| Literature DB >> 24443802 |
Luis Carlos Mata-Gómez, Julio César Montañez1, Alejandro Méndez-Zavala, Cristóbal Noé Aguilar.
Abstract
Nowadays, carotenoids are valuable molecules in different industries such as chemical, pharmaceutical, poultry, food and cosmetics. These pigments not only can act as vitamin A precursors, but also they have coloring and antioxidant properties, which have attracted the attention of the industries and researchers. The carotenoid production through chemical synthesis or extraction from plants is limited by low yields that results in high production costs. This leads to research of microbial production of carotenoids, as an alternative that has shown better yields than other aforementioned. In addition, the microbial production of carotenoids could be a better option about costs, looking for alternatives like the use of low-cost substrates as agro-industrials wastes. Yeasts have demonstrated to be carotenoid producer showing an important growing capacity in several agro-industrial wastes producing high levels of carotenoids. Agro-industrial wastes provide carbon and nitrogen source necessary, and others elements to carry out the microbial metabolism diminishing the production costs and avoiding pollution from these agro-industrial wastes to the environmental. Herein, we discuss the general and applied concepts regarding yeasts carotenoid production and the factors influencing carotenogenesis using agro-industrial wastes as low-cost substrates.Entities:
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Year: 2014 PMID: 24443802 PMCID: PMC3922794 DOI: 10.1186/1475-2859-13-12
Source DB: PubMed Journal: Microb Cell Fact ISSN: 1475-2859 Impact factor: 5.328
Figure 1Molecules of carotenes: a) β -carotene, b) Torulene; xanthophylls: c) Astaxanthin, d) Canthaxanthin.
Recent researches of use of agro-industrial wastes as substrates to yeasts carotenoid production
| Whey | 46 mg L-1 of β -carotene | ||
| Potato medium | 56 mg L-1 of β -carotene | ||
| Crude glycerol | 135.2 mg L-1 of carotenoids | ||
| Chicken feathers | 92 mg L-1 of carotenoids | ||
| Whey ultrafiltrate | 262 mg L-1 β -carotene | ||
| Whey | 590.4 μg L-1 of carotenoids | ||
| Fermented radish brine | 19 μg L-1 h-1 of β -carotene | ||
| Fermented radish brine | 201 μg L-1 of β -carotene | ||
| Mung bean waste flour and sweet potato extract | 3.48 mg L-1 of carotenoids | ||
| Ultrafiltrate whey | 10.2 mg L-1 of carotenoids |
Bioreactors employed to carotenoid production with yeasts
| 3 L stirred tank | 201 μg L-1 (24 h) | ||
| 3.7 L stirred tank | 710 μg L-1 | ||
| 5 L stirred tank | 266.1 μg g-1 of biomass | ||
| 3 L stirred tank | 8798.6 μg g-1 of biomass |
Figure 2General scheme of biotechnological processes for carotenoids production.
Extraction of carotenoids using different techniques of cell disruption
| Freezing and maceration with diatomaceous earth | 93.13 μg g-1 of biomass | ||
| Freezing and DMSO | 155.72 μg g-1 of biomass | ||
| Enzymatic lysis and ultrasonic waves | 163.12 μg g-1 of biomass | ||
| Bead grinder | 125 mg L-1 of medium | ||
| Freeze-dried | 266.1 μg g-1 of biomass | ||
| Freezing in liquid N2 and maceration | 590.4 μg L-1 of medium | ||
| DMSO, acetone and petroleum ether | 92 mg L-1 of medium | ||
| HCl and acetone | 4790 μg g-1 of biomass | ||
| DMSO, acetone and petroleum ether | 803.2 μg g-1 of biomass |
Current patents of microbial carotenoid production
| Carotenoid production in oleaginous yeasts and molds | MX | 2012 | |
| Biological production of Zeaxanthin and carotenoid biosynthesis control | US | 2013 | |
| Efficient astaxanthin production strains derived from | US | 2013 | |
| Novel strain of | GRM | 2010 | |
| Method for preparing and extracting carotenoid from microbial thalli | US | 2012 | |
| Fermentation process to produce natural carotenoids and carotenoid-enriched feed products. | US | 2012 | |
| Production of carotenoid in oleaginous yeast and fungi | US | 2010 |