LuH.LiK.ZhuY.ZhouJ. (2018). Enhancing growth-relevant metabolic pathways of Arthrospira platensis (CYA-1) with gamma irradiation from 60 Co. RSC Adv.8 (30), 1682416833. 10.1039/c8ra01626g

  • 37

    ChengL.ZhangL.ChenH.GaoC. (2006). Carbon dioxide removal from air by microalgae cultured in a membrane-photobioreactor. Sep. Purif. Technol.50 (3), 324329. 10.1016/j.seppur.2005.12.006

  • 38

    ChistiY. (2007). Biodiesel from microalgae. Biotechnol. Adv.25 (3), 294306. 10.1016/j.biotechadv.2007.02.001

  • 39

    ChiuS. Y.TsaiM. T.KaoC. Y.OngS. C.LinC. S. (2009). The air‐lift photobioreactors with flow patterning for high‐density cultures of microalgae and carbon dioxide removal. Eng. life Sci.9 (3), 254260. 10.1002/elsc.200800113

  • 40

    ChoJ. M.OhY.-K.ParkW.-K.ChangY. K. (2020). Effects of nitrogen supplementation status on CO2 biofixation and biofuel production of the promising microalga Chlorella sp. ABC-001. J. Microbiol. Biotechnol.30 (8), 12351243. 10.4014/jmb.2005.05039

  • 41

    ChoiS. P.NguyenM. T.SimS. J. (2010). Enzymatic pretreatment of Chlamydomonas reinhardtii biomass for ethanol production. Bioresour. Technol.101 (14), 53305336. 10.1016/j.biortech.2010.02.026

  • 42

    ColmanB.HuertasI. E.BhattiS.DasonJ. S. (2002). The diversity of inorganic carbon acquisition mechanisms in eukaryotic microalgae. Funct. Plant Biol.29 (3), 261270. 10.1071/pp01184

  • 43

    ColmanB.RotatoreC. (1995). Photosynthetic inorganic carbon uptake and accumulation in two marine diatoms. Plant, Cell. and Environ.18 (8), 919924. 10.1111/j.1365-3040.1995.tb00601.x

  • 44

    CoutoD.MeloT.CondeT. A.MoreiraA. S.FerreiraP.CostaM.et al (2022). Food grade extraction of Chlorella vulgaris polar lipids: a comparative lipidomic study. Food Chem.375, 131685. 10.1016/j.foodchem.2021.131685

  • 45

    CoutoE.CalijuriM.AssemanyP.SouzaM. (2018). Effect of depth of high-rate ponds on the assimilation of CO2 by microalgae cultivated in domestic sewage. Environ. Technol.39 (20), 26532661. 10.1080/09593330.2017.1364302

  • 46

    Cuaresma FrancoM.Vílchez LobatoC.JanssenM.WijffelsR. H. (2024). Productivity of Chlorella sorokiniana in a short light-path (SLP) panel photobioreactor under high irradiance.

  • 47

    de AssisT. C.CalijuriM. L.AssemanyP. P.de Paula PereiraA. S. A.MartinsM. A. (2019). Using atmospheric emissions as CO2 source in the cultivation of microalgae: productivity and economic viability. J. Clean. Prod.215, 11601169. 10.1016/j.jclepro.2019.01.093

  • 48

    De MoraisM. G.CostaJ. A. V. (2007). Carbon dioxide fixation by Chlorella kessleri, C. vulgaris, Scenedesmus obliquus and Spirulina sp. cultivated in flasks and vertical tubular photobioreactors. Biotechnol. Lett.29 (9), 13491352. 10.1007/s10529-007-9394-6

  • 49

    DoC. V. T.DinhC. T.DangM. T.TranT. D.LeT. G. (2022). A novel flat-panel photobioreactor for simultaneous production of lutein and carbon sequestration by Chlorella sorokiniana TH01. Bioresour. Technol.345, 126552. 10.1016/j.biortech.2021.126552

  • 50

    DoluiD.SahaI.SarkarB.GhoshA.AdakM. K. (2021). Bicarbonate toxicity and elevated pH in plants: metabolism, regulation and tolerance. Approaches Remediat. Inorg. Pollut., 7789. 10.1007/978-981-15-6221-1_5

  • 51

    DouchaJ.StrakaF.LívanskýK. (2005). Utilization of flue gas for cultivation of microalgae Chlorella sp. in an outdoor open thin-layer photobioreactor in an outdoor open thin-layer photobioreactor. J. Appl. Phycol.17 (5), 403412. 10.1007/s10811-005-8701-7

  • 52

    DuanH.LiuW.ZhouL.HanB.HuoS.El-SheekhM.et al (2023). Improving saline-alkali soil and promoting wheat growth by co-applying potassium-solubilizing bacteria and cyanobacteria produced from brewery wastewater. Front. Environ. Sci.11, 613. 10.3389/fenvs.2023.1170734

  • 53

    DuarteJ. H.de MoraisE. G.RadmannE. M.CostaJ. A. V. (2017). Biological CO2 mitigation from coal power plant by Chlorella fusca and Spirulina sp. Bioresour. Technol.234, 472475. Epub 2017 Mar 12. PMID: 28342576. 10.1016/j.biortech.2017.03.066

  • 54

    El‐KhodaryG. M.El‐SayedH. S.KhairyH. M.El‐SheikhM. A.QiX.ElshobaryM. E. (2021). Comparative study on growth, survival and pigmentation of Solea aegyptiaca larvae by using four different microalgal species with emphasize on water quality and nutritional value. Aquac. Nutr.27 (2), 615629. 10.1111/anu.13211

  • 55

    El-SheekhM.ElshobaryM.AbdullahE.Abdel-BassetR.MetwallyM. (2023). Application of a novel biological-nanoparticle pretreatment to Oscillatoria acuminata biomass and coculture dark fermentation for improving hydrogen production. Microb. Cell. Factories22, 34. 10.1186/s12934-023-02036-y

  • 56

    ElshobaryM.AbdullahE.Abdel-BassetR.MetwallyM.El-SheekhM. (2024). Maximizing biofuel production from algal biomass: a study on biohydrogen and bioethanol production using Mg Zn ferrite nanoparticles. Algal Res.81, 103595. 10.1016/j.algal.2024.103595

  • 57

    ElshobaryM.AshourM. (2023). “Algae for aquaculture: recent technological applications,” in Value-added products from algae: phycochemical production and applications (Germany: Springer), 525561.

  • 58

    ElshobaryM. E.EssaD. I.AttiahA. M.SalemZ. E.QiX. (2020). Algal community and pollution indicators for the assessment of water quality of Ismailia canal, Egypt. Stoch. Environ. Res. Risk Assess.34, 10891103. 10.1007/s00477-020-01809-w

  • 59

    ElshobaryM. E.ZabedH. M.QiX.El-ShenodyR. A. (2022). Enhancing biomass and lipid productivity of a green microalga Parachlorella kessleri for biodiesel production using rapid mutation of atmospheric and room temperature plasma. Biotechnol. Biofuels Bioprod.15 (1), 122. 10.1186/s13068-022-02220-z

  • 60

    ElzengaJ. T. M.PrinsH. B.StefelsJ. (2000). The role of extracellular carbonic anhydrase activity in inorganic carbon utilization of Phaeocystis globosa (Prymnesiophyceae): a comparison with other marine algae using the isotopic disequilibrium technique. Limnol. Oceanogr.45 (2), 372380. 10.4319/lo.2000.45.2.0372

  • 61

    EnamalaM. K.EnamalaS.ChavaliM.DonepudiJ.YadavalliR.KolapalliB.et al (2018). Production of biofuels from microalgae-A review on cultivation, harvesting, lipid extraction, and numerous applications of microalgae. Renew. Sustain. Energy Rev.94, 4968. 10.1016/j.rser.2018.05.012

  • 62

    FanL.-H.ZhangY.-T.ZhangL.ChenH.-L. (2008). Evaluation of a membrane-sparged helical tubular photobioreactor for carbon dioxide biofixation by Chlorella vulgaris. J. Membr. Sci.325 (1), 336345. 10.1016/j.memsci.2008.07.044

  • 63

    FAO (2020). Action, SI, World fisheries and aquaculture. Food Agric. Organ.2020, 1244.

  • 64

    FarrellyD. J.EverardC. D.FaganC. C.McDonnellK. P. (2013). Carbon sequestration and the role of biological carbon mitigation: a review. Renew. Sustain. energy Rev.21, 712727. 10.1016/j.rser.2012.12.038

  • 65

    FengP.DengZ.HuZ.FanL. (2011). Lipid accumulation and growth of Chlorella zofingiensis in flat plate photobioreactors outdoors. Bioresour. Technol.102 (22), 1057710584. 10.1016/j.biortech.2011.08.109

  • 66

    FivgaA.SperanzaL. G.BrancoC. M.OuadiM.HornungA. (2019). A review on the current state of the art for the production of advanced liquid biofuels. Aims Energy7 (1), 4676. 10.3934/energy.2019.1.46

  • 67

    FuW.GudmundssonO.FeistA. M.HerjolfssonG.BrynjolfssonS.PalssonB. Ø. (2012). Maximizing biomass productivity and cell density of Chlorella vulgaris by using light-emitting diode-based photobioreactor. J. Biotechnol.161 (3), 242249. 10.1016/j.jbiotec.2012.07.004

  • 68

    GalèsA.TripletS.GeoffroyT.RoquesC.CarréC.Le Floc’hE.et al (2020). Control of the pH for marine microalgae polycultures: a key point for CO2 fixation improvement in intensive cultures. J. CO2 Util.38, 187193. 10.1016/j.jcou.2020.01.019

  • 69

    GaoS.EdmundsonS.HuesemannM. (2022). Oxygen stress mitigation for microalgal biomass productivity improvement in outdoor raceway ponds. Algal Res.68, 102901. 10.1016/j.algal.2022.102901

  • 70

    GehlK. A.CookC. M.ColmanB. (1987). The effect of external pH on the apparent CO2 affinity of Chlorella saccharophila. J. Exp. Bot.38 (7), 12031210. 10.1093/jxb/38.7.1203

  • 71

    GerottoC.NoriciA.GiordanoM. (2020). Toward enhanced fixation of CO2 in aquatic biomass: focus on microalgae. Front. Energy Res.8, 213. 10.3389/fenrg.2020.00213

  • 72

    GiordanoM.BeardallJ.RavenJ. A. (2005). CO2 COncentrating mechanisms in algae: mechanisms, environmental modulation, and evolution. Annu. Rev. plant Biol.56 (1), 99131. 10.1146/annurev.arplant.56.032604.144052

  • 73

    GohB. H. H.OngH. C.CheahM. Y.ChenW.-H.YuK. L.MahliaT. M. I. (2019). Sustainability of direct biodiesel synthesis from microalgae biomass: a critical review. Renew. Sustain. Energy Rev.107, 5974. 10.1016/j.rser.2019.02.012

  • 74

    GollakotaA.KishoreN.GuS. (2018). A review on hydrothermal liquefaction of biomass. Renew. Sustain. Energy Rev.81, 13781392. 10.1016/j.rser.2017.05.178

  • 75

    HamidiM.MohammadiA.MashhadiH.MahmoudniaF. (2023). Evaluation of effective environmental parameters on lipid, protein and beta-carotene production in Spirulina platensis microalga. Results Eng.18, 101102. 10.1016/j.rineng.2023.101102

  • 76

    HanagataN.TakeuchiT.FukujuY.BarnesD. J.KarubeI. (1992). Tolerance of microalgae to high CO2 and high temperature. Phytochemistry31 (10), 33453348. 10.1016/0031-9422(92)83682-o

  • 77

    HeubeckS.CraggsR.ShiltonA. (2007). Influence of CO2 scrubbing from biogas on the treatment performance of a high rate algal pond. Water Sci. Technol.55 (11), 193200. 10.2166/wst.2007.358

  • 78

    HongW. Y. (2022). A techno-economic review on carbon capture, utilisation and storage systems for achieving a net-zero CO2 emissions future. Carbon Capture Sci. and Technol.3, 100044. 10.1016/j.ccst.2022.100044

  • 79

    HossainN.ZainiJ.MahliaT. M. I. (2019). Life cycle assessment, energy balance and sensitivity analysis of bioethanol production from microalgae in a tropical country. Renew. Sustain. Energy Rev.115, 109371. 10.1016/j.rser.2019.109371

  • 80

    HosseiniN. S.ShangH.ScottJ. A. (2018). Biosequestration of industrial off-gas CO2 for enhanced lipid productivity in open microalgae cultivation systems. Renew. Sustain. Energy Rev.92, 458469. 10.1016/j.rser.2018.04.086

  • 81

    HuertasI. E.ColmanB.EspieG. S. (2002). Inorganic carbon acquisition and its energization in eustigmatophyte algae. Funct. plant Biol.29 (3), 271277. 10.1071/pp01181

  • 82

    HuertasI. E.ColmanB.EspieG. S.LubianL. M. (2000a). Active transport of CO2 by three species of marine microalgae. J. Phycol.36 (2), 314320. 10.1046/j.1529-8817.2000.99142.x

  • 83

    HuertasI. E.EspieG. S.ColmanB.LubianL. M. (2000b). Light-dependent bicarbonate uptake and CO2 efflux in the marine microalga Nannochloropsis gaditana. Planta211 (1), 4349. 10.1007/s004250000254

  • 84

    IghaloJ. O.DultaK.KurniawanS. B.OmoarukheF. O.EwuzieU.EshiemogieS. O.et al (2022). Progress in microalgae application for CO2 sequestration. Clean. Chem. Eng.3, 100044. 10.1016/j.clce.2022.100044

  • 85

    IglinaT.IglinP.PashchenkoD. (2022). Industrial CO2 capture by algae: a review and recent advances. Sustainability14 (7), 3801. 10.3390/su14073801

  • 86

    IsosaariP.SrivastavaV.SillanpääM. (2019). Ionic liquid-based water treatment technologies for organic pollutants: current status and future prospects of ionic liquid mediated technologies. Sci. Total Environ.690, 604619. 10.1016/j.scitotenv.2019.06.421

  • 87

    JamesC. M.Al-KharsA. (1990). An intensive continuous culture system using tubular photobioreactors for producing microalgae. Aquaculture87 (3-4), 381393. 10.1016/0044-8486(90)90075-x

  • 88

    JiménezC.CossıoB. R.NiellF. X. (2003). Relationship between physicochemical variables and productivity in open ponds for the production of Spirulina: a predictive model of algal yield. Aquaculture221 (1-4), 331345. 10.1016/s0044-8486(03)00123-6

  • 89

    Jimenez-LlanosJ.Ramirez-CarmonaM.Rendon-CastrillonL.Ocampo-LopezC. (2020a). Sustainable biohydrogen production by Chlorella sp. microalgae: a review. Int. J. Hydrogen Energy45 (15), 83108328. 10.1016/j.ijhydene.2020.01.059

  • 90

    JuddS. J.Al MomaniF.ZnadH.Al KetifeA. (2017). The cost benefit of algal technology for combined CO2 mitigation and nutrient abatement. Renew. Sustain. Energy Rev.71, 379387. 10.1016/j.rser.2016.12.068

  • 91

    KadamK. L. (1997). Power plant flue gas as a source of CO2 for microalgae cultivation: economic impact of different process options. Energy Convers. Manag.38, S505S510. 10.1016/s0196-8904(96)00318-4

  • 92

    KadamK. L. (2001). Microalgae production from power plant flue gas: environmental implications on a life cycle basis. Golden, CO (United States): National Renewable Energy Lab.NREL.

  • 93

    KazbarA.CogneG.UrbainB.MarecH.Le-GouicB.TallecJ.et al (2019). Effect of dissolved oxygen concentration on microalgal culture in photobioreactors. Algal Res.39, 101432. 10.1016/j.algal.2019.101432

  • 94

    KhalekuzzamanM.KabirS. B.IslamM. B.DattaP.AlamM. A.XuJ. (2021). Enhancing microalgal productivity and quality by different colored photobioreactors for biodiesel production using anaerobic reactor effluent. Biomass Convers. Biorefinery11, 767779. 10.1007/s13399-020-00852-5

  • 95

    KhanS. A.HussainM. Z.PrasadS.BanerjeeU. (2009). Prospects of biodiesel production from microalgae in India. Renew. Sustain. energy Rev.13 (9), 23612372. 10.1016/j.rser.2009.04.005

  • 96

    KhooK. S.ChewK. W.YewG. Y.LeongW. H.ChaiY. H.ShowP. L.et al (2020). Recent advances in downstream processing of microalgae lipid recovery for biofuel production. Bioresour. Technol.304, 122996. 10.1016/j.biortech.2020.122996

  • 97

    KlinthongW.YangY.-H.HuangC.-H.TanC.-S. (2015). A review: microalgae and their applications in CO2 capture and renewable energy. Aerosol Air Qual. Res.15 (2), 712742. 10.4209/aaqr.2014.11.0299

  • 98

    KohH. G.ChoJ. M.JeonS.ChangY. K.LeeB.KangN. K. (2023). Transcriptional insights into Chlorella sp. ABC-001: a comparative study of carbon fixation and lipid synthesis under different CO2 conditions. Biotechnol. Biofuels Bioprod.16 (1), 113. 10.1186/s13068-023-02358-4

  • 99

    KorbR. E.SavilleP. J.JohnstonA. M.RavenJ. A. (1997). Sources of inorganic carbon for photosynthesis by three species of marine diatom 1. J. Phycol.33 (3), 433440. 10.1111/j.0022-3646.1997.00433.x

  • 100

    KumariS.KumarV.KothariR.KumarP. (2022). Nutrient sequestration and lipid production potential of Chlorella vulgaris under pharmaceutical wastewater treatment: experimental, optimization, and prediction modeling studies.

  • 101

    KusmiyatiK.HeratriA.KubikazariS.HidayatA.HadiyantoH. (2020). Hydrolysis of microalgae spirulina platensis, chlorella sp., and macroalgae ulva lactuca for bioethanol production. Int. Energy J.20 (4), 611620.

  • 102

    LakatosG. E.RanglováK.ManoelJ. C.GrivalskýT.KopeckýJ.MasojídekJ. (2019). Bioethanol production from microalgae polysaccharides. Folia Microbiol.64, 627644. 10.1007/s12223-019-00732-0

  • 103

    LamM. K.LeeK. T. (2014). Cultivation of Chlorella vulgaris in a pilot-scale sequential-baffled column photobioreactor for biomass and biodiesel production. Energy Convers. Manag.88, 399410. 10.1016/j.enconman.2014.08.063

  • 104

    LamM. K.LoyA. C. M.YusupS.LeeK. T. (2019). Biohydrogen production from algae. China: Biohydrogen. Elsevier, 219245.

  • 105

    LamareD. W.ChaurasiaN. (2022). “Microalgae and cyanobacteria: a potential source for drug discovery using genome mining approach,” in Micro-algae: next-generation feedstock for biorefineries (Germany: Springer), 177204.

  • 106

    LiJ.XiongZ.ZengK.ZhongD.ZhangX.ChenW.et al (2021). Characteristics and evolution of nitrogen in the heavy components of algae pyrolysis bio-oil. Environ. Sci. and Technol.55 (9), 63736385. 10.1021/acs.est.1c00676

  • 107

    LiQ.DuW.LiuD. (2008). Perspectives of microbial oils for biodiesel production. Appl. Microbiol. Biotechnol.80 (5), 749756. 10.1007/s00253-008-1625-9

  • 108

    LiS.LiX.HoS.-H. (2022). Microalgae as a solution of third world energy crisis for biofuels production from wastewater toward carbon neutrality: an updated review. Chemosphere291, 132863. 10.1016/j.chemosphere.2021.132863

  • 109

    LiS.LuoS.GuoR. (2013). Efficiency of CO2 fixation by microalgae in a closed raceway pond. Bioresour. Technol.136, 267272. 10.1016/j.biortech.2013.03.025

  • 110

    LimH. R.KhooK. S.ChewK. W.ChangC.-K.MunawarohH. S. H.KumarP. S.et al (2021). Perspective of Spirulina culture with wastewater into a sustainable circular bioeconomy. Environ. Pollut.284, 117492. 10.1016/j.envpol.2021.117492

  • 111

    LokugeN.AndersS. (2022). Carbon-credit systems in agriculture: a review of literature. Sch. Public Policy Publ.15.

  • 112

    MalekghasemiS.KariminiaH.-R.PlechkovaN. K.WardV. C. (2021). Direct transesterification of wet microalgae to biodiesel using phosphonium carboxylate ionic liquid catalysts. Biomass Bioenergy150, 106126. 10.1016/j.biombioe.2021.106126

  • 113

    MansourA. T.AshourM.AbbasE. M.AlsaqufiA. S.KelanyM. S.El-SawyM. A.et al (2022a). Growth performance, immune-related and antioxidant genes expression, and gut bacterial abundance of pacific white leg shrimp, Litopenaeus vannamei, dietary supplemented with natural astaxanthin. Front. Physiology13 (874172), 874172. 10.3389/fphys.2022.874172

  • 114

    MansourA. T.AshryO.AshourM.AlsaqufiA. S.RamadanK. M. A.SharawyZ. Z. (2022b). The optimization of dietary protein level and carbon sources on biofloc nutritive values, bacterial abundance, and growth performances of whiteleg shrimp (Litopenaeus vannamei) juveniles. Life12 (6), 888. 10.3390/life12060888

  • 115

    MarkouG.VandammeD.MuylaertK. (2014). Ammonia inhibition on Arthrospira platensis in relation to the initial biomass density and pH. Bioresour. Technol.166, 259265. 10.1016/j.biortech.2014.05.040

  • 116

    MathimaniT.BaldinelliA.RajendranK.PrabakarD.MatheswaranM.van LeeuwenR. P.et al (2019). Review on cultivation and thermochemical conversion of microalgae to fuels and chemicals: process evaluation and knowledge gaps. J. Clean. Prod.208, 10531064. 10.1016/j.jclepro.2018.10.096

  • 117

    MeloM.FernandesS.CaetanoN.BorgesM. T. (2018). Chlorella vulgaris (SAG 211-12) biofilm formation capacity and proposal of a rotating flat plate photobioreactor for more sustainable biomass production. J. Appl. Phycol.30 (2), 887899. 10.1007/s10811-017-1290-4

  • 118

    MetzB.DavidsonO.De ConinckH.LoosM.MeyerL. (2005). IPCC special report on carbon dioxide capture and storage. Cambridge: Cambridge University Press.

  • 119

    MinM.WangL.LiY.MohrM. J.HuB.ZhouW.et al (2011). Cultivating Chlorella sp. in a pilot-scale photobioreactor using centrate wastewater for microalgae biomass production and wastewater nutrient removal. Appl. Biochem. Biotechnol.165 (1), 123137. 10.1007/s12010-011-9238-7

  • 120

    MohamedA. (2018). System for harvesting microalgae. Efypt Pat. Appl.333/26022012.

  • 121

    MondalM.GoswamiS.GhoshA.OinamG.TiwariO.DasP.et al (2017). Production of biodiesel from microalgae through biological carbon capture: a review. 3 Biotech.7 (2), 9921. 10.1007/s13205-017-0727-4

  • 122

    MonjedM. K.AchourB.RobsonG. D.PittmanJ. K. (2021). Improved saccharification of Chlorella vulgaris biomass by fungal secreted enzymes for bioethanol production. Algal Res.58, 102402. 10.1016/j.algal.2021.102402

  • 123

    MoradiP.SaidiM. (2022). Biodiesel production from Chlorella Vulgaris microalgal-derived oil via electrochemical and thermal processes. Fuel Process. Technol.228, 107158. 10.1016/j.fuproc.2021.107158

  • 124

    MoralesM.SánchezL.RevahS. (2018). The impact of environmental factors on carbon dioxide fixation by microalgae. FEMS Microbiol. Lett.365 (3), fnx262. 10.1093/femsle/fnx262

  • 125

    MoroneyJ. V.JungnickN.DiMarioR. J.LongstrethD. J. (2013). Photorespiration and carbon concentrating mechanisms: two adaptations to high O2, low CO2 conditions. Photosynth. Res.117 (1), 121131. 10.1007/s11120-013-9865-7

  • 126

    MoroneyJ. V.YnalvezR. A. (2007). Proposed carbon dioxide concentrating mechanism in Chlamydomonas reinhardtii. Eukaryot. Cell.6 (8), 12511259. 10.1128/ec.00064-07

  • 127

    MustafaA.LougouB. G.ShuaiY.WangZ.TanH. (2020). Current technology development for CO2 utilization into solar fuels and chemicals: a review. J. Energy Chem.49, 96123. 10.1016/j.jechem.2020.01.023

  • 128

    NajmY.JeongS.LeiknesT. (2017). Nutrient utilization and oxygen production by Chlorella vulgaris in a hybrid membrane bioreactor and algal membrane photobioreactor system. Bioresour. Technol.237, 6471. 10.1016/j.biortech.2017.02.057

  • 129

    NandaN. (2022). Bioplastic production from Chlorella sp., and synthesis of biochar from residual biomass, characterization, and its application.

  • 130

    NapanK.TengL.QuinnJ. C.WoodB. D. (2015). Impact of heavy metals from flue gas integration with microalgae production. Algal Res.8, 8388. 10.1016/j.algal.2015.01.003

  • 131

    NayakM.SuhW. I.LeeB.ChangY. K. (2018). Enhanced carbon utilization efficiency and FAME production of Chlorella sp. HS2 through combined supplementation of bicarbonate and carbon dioxide. Energy Convers. Manag.156, 4552. 10.1016/j.enconman.2017.11.002

  • 132

    NgangkhamM.RathaS. K.PrasannaR.SaxenaA. K.DharD. W.SarikaC.et al (2012). Biochemical modulation of growth, lipid quality and productivity in mixotrophic cultures of Chlorella sorokiniana. SpringerPlus1, 3313. 10.1186/2193-1801-1-33

  • 133

    NguyenT. T.LamM. K.UemuraY.MansorN.LimJ. W.ShowP. L.et al (2020). High biodiesel yield from wet microalgae paste via in-situ transesterification: effect of reaction parameters towards the selectivity of fatty acid esters. Fuel272, 117718. 10.1016/j.fuel.2020.117718

  • 134

    NguyenX. P.HoangA. T.ÖlçerA. I.HuynhT. T. (2021). Record decline in global CO2 emissions prompted by COVID-19 pandemic and its implications on future climate change policies. Energy Sources, Part A Recovery, Util. Environ. Eff., 14. 10.1080/15567036.2021.1879969

  • 135

    NunezC. (2019). Carbon dioxide levels are at a record high. Here’s what you need to know. Natl. Geogr.13.

  • 136

    OkekeE. S.EjeromedogheneO.OkoyeC. O.EzeorbaT. P. C.NyaruabaR.IkechukwuC. K.et al (2022). Microalgae biorefinery: an integrated route for the sustainable production of high-value-added products. Energy Convers. Manag.X, 100323. 10.1016/j.ecmx.2022.100323

  • 137

    OsmanA. I.HefnyM.Abdel MaksoudM. I. A.ElgarahyA. M.RooneyD. W. (2021). Recent advances in carbon capture storage and utilisation technologies: a review. Environ. Chem. Lett.19 (2), 797849. 10.1007/s10311-020-01133-3

  • 138

    OsmanM. E.Abo-ShadyA. M.ElshobaryM. E.Abd El-GhafarM. O.HaneltD.AbomohraA. (2023a). Exploring the prospects of fermenting/Co-fermenting marine biomass for enhanced bioethanol production. Fermentation9 (11), 934. 10.3390/fermentation9110934

  • 139

    OsmanM. E.Abo-ShadyA. M.GhedaS. F.DesokiS. M.ElshobaryM. E. (2023b). Unlocking the potential of microalgae cultivated on wastewater combined with salinity stress to improve biodiesel production. Environ. Sci. Pollut. Res.30 (53), 114610114624. 10.1007/s11356-023-30370-6

  • 140

    PalmqvistK.YuJ. W.BadgerM. R. (1994). Carbonic anhydrase activity and inorganic carbon fluxes in low- and high-Ci cells of Chlamydomonas reinhardtii and Scenedesmus obliquus. Physiol. Plant.90 (3), 537547. 10.1034/j.1399-3054.1994.900315.x

  • 141

    ParkJ.KumarG.BakonyiP.PeterJ.NemestóthyN.KoterS.et al (2021). Comparative evaluation of CO 2 fixation of microalgae strains at various CO 2 aeration conditions. Waste Biomass Valorization12, 29993007. 10.1007/s12649-020-01226-8

  • 142

    PavithraK. G.KumarP. S.JaikumarV.VardhanK. H.SundarRajanP. (2020). Microalgae for biofuel production and removal of heavy metals: a review. Environ. Chem. Lett.18, 19051923. 10.1007/s10311-020-01046-1

  • 143

    Penhaul SmithJ.HughesA.McEvoyL.ThorntonB.DayJ. (2021). The carbon partitioning of glucose and DIC in mixotrophic, heterotrophic and photoautotrophic cultures of Tetraselmis suecica. Biotechnol. Lett.43, 729743. 10.1007/s10529-020-03073-y

  • 144

    PhwanC. K.OngH. C.ChenW.-H.LingT. C.NgE. P.ShowP. L. (2018). Overview: comparison of pretreatment technologies and fermentation processes of bioethanol from microalgae. Energy Convers. Manag.173, 8194. 10.1016/j.enconman.2018.07.054

  • 145

    PolitaevaN.IlinI.VelmozhinaK.ShinkevichP. (2023). Carbon dioxide utilization using chlorella microalgae. Environments10, 109.

  • 146

    PrasadR.GuptaS. K.ShabnamN.OliveiraC. Y. B.NemaA. K.AnsariF. A.et al (2021). Role of microalgae in global CO2 sequestration: physiological mechanism, recent development, challenges, and future prospective. Sustainability13 (23), 13061. 10.3390/su132313061

  • 147

    RanglováK.ManoelJ. C.LakatosG. E.GrivalskýT.MasojídekJ. (2022). Microalgae as an aquaculture feed produced in short light-path annular column photobioreactor.

  • 148

    RassoolD. (2021). Unlocking private finance to support CCS investments. USA: Global CCS Institute.

  • 149

    RenH.TuoJ.AddyM. M.ZhangR.LuQ.AndersonE.et al (2017). Cultivation of Chlorella vulgaris in a pilot-scale photobioreactor using real centrate wastewater with waste glycerol for improving microalgae biomass production and wastewater nutrients removal. Bioresour. Technol.245, 11301138. 10.1016/j.biortech.2017.09.040

  • 150

    RinantiA.KardenaE.AstutiD.DewiK. (2014). Improvement of carbon dioxide removal through artificial light intensity and temperature by constructed green microalgae consortium in a vertical bubble column photobioreactor.

  • 151

    RotatoreC.ColmanB. (1991). The active uptake of carbon dioxide by the unicellular green algae Chlorella saccharophila and C. ellipsoidea. Plant, Cell. and Environ.14 (4), 371375. 10.1111/j.1365-3040.1991.tb00945.x

  • 152

    RotatoreC.ColmanB. (1992). Active uptake of CO2 by the diatom Navicula pelliculosa. J. Exp. Bot.43 (4), 571576. 10.1093/jxb/43.4.571

  • 153

    RotatoreC.ColmanB.KuzmaM. (1995). The active uptake of carbon dioxide by the marine diatoms Phaeodactylum ticornutum and Cyclotella sp. Plant, Cell. and Environ.18 (8), 913918. 10.1111/j.1365-3040.1995.tb00600.x

  • 154

    RubinE. S.DavisonJ. E.HerzogH. J. (2015). The cost of CO2 capture and storage. Int. J. Greenh. gas control40, 378400. 10.1016/j.ijggc.2015.05.018

  • 155

    SadeghizadehA.MoghaddasiL.RahimiR. (2017). CO2 capture from air by Chlorella vulgaris microalgae in an airlift photobioreactor. Bioresour. Technol.243, 441447. 10.1016/j.biortech.2017.06.147

  • 156

    SatohA.KuranoN.MiyachiS. (2001). Inhibition of photosynthesis by intracellular carbonic anhydrase in microalgae under excess concentrations of CO2. Photosynth. Res.68 (3), 215224. 10.1023/a:1012980223847

  • 157

    SayreR. (2010). Microalgae: the potential for carbon capture. Bioscience60 (9), 722727. 10.1525/bio.2010.60.9.9

  • 158

    SerejoM. L.PosadasE.BonczM. A.BlancoS. l.García-EncinaP.MunozR. l. (2015). Influence of biogas flow rate on biomass composition during the optimization of biogas upgrading in microalgal-bacterial processes. Environ. Sci. and Technol.49 (5), 32283236. 10.1021/es5056116

  • 159

    SeroE. T.SizibaN.BunhuT.ShokoR.JonathanE. (2020). Biophotonics for improving algal photobioreactor performance: a review. Int. J. Energy Res.44 (7), 50715092. 10.1002/er.5059

  • 160

    ShareefdeenZ.ElkamelA.BabarZ. B. (2023). Recent developments on the performance of algal bioreactors for CO2 removal: focusing on the light intensity and photoperiods. BioTech12 (1), 10. 10.3390/biotech12010010

  • 161

    SharmaA. K.SahooP. K.SinghalS. (2016). Comparative evolution of biomass production and lipid accumulation potential of Chlorella species grown in a bubble column photobioreactor. Biofuels7 (4), 389399. 10.1080/17597269.2015.1138040

  • 162

    ShreyashN.SonkerM.BajpaiS.TiwaryS. K.KhanM. A.RajS.et al (2021). The review of carbon capture-storage technologies and developing fuel cells for enhancing utilization. Energies14 (16), 4978. 10.3390/en14164978

  • 163

    SommerU.StiborH.KatechakisA.SommerF.HansenT. (2002). “Pelagic food web configurations at different levels of nutrient richness and their implications for the ratio fish production: primary production,” in Sustainable increase of marine harvesting: fundamental mechanisms and new concepts (Germany: Springer), 1120.

  • 164

    SongC.LiuQ.DengS.LiH.KitamuraY. (2019). Cryogenic-based CO2 capture technologies: state-of-the-art developments and current challenges. Renew. Sustain. Energy Rev.101, 265278. 10.1016/j.rser.2018.11.018

  • 165

    SoulièsA.LegrandJ.MarecH.PruvostJ.CastelainC.BurgheleaT.et al (2016). Investigation and modeling of the effects of light spectrum and incident angle on the growth of <scp>C</scp>hlorella vulgaris in photobioreactors. Biotechnol. Prog.32 (2), 247261. 10.1002/btpr.2244

  • 166

    StephensonP. G.MooreC. M.TerryM. J.ZubkovM. V.BibbyT. S. (2011). Improving photosynthesis for algal biofuels: toward a green revolution. Trends Biotechnol.29 (12), 615623. 10.1016/j.tibtech.2011.06.005

  • 167

    SultemeyerD. F.MillerA. G.EspieG. S.FockH. P.CanvinD. T. (1989). Active CO2 transport by the green alga Chlamydomonas reinhardtii. Plant Physiol.89 (4), 12131219. 10.1104/pp.89.4.1213

  • 168

    TanX.ChuH.ZhangY.YangL.ZhaoF.ZhouX. (2014). Chlorella pyrenoidosa cultivation using anaerobic digested starch processing wastewater in an airlift circulation photobioreactor. Bioresour. Technol.170, 538548. 10.1016/j.biortech.2014.07.086

  • 169

    TanX.-B.WanX.-P.YangL.-B.WangX.MengJ.JiangM.-J.et al (2021). Nutrients recycling and biomass production from Chlorella pyrenoidosa culture using anaerobic food processing wastewater in a pilot-scale tubular photobioreactor. Chemosphere270, 129459. 10.1016/j.chemosphere.2020.129459

  • 170

    ThomasD. M.MecheryJ.PauloseS. V. (2016). Carbon dioxide capture strategies from flue gas using microalgae: a review. Environ. Sci. Pollut. Res.23, 1692616940. 10.1007/s11356-016-7158-3

  • 171

    ToumiA.PolitaevaN.ĐurovićS.MukhametovaL.IlyashenkoS. (2022). Obtaining DHA–EPA oil concentrates from the biomass of microalga chlorella sorokiniana. Resources11 (2), 20. 10.3390/resources11020020

  • 172

    TrevesH.KükenA.ArrivaultS.IshiharaH.HoppeI.ErbanA.et al (2022). Carbon flux through photosynthesis and central carbon metabolism show distinct patterns between algae, C3 and C4 plants. Nat. plants8 (1), 7891. 10.1038/s41477-021-01042-5

  • 173

    Valdovinos-GarcíaE. M.Barajas-FernándezJ.Olán-AcostaM. D. L. Á.Petriz-PrietoM. A.Guzmán-LópezA.Bravo-SánchezM. G. (2020). Techno-economic study of CO2 capture of a thermoelectric plant using microalgae (Chlorella vulgaris) for production of feedstock for bioenergy. Energies13 (2), 413. 10.3390/en13020413

  • 174

    Valdovinos-GarcíaE. M.Petriz-PrietoM. A.Olán-AcostaM. d.l.Á.Barajas-FernándezJ.Guzmán-LópezA.Bravo-SánchezM. G. (2021). Production of microalgal biomass in photobioreactors as feedstock for bioenergy and other uses: a techno-economic study of harvesting stage. Appl. Sci.11 (10), 4386. 10.3390/app11104386

  • 175

    Van Den HendeS.VervaerenH.BoonN. (2012). Flue gas compounds and microalgae:(Bio-) chemical interactions leading to biotechnological opportunities. Biotechnol. Adv.30 (6), 14051424. 10.1016/j.biotechadv.2012.02.015

  • 176

    van LeeuwenC.SgubinG.BoisB.OllatN.SwingedouwD.ZitoS.et al (2024). Climate change impacts and adaptations of wine production. Nat. Rev. Earth and Environ.5, 258275. 10.1038/s43017-024-00521-5

  • 177

    VelmozhinaK.ShinkevichP.ZhazhkovV.PolitaevaN.KorablevV.VladimirovI.et al (2023). Production of biohydrogen from microalgae biomass after wastewater treatment and air purification from CO2. Processes11 (10), 2978. 10.3390/pr11102978

  • 178

    VitovaM.BisovaK.KawanoS.ZachlederV. (2015). Accumulation of energy reserves in algae: from cell cycles to biotechnological applications. Biotechnol. Adv.33 (6), 12041218. 10.1016/j.biotechadv.2015.04.012

  • 179

    VoH.-N.-P.BuiX.-T.NguyenT.-T.NguyenD. D.DaoT.-S.CaoN.-D.-T.et al (2018). RETRACTED: effects of nutrient ratios and carbon dioxide bio-sequestration on biomass growth of Chlorella sp. in bubble column photobioreactor. J. Environ. Manag.219, 18. 10.1016/j.jenvman.2018.04.109

  • 180

    VuppaladadiyamA. K.VuppaladadiyamS. S. V.SikarwarV. S.AhmadE.PantK. K.MurugavelhS.et al (2023). A critical review on biomass pyrolysis: reaction mechanisms, process modeling and potential challenges. J. Energy Inst.108, 101236. 10.1016/j.joei.2023.101236

  • 181

    WangH.HuX.ElshobaryM.SobhiM.ZhuF.CuiY.et al (2024). Integrated partial nitrification and Tribonema minus cultivation for cost-effective ammonia recovery and lipid production from slaughterhouse wastewater. Chem. Eng. J.152199.

  • 182

    WangK.KhooK. S.ChewK. W.SelvarajooA.ChenW.-H.ChangJ.-S.et al (2021). Microalgae: the future supply house of biohydrogen and biogas. Front. Energy Res.9, 660399. 10.3389/fenrg.2021.660399

  • 183

    WatanabeY.SaikiH. (1997). Development of a photobioreactor incorporating Chlorella sp. for removal of CO2 in stack gas. Energy Convers. Manag.38, S499S503. 10.1016/s0196-8904(96)00317-2

  • 184

    WeiL.ShenC.El HajjamiM.YouW.WangQ.ZhangP.et al (2019). Knockdown of carbonate anhydrase elevates Nannochloropsis productivity at high CO2 level. Metab. Eng.54, 96108. 10.1016/j.ymben.2019.03.004

  • 185

    WuH.-H.GauS.-H.LiM.-G.ChenY.-J.SunC.-J. (2015). Effects of Chlorella sp. on nutrient treatment in cultures with different carbon to nitrogen ratios. Water Sci. Technol.71 (11), 15971603. 10.2166/wst.2015.123

  • 186

    WuW.TanL.ChangH.ZhangC.TanX.LiaoQ.et al (2023). Advancements on process regulation for microalgae-based carbon neutrality and biodiesel production. Renew. Sustain. Energy Rev.171, 112969. 10.1016/j.rser.2022.112969

  • 187

    XuG.LiY.HouW.WangS.KongF. (2021). Effects of substrate type on enhancing pollutant removal performance and reducing greenhouse gas emission in vertical subsurface flow constructed wetland. J. Environ. Manag.280, 111674. 10.1016/j.jenvman.2020.111674

  • 188

    XuG.LiangF.YangY.HuY.ZhangK.LiuW. (2014). An improved CO2 separation and purification system based on cryogenic separation and distillation theory. Energies7 (5), 34843502. 10.3390/en7053484

  • 189

    YaakobM. A.MohamedR. M. S. R.Al-GheethiA.Aswathnarayana GokareR.AmbatiR. R. (2021). Influence of nitrogen and phosphorus on microalgal growth, biomass, lipid, and fatty acid production: an overview. Cells10 (2), 393. 10.3390/cells10020393

  • 190

    YamashitaS.MiyazawaT.HiguchiO.TakekoshiH.MiyazawaT.KinoshitaM. (2022). Characterization of glycolipids in the strain chlorella pyrenoidosa. J. Nutr. Sci. Vitaminology68 (4), 353357. 10.3177/jnsv.68.353

  • 191

    YirguZ.LetaS.HussenA.KhanM. M.AragawT. (2023). Pretreatment of lipid-extracted biomass of Scenedesmus sp. grown in wastewater for bioethanol production. Biomass Convers. Biorefinery14, 1686716878. 10.1007/s13399-023-03917-3

  • 192

    YuG.NakajimaK.GruberA.Rio BartulosC.SchoberA. F.LepetitB.et al (2022). Mitochondrial phosphoenolpyruvate carboxylase contributes to carbon fixation in the diatom Phaeodactylum tricornutum at low inorganic carbon concentrations. New Phytol.235, 13791393. 10.1111/nph.18268

  • 193

    YuQ.WangH.LiX.YinY.QinS.GeB. (2020). Enhanced biomass and CO2 sequestration of Chlorella vulgaris using a new mixotrophic cultivation method. Process Biochem.90, 168176. 10.1016/j.procbio.2019.11.022

  • 194

    YueL.ChenW. (2005). Isolation and determination of cultural characteristics of a new highly CO2 tolerant fresh water microalgae. Energy Convers. Manag.46 (11-12), 18681876. 10.1016/j.enconman.2004.10.010

  • 195

    ZabedH. M.AkterS.YunJ.ZhangG.ZhangY.QiX. (2020). Biogas from microalgae: technologies, challenges and opportunities. Renew. Sustain. Energy Rev.117, 109503. 10.1016/j.rser.2019.109503

  • 196

    ZengJ.WangZ.ChenG. (2021). Biological characteristics of energy conversion in carbon fixation by microalgae. Renew. Sustain. Energy Rev.152, 111661. 10.1016/j.rser.2021.111661

  • 197

    ZengX.DanquahM. K.ChenX. D.LuY. (2011). Microalgae bioengineering: from CO2 fixation to biofuel production. Renew. Sustain. Energy Rev.15 (6), 32523260. 10.1016/j.rser.2011.04.014

  • 198

    ZhangD.SongJ. (2014). Mechanisms for geological carbon sequestration. Procedia IUTAm10, 319327. 10.1016/j.piutam.2014.01.027

  • 199

    ZhangH.ZhouY.LiuT. Q.YinX. J.LinL.LinQ.et al (2021). Initiation of efficient C<sub>4</sub> pathway in response to low ambient CO<sub>2</sub> during the bloom period of a marine dinoflagellate. Environ. Microbiol.23 (6), 31963211. 10.1111/1462-2920.15545

  • 200

    ZhangS.LiuZ. (2021). Advances in the biological fixation of carbon dioxide by microalgae. J. Chem. Technol. and Biotechnol.96 (6), 14751495. 10.1002/jctb.6714

  • 201

    ZhengQ.XuX.MartinG. J.KentishS. E. (2018). Critical review of strategies for CO2 delivery to large-scale microalgae cultures. Chin. J. Chem. Eng.26 (11), 22192228. 10.1016/j.cjche.2018.07.013

  • 202

    ZhouL.LiK.DuanX.HillD.BarrowC.DunsheaF.et al (2022). Bioactive compounds in microalgae and their potential health benefits. Food Biosci.49, 101932. 10.1016/j.fbio.2022.101932

  • 203

    ZhouW.WangJ.ChenP.JiC.KangQ.LuB.et al (2017). Bio-mitigation of carbon dioxide using microalgal systems: advances and perspectives. Renew. Sustain. Energy Rev.76, 11631175. 10.1016/j.rser.2017.03.065

  • 204

    ZuñigaC.LeveringJ.AntoniewiczM. R.GuarnieriM. T.BetenbaughM. J.ZenglerK. (2018). Predicting dynamic metabolic demands in the photosynthetic eukaryote Chlorella vulgaris. Plant physiol.176 (1), 450462. 10.1104/pp.17.00605

Summary

Keywords

Chlorella, climate change, CO2 fixation, carbon concentration mechanism, algal biomass, flue gas

Citation

Ashour M, Mansour AT, Alkhamis YA and Elshobary M (2024) Usage of Chlorella and diverse microalgae for CO2 capture - towards a bioenergy revolution. Front. Bioeng. Biotechnol. 12:1387519. doi: 10.3389/fbioe.2024.1387519

Received

17 February 2024

Accepted

05 August 2024

Published

20 August 2024

Volume

12 - 2024

Edited by

Klaus Von Schwartzenberg, University of Hamburg, Germany

Reviewed by

Ihana Aguiar Severo, Florida State University, United States

Sachitra Kumar Ratha, National Botanical Research Institute (CSIR), India

Updates

Copyright

*Correspondence: Mohamed Ashour, ; Abdallah Tageldein Mansour, ; Mostafa Elshobary,

Disclaimer

All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article or claim that may be made by its manufacturer is not guaranteed or endorsed by the publisher.

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