Estudio de gestión de la finca La Esperanza, municipio de Pueblo Nuevo, Nicaragua

El presente proyecto tiene como finalidad el análisis de la Finca la Esperanza, en la localidad de Pueblo Nuevo, en la República de Nicaragua. En dicho análisis se estudian parámetros edáficos, calidad de agua y económicos, con el objetivo de poder plantear una propuesta de mejora en los rendimientos de la finca tanto a nivel económico como ambiental. La iniciativa de realizar este estudio surge de las necesidades del propio agricultor, que plantea el desarrollo rural sobre la base de actividades respetuosas con el medio. Las estrategias a los problemas sociales originados por la producción agraria industrial, como el éxodo rural, la pérdida de la agricultura convencional, la nueva función de los espacios agrarios de la sociedad, etc., se formalizaron en el denominado Desarrollo Sostenible. A nivel de finca cualquier concepción de sustentabilidad necesita que el agrosistema sea considerado como un ecosistema, en el que la investigación y la producción busquen no solamente altos rendimientos sino la optimización del sistema como un todo. Tal propósito requiere armonizar una viabilidad económica con otras variables, como estabilidad ecológica y equidad social. Para ello, los principios básicos de un sistema sostenible son: la conservación de los recursos renovables, la adaptación del cultivo al ambiente y el mantenimiento de un moderado pero sostenible nivel de producción. Como resultado de los análisis y observaciones hechas a lo largo de la estancia en la finca, se propone un plan de actuación de 10 años de duración en los cuales se procura alcanzar no únicamente unas cuotas máximas de rendimiento sino también la supervivencia de los recursos, base de la familia Videa Vanegas, propietarios.

Versatile methodology to hydrate alkynes, in the presence of a wide variety of functional groups, with Mercury(II) p-Toluensulfonamidate, under catalytic, mild and neutral conditions

A method to generate carbonylic compounds from alkynes under mild and neutral conditions, with excellent functional group compatibility and high yields, is described. Hydration takes place under catalytic conditions by using from 0.1 to 0.2 equivalents of the easily available and inexpensive mercury(II) p-toluensulfonamidate in a hydroalcoholic solution. After use the catalyst is iner tized and/or recycled ...

Catalytic gasification of glycerol in supercritical water

The conversion of glycerol in supercritical water (SCW) was studied at 510-550 °C and a pressure of 350 bars using both a bed of inert and non-porous ZrO2 particles (hydrothermal experiments), and a bed of a 1% Ru/ZrO2 catalyst. Experiments were conducted with a glycerol concentration of 5 wt% in a continuous isothermal fixed-bed reactor at a residence time between 2 and 10 s. Hydrothermolysis of glycerol formed water-soluble products such as acetaldehyde, acetic acid, hydroxyacetone and acrolein, and gases like H2, CO and CO2. The catalyst enhanced the formation of acetic acid, inhibited the formation of acrolein, and promoted gasification of the glycerol decomposition products. Hydrogen and carbon oxides were the main gases produced in the catalytic experiments, with minor amounts of methane and ethylene. Complete glycerol conversion was achieved at a residence time of 8.5 s at 510 °C, and at around 5 s at 550 °C with the 1 wt% Ru/ZrO2 catalyst. The catalyst was not active enough to achieve complete gasification since high yields of primary products like acetic acid and acetaldehyde were still present. Carbon balances were between 80 and 60% in the catalytic experiments, decreasing continuously as the residence time was increased. This was attributed partially to the formation of methanol and acetaldehyde, which were not recovered and analyzed efficiently in our set-up, but also to the formation of carbon deposits. Carbon deposition was not observed on the catalyst particles but on the surface of the inert zirconia particles, especially at high residence time. This was related to the higher concentration of acetic acid and other acidic species in the catalytic experiments, which may polymerize to form tar-like carbon precursors. Because of carbon deposition, hydrogen yields were significantly lower than expected; for instance at 550 °C the hydrogen yield potential was only 50% of the stoichiometric value.

Low environmental impact bleaching sequences for attaining high brightness level with eucalyptus SPP pulp

The alternatives used for minimizing the usage of chlorine dioxide in bleaching sequences included a hot acid hydrolysis (Ahot) stage, the use of hot chlorine dioxide (Dhot) and ozone stages at medium consistency and high consistency (Zmc and Zhc), in addition to stages with atmospheric hydrogen peroxide (P) and pressurized hydrogen peroxide (PO). The results were interpreted based on the cost of the chemical products, bleaching process yields and on minimizing the environmental impact of the bleaching process. In spite of some process restrictions, high ISO brightness levels were kept around 90 % brightness. Additionally, the inclusion of stages like acid hydrolysis, pressurized peroxide and ozone in the bleaching sequences provided an increase in operating flexibility, aimed at reducing environmental impact (ECF Light). The Dhot(EOP)D(PO) sequence presented lower operating cost for ISO brightness above 92 %. However, this kind of sequence was not allowed for closing the wastewater circuit, even partially. For ISO brightness level around 91%, the AhotZhcDP sequence presented a lower operating cost than the others