Publicaciones Portero Barahona Patricia
Production, Extraction And Characterization Of Lipases From The Antarctic Yeast Guehomyces Pullulans
REVISTA
AMERICAN JOURNAL OF BIOCHEMISTRY AND BIOTECHNOLOGY
Publicación
2019-04-11
The production of extracellular lipases from the Antarctic yeast Guehomyces pullulans is induced using an olive oil medium as an inductor substrate and a first characterization of its enzyme, using the protein extract obtained from the medium, is described. For this, the effect of pH and temperature on the lipase activity are evaluated and the enzyme kinetic for the lipase is determined. Lipase production was 0.27 U/mL, a high value compared to lipolytic activities in non-optimized media. However, this value can be increased by optimizing the culture medium. The lipase of G. pullulans has maximum activity at pH 8.0 and 40°C (thermal stability 40- 50°C). Regarding the kinetic parameters, a KM = 3.7×10−4 M was obtained, a value located in the range of industrial lipases. In addition, its kinetics presented the phenomenon of interfacial activation. The results presented in this work show the biotechnological potential of the lipase due its biochemical properties and are useful for later work directed to study other factors that affect the enzyme activity and potential biotechnological applications of the Guehomyces pullulans lipase.
Sugarcane Bagasse Hydrolysis Enhancement By Microwave-Assisted Sulfolane Pretreatment
REVISTA
ENERGIES
Publicación
2019-05-06
Sugarcane bagasse is the major by-product of the sugarcane industry and, due to its abundant availability, it has been extensively studied for lignocellulosic bioconversion in the production of bioethanol and other value-added commercial products. In the study presented herein, a combined pretreatment using sulfolane, TiO2 and alkali microwave irradiation (MW-A) was assessed for the dissolution of lignin prior to enzymatic saccharification of holocellulose. Total reducing sugars (TRS) and saccharine acid yields were investigated. The increase in NaOH concentration up to 5% and in temperature from 120 ◦C to 140 ◦C were found to have a positive influence on both yields. While increasing the reaction time from 5 to 60 min only led to an increase in TRS yield
Assessment Of The Effect Of Nitrogen Concentration On Fermentation And Selection Of A Highly Competitive Saccharomyces Cerevisiae Strain For Efficient Ethanol Production
REVISTA
ENERGIES
Publicación
2019-07-07
The optimum nitrogen concentration for media supplementation and strain dominance are aspects of key importance to the industrial production of ethanol with a view to reducing costs and increasing yields. In this work, these two factors were investigated for four ethanologenic Saccharomyces cerevisiae strains (CLQCA-INT-001, CLQCA-INT-005, CLQCA-10-099, and UCLM 325), selected from the screening of 150 isolates, mostly from Ecuadorian yeast biodiversity. The effect of nitrogen concentration was assessed in terms of cellular growth, glucose consumption and ethanol production, and the yeast strains’ dominance was evaluated in continuous co-fermentation with cellular recycling by mitochondrial DNA analyses. Among the four selected yeast strains under study, CLQCA-INT-005 presented the highest glucose consumption at a nitrogen supplement concentration as low as 0.4 g·L−1, attaining an ethanol yield of up to 96.72% in 24 h. The same yeast strain was found to be highly competitive, showing a dominance of 80% after four cycles of fermentation in co-culture. Thus, CLQCA-INT-005 may be deemed as a very promising candidate to be used both at pilot-plant scale and at industrial scale cellulosic ethanol production.
Ecuadorian Yeast Species As Microbial Particles For Cr(Vi) Biosorption
REVISTA
ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH
Publicación
2019-09-01
Pollution caused by heavy metals is a prime concern due to its impact on human health, animals, and ecosystems. Cr(VI), generated in a range of different industries as a liquid effluent, is one of the most frequent contaminants. In the work presented herein, the adsorption efficiency of three species of native yeasts from Ecuador (Kazachstania yasuniensis, Kodamaea transpacifica, and Saturnispora quitensis) for Cr(VI) removal from simulated wastewater was assessed, taking Saccharomyces cerevisiae as a reference. After disruption of the flocs of yeast with a cationic surfactant, adsorption capacity, kinetics, and biosorption isotherms were studied. K. transpacifica isolate was found to feature the highest efficiency among the four yeasts tested, as a result of its advantageous combination of surface charge, individual cell size (4.04 μm), and surface area (1588.27 m2 /L). The performance of S. quitensis was only slightly lower. The remarkable biosorption capacities of these two isolates (476.19 and 416.67 mg of Cr(VI)/g of yeast, respectively) evidence the potential of non-conventional yeast species as sorption microbial particles for polluted water remediation.
Cellulosic Ethanol: Improving Cost Efficiency By Coupling Semi-Continuous Fermentation And Simultaneous Saccharification Strategies
REVISTA
PROCESSES
Publicación
2020-11-15
A novel approach to improve ethanol production from sugarcane bagasse is proposed. Biomass was pretreated with sodium hydroxide, sulfuric, oxalic, and maleic acids (1% w/v) at different temperatures (130–170 ◦C) and times (10–30 min). The pretreatment with NaOH at 160 ◦C for 20 min was found to be the most efficient for further enzymatic saccharification. A semi-continuous fermentation system coupled with a simultaneous saccharification and fermentation strategy was used, attaining fermented liquor every 24 h. The amount of enzymes needed for saccharification was optimized, as well as the production time and ethanol concentration. The process occurred with near to complete depletion of glucose, obtaining ethanol concentrations ranging from 8.36 to 10.79% (v/v). The whole system, at bench scale, showed stability over 30 days, and ease of management and control. This strategy may improve cost efficiency in the production of cellulosic ethanol at industrial scale