| Literature DB >> 36159694 |
Piroonporn Srimongkol1, Papassara Sangtanoo1, Pajareeya Songserm1, Wannapawn Watsuntorn2, Aphichart Karnchanatat1.
Abstract
Over the last several decades, concerns about climate change and pollution due to human activity has gained widespread attention. Microalgae have been proposed as a suitable biological platform to reduce carbon dioxide, a major greenhouse gas, while also creating commercial sources of high-value compounds such as medicines, cosmetics, food, feed, and biofuel. Industrialization of microalgae culture and valorization is still limited by significant challenges in scaling up the production processes due to economic constraints and productivity capacities. Therefore, a boost in resource usage efficiency is required. This enhancement not only lowers manufacturing costs but also enhancing the long-term viability of microalgae-based products. Using wastewater as a nutrient source is a great way to reduce manufacturing costs. Furthermore, water scarcity is one of the most important global challenges. In recent decades, industrialization, globalization, and population growth have all impacted freshwater resources. Moreover, high amounts of organic and inorganic toxins in the water due to the disposal of waste into rivers can have severe impacts on human and animal health. Microalgae cultures are a sustainable solution to tertiary and quaternary treatments since they have the ability to digest complex contaminants. This review presents biorefineries based on microalgae from all angles, including the potential for environmental pollution remediation as well as applications for bioenergy and value-added biomolecule production. An overview of current information about microalgae-based technology and a discussion of the associated hazards and opportunities for the bioeconomy are highlighted.Entities:
Keywords: bioenergy; biomolecule production; biorefineries; microalgae; wastewater treatment
Year: 2022 PMID: 36159694 PMCID: PMC9489850 DOI: 10.3389/fbioe.2022.904046
Source DB: PubMed Journal: Front Bioeng Biotechnol ISSN: 2296-4185
FIGURE 1Wastewater integrated algal-biorefinery for biofuel and other value-added compound productions (created with BioRender.com).
Several studies of microalgae growth coupled with wastewater treatment for biofuel and other value-added compounds production.
| Microalgae | Sources of wastewater | Process | Bioproduct | References |
|---|---|---|---|---|
| Microalgae consortium | 85–90% carpet industry effluents with 10–15% municipal sewage | Cultured in Erlenmeyer flasks | 63.9% biodiesel of algal oil |
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| Piggery wastewater | Semi-continuous feeding operation in the tubular bubble column photobioreactors under outdoor conditions | 9.19 g biodiesel/100 g dry weight |
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| Municipal wastewater | Cultivated in High-Rate Algal Pond (HRAP) | 70.9% yield of biodiesel |
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| Microalgae | Wastewater-grown microalgae | Fermentation by | 9.74 g L−1 of total acetone, butanol, and ethanol (ABE) |
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| Municipal wastewater | Microalgae biomass production and fermentation | 94.3 mg ethanol/g biomass |
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| Wastewater treatment effluent from tilapia culture pond | Microalgae biomass production and fermentation | 33.213 g ethanol L−1 |
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| Urban wastewater | Microalgae biomass production and dark fermentation using | 56.8 ml H2 g−1 VS. |
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| Artificial wastewater | Sulfur deprivation and two light quality priors to anaerobic condition | 128 ml H2 L−1 (productivity 204.8 ml H2 L−1 d−1) |
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| Synthetic and wastewater media | Cultured in synthetic medium, wastewater (sterilized and non-sterilized) and digestate from anaerobic digestion of pulp and paper biosludge (sterilized and non-sterilized) | 154–252 L CH4 kg−1 (depending on culture media) |
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| Domestic sewage | High-rate algal ponds (HRAP) for post-treating Up flow anaerobic sludge blanket (UASB) reactors’ effluent and anaerobic co-digestion with microalgae | 156–211 NL CH4 kgvs −1 |
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| Primary-treated sewage (PTS), Primary-treated piggery wastewater (PTP) | Cultured in wastewater with serial dilution | 5.1 and 5.9% of the total biomass of the PTS and PTP |
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| Industrial wastewater | Cultured in Erlenmeyer flasks | 179 mg phycobiliproteins/g dry weight |
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| Aquaculture effluents | Cultured in Erlenmeyer flasks sealed with hydrophobic cotton and agitated by an air flow | 31% proteins, 6% lipids and 39% carbohydrates of |
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Nutrient compositions in different microalgae species and their health benefits.
| Microalgae | Active compounds | Health benefits | References |
|---|---|---|---|
| Carbohydrate | |||
| Chlamydomonas reinhardtii | Ara, Rha, Rib, Xyl, Gal, Glc | Antioxidant properties |
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| Gyrodinium impudicum | Gal | Anti-viral activity, immunostimulatory |
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| Nostoc flagelliforme | Glu, Gal, GlcA Xyl, Man | Anti-viral activity, antithrombin activity |
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| Aphanothece sacrum | Glc, Fuc, GalA, Rha, GlcA, Gal, Man, Xyl | Anti-inflammatory, anti-allergic, adsorption of metal ions, liquid crystallization |
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| Protein | |||
| Schizochytrium limacinum | Short peptide with molecular weight about 5–10 kDa | Antioxidant properties |
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| Synechococcus sp. VDW | Short peptide with molecular weight <3 kDa | Antioxidant, anti-inflammatory and anti-colon cancer (SW 620) |
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| C. vulgaris | Short peptide with molecular weight <1.3 kDa | Antioxidant, antiproliferation and induced a post-G1 cell cycle arrest of human gastric cancer cell lines |
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| C. vulgaris | Di- and tri-peptides | Anti-diabetes (type 2) |
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| C. ellipsoidea | Short peptide with molecular weight 467.2 Da | Reduces blood pressure levels |
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| Lipid | |||
| Nannochloropsis, Schizochytrium | EPA and DHA | Protection of neurons |
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| Phaeodactylum tricornutum | EPA | Antibacterial activity (Staphylococcus aureus) |
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| Isochrysis, Nannochloropsis, Phaeodactylum, Pavlova and Thalassiosira | Omega-3 | Fetal neurodevelopment, anti-inflammatory, antibiotic, antiproliferative, anti-arrythmic, anti-atherosclerotic, and anti-thrombotic properties |
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| S. intermedius | Fatty acid methyl esters | Antibacterial activity (Escherichia coli and Pseudomonas aeruginosa |
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| Pigment | |||
| | Astaxanthin | Antioxidant activity, anticancer properties and the ability to prevent diseases |
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| Dunaliella salina | β-carotene | Preventing night blindness and liver fibrosis and improving the immune system |
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| | phycocyanin | Anticancer, anti-diabetic and anti-inflammatory |
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| | Lutein | Prevent some types of cancer and cardiovascular disease |
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| | Violaxanthin | Anti-inflammatory, anti-cancer |
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Role of microalgae in different types of wastewaters in terms of nutrient removal efficiency, incubation time, and microalgae production.
| Wastewater source | Microalgae | Cultivation system | Nutrient removal efficiency (%) | Incubation time (d) | Micro algae production | References |
|---|---|---|---|---|---|---|
| Municipal wastewater |
| 2.5-L photobioreactors | NO3 − 88, NH4-N 70, TP 47.5 | 6 | 169.5 mg L−1 (VSS) |
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| Pretreated municipal wastewater |
| continuous culture | TN:99.8 TP 83.1 | 9 | -0.58 g L−1 |
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| Primary settling tank | Mixed indigenous microalgae | Flasks | TN:99.8 TP 97.6 | 25 | 0.62 g L−1 |
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| Secondary settling tank | Mixed indigenous microalgae | Flasks | TN:63.2, TP 70, NH4-N 63.2, COD 64.9TN:67.3 TP 30.8, NH4-N 67.5, COD 70.3TN:80.8, TP 50, NH4-N 71.1, COD 69.3TN 98 TP 25 | 9 | 1.03 g L−1 |
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| Primary effluent | Mixed indigenous microalgae | Photobioreactor | NH4-N 81.16, TP 85.29, COD 62.3 | 4 | 125 mg L−1 d−1 |
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| Secondary effluent |
| Flasks | TN 78.3, TP > 97.7, COD 88.8 | 15 | 1,182.5 mg L−1 |
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| Centrate |
| Flasks | TN 85, TP 66, COD 81 | 10 | 0.29 ± 0.01 g L−1 d−11.23 g L−1 |
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| Dehydration of sludge |
| Batch cultivation | NH4-N 98–100 | 18 | 0.087 g L−1 d−1 |
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| Agricultural wastewater |
| Flasks | NH4-N > 99.99, PO₄ ¯³ > 97 | 14 | 0.0204 g L−1 d−1 |
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| Undiluted cattle farm wastewater |
| Flasks | NH4-N-84, COD >60TN 86, 85% Reactive PO₄−3 85, COD 48 | 7 25 | 0.4403 g L−1 d−1 |
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| Swine wastewater |
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| Digested dairy wastewater |
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| Brackish shrimp aquaculture wastewater |
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| Industrial wastewater | ||||||
| Pulp and paper mill biosludge digestate | ||||||
| Textile wastewater, Palm oil mill effluent |
CO2 fixation using various microalgae species under various cultivation systems.
| Microalgae | Cultivation system | Culture medium | CO2 concentration | CO2 fixation rate (g L−1/d−1) | References |
|---|---|---|---|---|---|
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| Illuminated incubator chamber | ‒ | 15% | 0.097 |
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| Algae consortium | High-rate pond (HRP) | Natural water | ‒ | 0.159 |
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| Glass culture bottles | Palm oil mill effluent (POME) | 10% | 0.829 |
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| Bubble column photobioreactors (BCR) | Domestic wastewater puls poultry waste | Flue gas containing 10% CO2 | 0.261 |
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| Bubble column photobioreactors (BCR) | BG-11 medium | 7% | 0.633 |
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| Open raceway pond | BG-11 medium | 5% | 0.290 |
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| Bubble column PBRs | BG-11 medium | 5%15% | 0.660, 0.710 |
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| Glass culture bottles | BG-11 medium | 20% mixed with N2 | 0.532, 2.177 |
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| Vertical bubble column photo-bioreactor (VBC-PBR) | Modified Mann and Myers medium | 3% mixed with N2 and O2 | 0.240 |
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Microalgae and green algae as the dominant species.