| Literature DB >> 25939034 |
Vandana Vinayak1, Kalina M Manoylov2, Hélène Gateau3, Vincent Blanckaert4, Josiane Hérault5, Gaëlle Pencréac'h6, Justine Marchand7, Richard Gordon8,9, Benoît Schoefs10.
Abstract
The rise of human populations and the growth of cities contribute to the depletion of natural resources, increase their cost, and create potential climatic changes. To overcome difficulties in supplying populations and reducing the resource cost, a search for alternative pharmaceutical, nanotechnology, and energy sources has begun. Among the alternative sources, microalgae are the most promising because they use carbon dioxide (CO2) to produce biomass and/or valuable compounds. Once produced, the biomass is ordinarily harvested and processed (downstream program). Drying, grinding, and extraction steps are destructive to the microalgal biomass that then needs to be renewed. The extraction and purification processes generate organic wastes and require substantial energy inputs. Altogether, it is urgent to develop alternative downstream processes. Among the possibilities, milking invokes the concept that the extraction should not kill the algal cells. Therefore, it does not require growing the algae anew. In this review, we discuss research on milking of diatoms. The main themes are (a) development of alternative methods to extract and harvest high added value compounds; (b) design of photobioreactors; (c) biodiversity and (d) stress physiology, illustrated with original results dealing with oleaginous diatoms.Entities:
Mesh:
Year: 2015 PMID: 25939034 PMCID: PMC4446598 DOI: 10.3390/md13052629
Source DB: PubMed Journal: Mar Drugs ISSN: 1660-3397 Impact factor: 5.118
Main storage compounds and oil percentage of some microalgae.
| Phylum | Class | Taxonomy | Oil Content (% d.w.) | High Value Molecules | Reference |
|---|---|---|---|---|---|
| Chlorophyta | Chlorodendrophyceae | 15–32 | Carotenoids, chlorophyll, tocopherol, lipids | [ | |
| Chlorophyta | Chlorophyceae | 28–40 | Mycosporine-like amino acids, polysaccharides | [ | |
| Chlorophyta | Chlorophyceae | 10 | Carotenoid, β carotene, | [ | |
| Chlorophyta | Chlorophyceae | 36–42 | Carotenoid, β carotene, mycosporine-like amino acids | [ | |
| Chlorophyta | Chlorophyceae | 35–65 | Fatty acids, starch | [ | |
| Chlorophyta | Trebouxiophyceae | 29–75 | Isobotryococcene, botryococcene, triterpenes | [ | |
| Chlorophyta | Trebouxiophyceae | 58 | Neutral lipids | [ | |
| Chlorophyta | Trebouxiophyceae | 34 | Neutral lipids | [ | |
| Chlorophyta | Trebouxiophyceae | 15–55 | Eicosapentaenoic acid (EPA), ascorbic acid | [ | |
| Chlorophyta | Trebouxiophyceae | 57 | C16- and C18-lipids | [ | |
| Heterokontophyta | Bacillariophyceae | 28–69 | EPA | [ | |
| Heterokontophyta | Coscinodiscophyceae | 21–31 | Glycosylglycerides, neutral lipids, TAG | [ | |
| Heterokontophyta | Labrynthulomycetes | 50–77 | Docosahexaenoic acid (DHA) | [ | |
| Myzozoa | Peridinea | 20 | DHA, Starch | [ | |
| Ochrophyta | Coscinodiscophyceae | 42 | Neutral lipids | [ | |
| Ochrophyta | Eustigmatophyceae | 46–68 | EPA, TAG, ω-3 LC-PUFA | [ |
Figure 1Scheme presenting milking as an alternative to current processes. (Top): Current processes are systems that require starting new microalgal cultures for each batch of HVM, with fresh nutrients; (Bottom): Milking only requires inputs of carbon dioxide and water used up in producing HVM, and thus is closer to a closed system.
Extraction processes potentially applicable for milking of microorganisms.
| Milking Process | Microorganism | Advantages | Disadvantages | Ability to Keep Cells Alive |
|---|---|---|---|---|
| Microalgae [ | Improvement of lipid production | Not environmentally friendly | Yes, when using hydrophobic solvents | |
| Yeast [ | High extraction yield | Effect of electric pulsation is size dependent | Yes, but depends on the PEF parameters | |
| Microalgae [ | Not an energy-intensive process | Slow oozing of HVM | Yes, it is a natural mechanism | |
| -sonication | Microalgae [ | Improvement of lipid recovery | Cellular damage apoptosis | No |
| -pressure | Microalgae [this work] | Not an energy-intensive process | Large-scale process not demonstrated Process needs to be improved | Yeswhen using low pressure (< 750 µN) |
| -centrifugation | Diatoms [work in progress] | Continuous process | Requires energy | Not yet tested |
| Bacteria [ | Oozing of HVM | Metabolism engineering | Yes |
Figure 2Diadesmis confervaceae in solitary and chain forms as observed under 100× oil immersion. Note oozed oil droplets in panel C. Cf. [109]. Scale bar: 10 µm.
Figure 3Terpsinoë musica is a freshwater diatom that releases oil under mechanical pressure on the cover slip. Scale bar = 10 µm. (A) Freshly collected Terpsinoë musica; (B,C) Terpsinoë musica cells kept 7 days in an incubator released oil when mechanically pressed; (D) Terpsinoë musica divides 10 days after oil release; (E) Zigzag colony of Terpsinoë musica.
Site locality and identification for sites collection within southeastern USA, temperature (T), pH, percent dissolved oxygen (DO %) and conductivity (µS cm−1), mean ± SE.
| Location | No. | T (°C) | pH | DO % | Conductivity | Latitude | Longitude |
|---|---|---|---|---|---|---|---|
| Lake Sinclair Power Plant | 1 | 23.5 ± 4.2 | 7.0 ± 0.2 | 9 ± 2.52 | 32 ± 3.6 | 33.20 | −83.30 |
| Lake Sinclair, Goat Island | 2 | 21.8 ± 1.3 | 8.5 ± 0.1 | 110 ± 14.1 | 67 ± 6.2 | 33.16 | −83.23 |
| Lake Sinclair at Dam | 3 | 19.9 ± 6.1 | 7.8 ± 0.8 | 69 ± 8.2 | 46 ± 7 | 33.14 | −83.20 |
| Oconee River at Dam | 4 | 23.8±5.1 | 7.1± 2.1 | 61 ± 11.1 | 82.6 ± 1.4 | 33.14 | −83.20 |
| Oconee River Greenway | 5 | 20.2 ± 9 | 7.2 ± 1.6 | 75 ± 2.6 | 78.3 ± 6.9 | 33.08 | −83.21 |
| Fishing Creek | 6 | 22.4 ± 3.2 | 6.3 ± 0.4 | 89 ± 8.2 | 29.2 ± 11.4 | 33.08 | −83.22 |
| Tobler Creek | 7 | 22.1 ± 2.1 | 7.2 ± 0.2 | 45 ± 10.6 | 85 ± 5.3 | 33.12 | −83.27 |
| Andalusia pond | 8 | 23.5 ± 1.8 | 6.8 ± 0.5 | 76 ± 9.6 | 24.3 ± 1.8 | 33.13 | −83.27 |
| Bartram forest pond | 9 | 19.5 ± 3.2 | 7.4 ± 1.3 | 58 ± 12.6 | 78.5 ± 1.6 | 33.02 | −83.21 |
| Savannah River at Port Wentworth, GA | 10 | 25.5 ± 4.4 | 7.6 ± 0.4 | 86 ± 9.7 | 8204 ± 125.4 | 32.17 | −81.16 |
Figure 4Frequency of cells in five diatom cell biovolume categories, for cells that contained lipid droplets. (A) Frequency of cells in 5 diatom cell biovolume categories, for cells that contained lipid droplets; (B) Average biovolume within each cell biovolume category; (C) Oil content within each cell biovolume category.
Cloning of efflux pumps facilitate the excretion of synthesized lipids out from bacteria cells. “Pro/cons” stands for advantages and disadvantages.
| Type of Transporter | Origin | Host Cells | Molecules Transported | Pro/Cons | References |
|---|---|---|---|---|---|
| Resistance-nodulation-cell division (RND) family | Gram-negative bacteria, similarities with cyanobacteria |
| limonene | Pro: increase the excretion of limonene | [ |
| ATP-binding cassette (ABC) | Bacteria |
| carotenoids, squalene, botrycoccene | Pro: present in all 5 kingdoms; import or export molecules and ions across cell membranes | [ |
| Formate transporter (focA) |
|
| formate | [ |