Marcos A. Coronado

Dr. Marcos A. Coronado

Universidad Autónoma de Baja California
orcid

Research Focus & Metrics

Academic Career Length

16Years (2011-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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3 March 2021 in Molecules
Verified
Journal Article
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JAJosé Ramón Ayala
José Ramón Ayala
GMGisela Montero
Gisela Montero
MCMarcos A. Coronado
Marcos A. Coronado
Conrado García-GonzálezConrado García-González
Conrado García-González
MCMario Curiel-Alvarez
Mario Curiel-Alvarez
DMDaniela G. Montes
Daniela G. Montes
Annually, millions of tons of foods are generated with the purpose to feed the growing world population. One particular eatable is orange, the production of which in 2018 was 75.54 Mt. One way to valorize the orange residue is to produce bioethanol by fermenting the reducing sugars generated from orange peel. Hence, the objective of the present work was to determine the experimental conditions to obtain the maximum yield of reducing sugars from orange peel using a diluted acid hydrolysis process. A proximate and chemical analysis of the orange peel were conducted. For the hydrolysis, two factorial designs were prepared to measure the glucose and fructose concentration with the 3,5-DNS acid method and UV-Visible spectroscopy. The factors were acid concentration, temperature and hydrolysis time. After the hydrolysis, the orange peel samples were subjected to an elemental SEM-EDS analysis. The results for the orange peel were 73.530% of moisture, 99.261% of volatiles, 0.052% of ash, 0.687% of fixed carbon, 19.801% of lignin, 69.096% of cellulose and 9.015% of hemicellulose. The highest concentration of glucose and fructose were 24.585 and 9.709 g/L, respectively. The results highlight that sugar production is increased by decreasing the acid concentration.

1 August 2016 in Energy
Verified
Journal Article
Closed access
GMGisela Montero
Gisela Montero
MCMarcos A. Coronado
Marcos A. Coronado
RTRicardo Torres
Ricardo Torres
BJBeatriz E. Jaramillo
Beatriz E. Jaramillo
Conrado García-GonzálezConrado García-González
Conrado García-González
EVEdgar Valenzuela
Edgar Valenzuela

1 April 2014 in Energy
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Journal Article
Closed access
MCMarcos A. Coronado
Marcos A. Coronado
GMGisela Montero
Gisela Montero
BVBENJAMIN VALDEZ
BENJAMIN VALDEZ
MSMargarita Stoytcheva
Margarita Stoytcheva
AEAmir Eliezer
Amir Eliezer
Armando PerezArmando Perez
Armando Perez

4 July 2017 in Journal of Essential Oil Bearing Plants
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Journal Article
Closed access
JAJosé Ramón Ayala
José Ramón Ayala
GMGisela Montero
Gisela Montero
HCHéctor E. Campbell
Héctor E. Campbell
Conrado García-GonzálezConrado García-González
Conrado García-González
MCMarcos A. Coronado
Marcos A. Coronado
LPLaura J. Pérez
Laura J. Pérez
The food industry is growing significantly every year. Annually, large quantities of fruits and vegetables are grown to meet the population demand. Among them, the orange (Citrus sinensis) production was 70.45 Mt in 2013. After consumption, the remaining orange peel is considered as a waste. From an economic and environmental perspective, the extraction of orange essential oil is a high value-added option for the valorization and use of the orange peel. Therefore, the objective of this study was to determine the experimental conditions where the maximum yield of essential oil of orange peel is obtained by applying a factorial design. The most relevant extraction process factors studied were the grinding time and the operating time. The characterization of the essential oil included FT-IR, GC-FID, high heating value determination and TG analysis. For the processed orange peel, the high heating value was measured, and the SEM-EDS analyses were performed. The maximum experimental yield was achieved with 500 cm3 of solvent, 50 min of extraction time and 2 min of grinding time. The results obtained at these conditions were: a yield of essential oil of 5.23% v/w, with a concentration of 74.43% of limonene, 4.27% of p-myrcene, 3.26% of sabinene, 1.54% of β-pinene, and 1.54 % of linalool. The high heating value of essential oil was 44.25 MJ/kg, and for orange peel was 15.82 MJ/kg. The orange peel elemental composition analysis showed 24.1% oxygen and 73.51% carbon.

18 September 2020 in Sustainability
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Journal Article
Open access
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MCMarcos A. Coronado
Marcos A. Coronado
GMGisela Montero
Gisela Montero
DMDaniela G. Montes
Daniela G. Montes
BVBENJAMIN VALDEZ
BENJAMIN VALDEZ
JAJosé Ramón Ayala
José Ramón Ayala
AMAbigail Moreno
Abigail Moreno
The brewing industry generates, as the primary coproduct, brewers’ spent grain (BSG). In Mexicali, Baja California, Mexico, there are 17 companies that generated 282 tons of BSG by 2016. Cattle feeding is the most common type of disposal for this waste. However, it can be valorized for the production of bioenergy or as a source of added-value products. Therefore, the objective of the present work was to assess the physicochemical properties of the brewers’ spent grain from a local craft brewery, to choose the most appropriate exploitation route. Chemical and morphological analyses were carried out by energy dispersive X-ray fluorescence spectroscopy (EDX), scanning electron microscopy, and the higher heating value determination. The results of the proximate analyses were 72.32% moisture, 78.47% volatile matter, 17.48% fixed carbon, and 4.05% ash. The results of the chemical analysis for extractables were 5.23% using organic solvent and 50.25% using hot water. The content determination were 17.13% lignin, 26.80% cellulose, and 37.17% hemicellulose. The results of the ultimate analysis were 43.59% C, 6.18% H, 3.46% N, and 37.22% O. The higher heating value experimentally obtained was 18.70 MJ/kg. Moreover, in the EDX analysis, Ca, P, K, and S were mainly found. It is recommendable to valorize the BSG through the xylitol, bioethanol or biogas production, because of its high moisture, hemicellulose and cellulose content.

22 September 2016 in Waste and Biomass Valorization
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Journal Article
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Conrado García-GonzálezConrado García-González
Conrado García-González
GMGisela Montero
Gisela Montero
MCMarcos A. Coronado
Marcos A. Coronado
BVBENJAMIN VALDEZ
BENJAMIN VALDEZ
MSMargarita Stoytcheva
Margarita Stoytcheva
CSCarlos Alfonso Sagaste
Carlos Alfonso Sagaste