Time required to stabilize thermographic images at rest

Thermography for scientific research and practical purposes requires a series of procedures to obtain images that should be standardized; one of the most important is the time required for acclimatization in the controlled environment. Thus, the objective of this study was to identify the appropriate acclimatization time in rest to reach a thermal balance on young people skin. Forty-four subjects participated in the study, 18 men (22.3 ± 3.1 years) and 26 women (21.7 ± 2.5 years). Thermographic images were collected using a thermal imager (Fluke ®), totaling 44 images over a period of 20 minutes. The skin temperature (TSK) was measured at the point of examination which included the 0 minute, 2, 4, 6, 8, 10, 12, 14, 16, 18 and 20. The body regions of interest (ROI) analyzed included the hands, forearms, arms, thighs, legs, chest and abdomen. We used the Friedman test with post hoc Dunn?s in order to establish the time at rest required to obtain a TSK balance and the Mann-Whitney test was used to compare age, BMI, body fat percentage and temperature variations between men and women, considering always a significance level of pmenor que0.05. Results showed that women had significantly higher temperature variations than men (pmenor que0.01) along the time. In men, only the body region of the abdomen obtained a significant variance (pmenor que0.05) on the analyzed period, both in the anterior and posterior part. In women, the anterior abdomen and thighs, and the posterior part of the hands, forearms and abdomen showed significant differences (pmenor que0.05). Based on our results, it can be concluded that the time in rest condition required reaching a TSK balance in young men and women is variable, but for whole body analysis it is recommended at least 10 minutes for both sexes.

Improved walnut mass micropropagation through the combined use of phloroglucinol and FeEDDHA

Despite the socioeconomic importance of walnut trees, poor rooting and recalcitrance to in vitro culture have hampered the establishment of high-yield clonal plantations. To improve walnut micropropagation, we introduced several modifications to current methods and evaluated the effects on microshoot performance and acclimatization. Nine selected genotypes (13-year-old trees) of the commercial hybrid Juglans major 209 x J. regia were cultured in vitro on DKW-C medium supplemented with 4.4 µM BA and 50 µM IBA. A protocol was developed that relies on the use of 0.40 mM phloroglucinol during shoot multiplication, 0.20 mM previous root induction, and 6.81 mg/L Fe3+ (FeEDDHA). Moreover, the addition of 83.2 µM glucose during the root expression phase significantly improved plant survival during acclimatization. Phloroglucinol promoted microshoot elongation but inhibited rooting, especially at concentrations above 0.40 mM. Replacing FeEDTA by FeEDDHA diminished chlorotic symptoms and improved rooting, with up to 90% microshoots developing viable roots. Likewise, glucose was more efficient than sucrose or fructose in promoting plant survival. At the proposed working concentrations, neither glucose nor FeEDDHA caused any noticeable deleterious effect on walnut micropropagation. Microscopic analysis revealed the physical continuity between adventitious roots and stem pericycles. Analysis of leaf genomic DNA with eight polymorphic microsatellite markers was supportive of the clonal fidelity and genetic stability of the micropropagated material. Successful clonal plantations (over 5,800 ramets) have been established by applying this protocol.

Investigación sobre fermentaciones metánicas de desechos estacionales

En el campo agrícola se producen una serie de desechos orgánicos, que por un lado representan serios problemas de contaminación ambiental y por otro el desperdicio de valores energéticos importantes. Es decir una acción contraria a la sostenibilidad que debe buscarse en este siglo XXI. Entre estos productos agrícolas pueden citarse la pulpa de café, residuos herbáceos, bagazo de caña y la fracción insoluble de estiércol de ganado porcino conocida como cerdaza. Un problema añadido para dar solución adecuada es la disponibilidad de estos solo en cortas épocas del año. Todo lo anterior ha sido el origen de la presente investigación, para dar solución adecuada tanto en el aprovechamiento de biogás como en la reducción de la contaminación. La investigación descrita en este documento contempla el desarrollo de los siguientes aspectos: 1) Caracterización y problemática de cada uno de los productos señalados, 2) la solución al problema mediante el proceso de digestión anaerobia con fases separadas con el aprovechamiento del biogás generados y 3) recomendaciones para el arranque del proceso de digestión anaerobia y su mantenimiento en una alternancia de los productos citados. En la primera etapa de la fase experimental se estimó el rendimiento específico de metano para los diferentes sustratos, utilizando reactores batch configurados en una y dos fases concluyendo que la digestión anaerobia en dos fases presenta diferentes ventajas sobre la digestión monoetapa. En general se obtuvo un mayor rendimiento en la producción de metano, una reducción en los tiempos de retención, mayor eficiencia en la eliminación de los sólidos volátiles agregados, y una mayor estabilidad en el proceso reflejado en el mantenimiento de valores de pH en los rangos de operación recomendados. Seguidamente, al comparar dos procesos para la puesta en marcha de digestores metanogénicos operados en forma continua, se concluye que las variables determinantes en la estabilidad del sistema son la alcalinidad total presente en el digestor, el establecimiento de la población de microorganismos y la carga orgánica aplicada. Las dos primeras están determinadas por la calidad y proporción del inóculo suministrado al inicio del proceso. La alternación de sustratos suministrados al sistema de digestión en dos fases, permitió determinar el impacto sobre el desempeño del mismo, registrando una reducción en la producción de biogás, la riqueza de metano y la eficiencia de eliminación de sólidos volátiles durante los primeros días de operación luego del cambio de sustrato. Este periodo corresponde al proceso de aclimatación de los microorganismos el cual requirió de 20 días para asimilar los componentes del nuevo sustrato. Finalmente, entre los sustratos analizados, la menor carga orgánica de operación para mantener la operación del sistema en continuo corresponde a la pulpa de café con 0.1 kg SV/m3. La composición de este sustrato favorece la rápida acumulación de acidez volátil en el sistema, proporcionando una tendencia a la acidificación. Sin embargo, al controlar las cargas orgánicas volumétricas, el sistema permaneció operando sin necesidad de adición de alcalinizantes. La aplicación de los resultados de la presente investigación a la problemática de residuos de café es alentadora, comprobando que el sistema puede ser operado en continuo alternando residuos boreales y pulpa de café, ambos sustratos disponibles en las plantas de procesamiento de la cereza de café. ABSTRACT In the agricultural field there are series of organic wastes, which in one hand are the source of serious problems of environmental pollution and in the other, they represent a residue that could be used as a feedstock with significant energy values. These actions are contrary to efforts towards sustainability, which should be a priority in this century. Among agricultural residues with significant abundance, the coffee pulp, herbaceous waste, sugarcane bagasse and the insoluble fraction of pig manure can be mentioned. An added problem to the development of appropriate treatment systems, which provides a solution to the disposal of such wastes, is the limited availability of these feedstocks only in short seasons. These arguments have been the source of our research, in order to provide properly measures to biogas usage and pollution reduction. The research presented in this document includes the approaches to the following aspects. 1) Characterization and problems regarding the selected feedstocks 2) the solution to the problem by anaerobic digestion process with separate phases and 3) recommendations for starting the process of anaerobic digestion and its maintenance with alternation of the products listed For the first stage of the experimental phase, the specific methane yield of the selected feedstocks was estimated using batch reactors configured in one and two phases. It was concluded that two-phase anaerobic digestion offered distinct advantages over the single-stage digestion. In general a higher methane production yields, lower retention times, higher efficiency in volatile solids removal, and increased stability among the process were obtained. When comparing two processes for starting up methanogenic digesters, it is concluded that the variables that determine the stability of the system are the total alkalinity in the digester, the establishment of the population of microorganisms and the organic load. The first variables are influenced by the proportion and quality of the inoculum supplied at the beginning of the process. The alternation of substrates gave as a result a negative impact on system performance, recording a reduction on biogas production, the methane concentration and the efficiency of volatile solids removal. The situation was observed during the first days of operation after the change of feeding. This period corresponds to the process of acclimatization of the microorganisms which required 20 days to assimilate new substrate components. Finally, among substrates studied, the lowest organic load applied to maintain a continuous operation of the system, corresponds to the coffee pulp with 0.1 kg VS / m3. The composition of this substrate promotes a rapid accumulation of volatile acidity within the system, providing a tendency to acidification. However, by controlling organic loads, the operating system remained stable without addition of alkalizing components. The application of the results of this research to the problem of coffee waste is promising, proving that an anaerobic system can be operated continuously by alternating boreal waste and coffee pulp, both substrates available in coffee processing plants.