Nutritional impact on health and performance in intensively reared rabbits

The present work summarizes research related to the definition of nutrient recommendations for feeds used in the intensive production of rabbit's meat. Fibre is the main chemical constituent of rabbit diets that typically contain 320 to 360 and 50 to 90 g/kg of insoluble and soluble fibre, respectively. Instead, the dietary contents of cereal grains (∼120 to 160 g/kg), fat (15 to 25 g/kg) and protein concentrates (150 to 180 g/kg) are usually low with respect to other intensively reared monogastric animals. Cell wall constituents are not well digested in rabbits, but this effect is compensated by its stimulus of gut motility, which leads to an increasing rate of passage of digesta, and allows achieving an elevated dry matter intake. A high feed consumption and an adequate balance in essential nutrients are required to sustain the elevated needs of high-productive rabbits measured either as reproductive yield, milk production or growth rate in the fattening period. Around weaning, pathologies occur in a context of incomplete development of the digestive physiology of young rabbits. The supply of balanced diets has also been related to the prevention of disorders by means of three mechanisms: (i) promoting a lower retention time of the digesta in the digestive tract through feeding fibre sources with optimal chemical and physical characteristics, (ii) restricting feed intake after weaning or (iii) causing a lower flow of easily available substrates into the fermentative area by modifying feed composition (e.g. by lowering protein and starch contents, increasing its digestibility or partially substituting insoluble with soluble fibre), or by delaying age at weaning. The alteration in the gut microbiota composition has been postulated as the possible primary cause of these pathologies.

Morphological and germination response variability in seeds of wild yellow gentian (Gentiana lutea L.) accessions from northwest Spain

Gentiana lutea L. (yellow gentian, Gentianaceae) is an important medicinal plant under protection as endangered species in most European countries. The aim of this work was to evaluate variation in seed mass, seed water content, and seed germination among 56 wild accessions of G. lutea. The effect of gibberellic acid (GA3), putrescine, moist chilling, and level of ripeness of seeds on subsequent germination was also investigated. Seeds of G. lutea showed physiological dormancy (final germination percentages ranged from 0% to 11%, depending on the accession) and GA3 enhanced seed germination drastically in all the accessions. The highest germination (99%) of GA3-treated seeds was reached at 15 °C. Final germination percentage and germination rate (as expressed by mean germination time), as well as seed mass and seed water content, varied significantly among accessions. In general, 1 year moist chilling did not significantly enhance G. lutea seed germination. For most accessions, no significant differences were found between fully ripe seeds and less ripe seeds for seed water content, seed mass, and seed germination. Applications of GA3 were always most effective than those of putrescine for increasing seed germination.

Spatial variability of seed depth placement of maize under no tillage.

Among the various factors that contribute towards producing a successful maize crop, seed depth placement is a key determinant, especially in a no-tillage system. The main objective of this work was to evaluate the spatial variability of seed depth placement and crop establishment in a maize crop under no-tillage conditions, using precision farming technologies. The obtained results indicate that seed depth placement was significantly affected by soil moisture content, while a very high coefficient of variation of 39% was found for seed depth. Seeding depth had a significant impact on mean emergence time and percentage of emerged plants. Shallow average depth values and the high coefficient of variation suggest a need for improvement in controlling the seeder sowing depth.

A partial study of vertical distribution of conventional no-till seeders and spatial variability of seed depth placement of maize in the Alentejo region, Portugal

The requirements for a good stand in a no-till field are the same as those for conventional planting as well as added field and machinery management. Among the various factors that contribute towards producing a successful maize crop, seed depth placement is a key determinant. Although most no-till planters on the market work well under good soil and residue conditions, adjustments and even modifications are frequently needed when working with compacted or wet soils or with heavy residues. The main objective of this study, carried out in 2010, 2011 and 2012, was to evaluate the vertical distribution and spatial variability of seed depth placement in a maize crop under no-till conditions, using precision farming technologies and conventional no-till seeders. The results obtained indicate that the seed depth placement was affected by soil moisture content and forward speed. The seed depth placement was negatively correlated with soil resistance and seeding depth had a significant impact on mean emergence time and the percentage of emerged plants. Shallow average depth values and high coefficients of variation suggest a need for improvements in controlling the seeders’ sowing depth mechanism or more accurate calibration by operators in the field.

Spatial variability of seed depth placement of maize under no tillage in Alentejo, Portugal

Among the various factors that contribute towards producing a successful maize crop, seed depth placement is a key determinant, especially in a no-tillage system. The main objective of this work was to evaluate the spatial variability of seed depth placement and crop establishment in a maize crop under no-tillage conditions, using precision farming technologies. The obtained results indicate that seed depth placement was significantly affected by soil moisture content, while a very high coefficient of variation of 39% was found for seed depth. Seeding depth had a significant impact on mean emergence time and percentage of emerged plants. Shallow average depth values and the high coefficient of variation suggest a need for improvement in controlling the seeders sowing depth.

Optimización de la agitación de un digestor anaerobio mediante mecánica de fluidos computacional

Debido al gran interés existente en el ahorro y recuperación de energía, y en el deseo de obtener productos que permitan usos beneficiosos del fango procedente de la depuración del agua residual, la digestión anaerobia es el proceso de estabilización de uso más extendido. El tiempo de retención de sólidos es un factor clave en el proceso de digestión anaerobia. En base al tiempo de retención de sólidos, se dimensiona el volumen de los digestores anaerobios para así obtener la reducción de materia orgánica deseada, con la correspondiente producción de biogás. La geometría del digestor y su sistema de agitación deben ser adecuados para alcanzar el tiempo de retención de sólidos de diseño. Los primeros trabajos sobre la agitación de los digestores realizaban únicamente experimentos con trazadores y otros métodos de medición. En otros casos, la mezcla era evaluada mediante la producción de biogás. Estas técnicas tenían el gran hándicap de no conocer lo que sucedía realmente dentro del digestor y sólo daban una idea aproximada de su funcionamiento. Mediante aplicación de la mecánica de fluidos computacional (CFD) es posible conocer con detalle las características del fluido objeto de estudio y, por lo tanto, simular perfectamente el movimiento del fango de un digestor anaerobio. En esta tesis se han simulado mediante CFD diferentes digestores a escala real (unos 2000 m3 de volumen) agitados con bomba/s de recirculación para alcanzar los siguientes objetivos: establecer la influencia de la relación entre el diámetro y la altura, de la pendiente de la solera, del número de bombas y del caudal de recirculación en dichos digestores, definir el campo de velocidades en la masa de fango y realizar un análisis energético y económico. Así, es posible conocer mejor cómo funciona el sistema de agitación de un digestor anaerobio a escala real equipado con bomba/s de recirculación. Los resultados obtenidos muestran que una relación diámetro/altura del digestor por encima de 1 empeora la agitación del mismo y que la pendiente en la solera del digestor favorece que la masa de fango esté mejor mezclada, siendo más determinante la esbeltez del tanque que la pendiente de su solera. No obstante, también es necesario elegir adecuadamente los parámetros de diseño del sistema de agitación, en este caso el caudal de recirculación de fango, para obtener una agitación completa sin apenas zonas muertas. En el caso de un digestor con una geometría inadecuada es posible mejorar su agitación aumentando el número de bombas de recirculación y el caudal de las mismas, pero no se llegará a alcanzar una agitación total de la masa de fango debido a su mal diseño original. Anaerobic digestion is the process for waste water treatment sludge stabilization of more widespread use due to the huge interest in saving and recovering energy and the wish to obtain products that allow beneficial uses for the sludge. The solids retention time is a key factor in the anaerobic digestion. Based on the solids retention time, volume anaerobic digester is sized to obtain the desired reduction in organic matter, with the corresponding production of biogas. The geometry of the digester and the stirring system should be adequate to achieve the design solid retention time. Early works on digesters stirring just performed tracer experiments and other measurement methods. In other cases, mixing was evaluated by biogas production. These techniques had the great handicap of not knowing what really happened inside the digester and they only gave a rough idea of its operation. By application of computational fluid dynamics (CFD), it is possible to know in detail the characteristics of the fluid under study and, therefore, simulate perfectly the sludge movement of an anaerobic digester. Different full-scale digesters (about 2000 m3 of volume) agitated with pump/s recirculation have been simulated by CFD in this thesis to achieve the following objectives: to establish the influence of the relationship between the diameter and height, the slope of the bottom, the number of pumps and the recirculation flow in such digesters, to define the velocity field in the mass of sludge and carry out an energy and economic analysis. Thus, it is possible to understand better how the agitation system of a full-scale anaerobic digester equipped with pump/s recirculation works. The results achieved show that a diameter/height ratio of the digester above 1 worsens its stirring and that the slope of the digester bottom favors that the mass of sludge is better mixed, being more decisive the tank slenderness than the slope of its bottom. However, it is also necessary to select properly the design parameters of the agitation system, in this case the sludge recirculation flow rate, for a complete agitation with little dead zones. In the case of a digester with inadequate geometry, its agitation can be improved by increasing the number of recirculation pumps and flow of them, but it will not reach a full agitation of the mass of sludge because of the poor original design.

First passages in bounded domains: When is the mean first passage time meaningful?

We study the first passage statistics to adsorbing boundaries of a Brownian motion in bounded two-dimensional domains of different shapes and configurations of the adsorbing and reflecting boundaries. From extensive numerical analysis we obtain the probability P(ω) distribution of the random variable ω=τ1/(τ1+τ2), which is a measure for how similar the first passage times τ1 and τ2 are of two independent realizations of a Brownian walk starting at the same location. We construct a chart for each domain, determining whether P(ω) represents a unimodal, bell-shaped form, or a bimodal, M-shaped behavior. While in the former case the mean first passage time (MFPT) is a valid characteristic of the first passage behavior, in the latter case it is an insufficient measure for the process. Strikingly we find a distinct turnover between the two modes of P(ω), characteristic for the domain shape and the respective location of absorbing and reflective boundaries. Our results demonstrate that large fluctuations of the first passage times may occur frequently in two-dimensional domains, rendering quite vague the general use of the MFPT as a robust measure of the actual behavior even in bounded domains, in which all moments of the first passage distribution exist.