Levantamento de coeficientes de desempenho de refrigeradores domésticos associados a armazenador térmico

Pós-graduação em Engenharia Mecânica - FEB

Projeto de um tanque de armazenamento atmosférico com teto flutuante para estocagem de gasolina

In this paper are discussed the main project stages of an atmospheric storage tank with floating roof. It emphasizes the calculations of the bottom, the shell and the floating roof, discussing its stages and conditions, based on the technical standards of the project. The storage tanks are static equipment working under low pressure and has an essential importance for the operation of a process plant. This paper has the purpose of obtaining the dimensions and materials of each component of the tank through the calculations and prove them with results obtained by numerical simulation by finite elements with the help of Autodesk Inventor software, consolidating the project

Projeto de um tanque de armazenamento atmosférico com teto flutuante para estocagem de gasolina

In this paper are discussed the main project stages of an atmospheric storage tank with floating roof. It emphasizes the calculations of the bottom, the shell and the floating roof, discussing its stages and conditions, based on the technical standards of the project. The storage tanks are static equipment working under low pressure and has an essential importance for the operation of a process plant. This paper has the purpose of obtaining the dimensions and materials of each component of the tank through the calculations and prove them with results obtained by numerical simulation by finite elements with the help of Autodesk Inventor software, consolidating the project

Chemical resistance of the gram-negative bacteria to different sanitizers in a water purification system

Abstract Background Purified water for pharmaceutical purposes must be free of microbial contamination and pyrogens. Even with the additional sanitary and disinfecting treatments applied to the system (sequential operational stages), Pseudomonas aeruginosa, Pseudomonas fluorescens, Pseudomonas alcaligenes, Pseudomonas picketti, Flavobacterium aureum, Acinetobacter lowffi and Pseudomonas diminuta were isolated and identified from a thirteen-stage purification system. To evaluate the efficacy of the chemical agents used in the disinfecting process along with those used to adjust chemical characteristics of the system, over the identified bacteria, the kinetic parameter of killing time (D-value) necessary to inactivate 90% of the initial bioburden (decimal reduction time) was experimentally determined. Methods Pseudomonas aeruginosa, Pseudomonas fluorescens, Pseudomonas alcaligenes, Pseudomonas picketti, Flavobacterium aureum, Acinetobacter lowffi and Pseudomonas diminuta were called in house (wild) bacteria. Pseudomonas diminuta ATCC 11568, Pseudomonas alcaligenes INCQS , Pseudomonas aeruginosa ATCC 15442, Pseudomonas fluorescens ATCC 3178, Pseudomonas picketti ATCC 5031, Bacillus subtilis ATCC 937 and Escherichia coli ATCC 25922 were used as 'standard' bacteria to evaluate resistance at 25°C against either 0.5% citric acid, 0.5% hydrochloric acid, 70% ethanol, 0.5% sodium bisulfite, 0.4% sodium hydroxide, 0.5% sodium hypochlorite, or a mixture of 2.2% hydrogen peroxide (H2O2) and 0.45% peracetic acid. Results The efficacy of the sanitizers varied with concentration and contact time to reduce decimal logarithmic (log10) population (n cycles). To kill 90% of the initial population (or one log10 cycle), the necessary time (D-value) was for P. aeruginosa into: (i) 0.5% citric acid, D = 3.8 min; (ii) 0.5% hydrochloric acid, D = 6.9 min; (iii) 70% ethanol, D = 9.7 min; (iv) 0.5% sodium bisulfite, D = 5.3 min; (v) 0.4% sodium hydroxide, D = 14.2 min; (vi) 0.5% sodium hypochlorite, D = 7.9 min; (vii) mixture of hydrogen peroxide (2.2%) plus peracetic acid (0.45%), D = 5.5 min. Conclusion The contact time of 180 min of the system with the mixture of H2O2+ peracetic acid, a total theoretical reduction of 6 log10 cycles was attained in the water purified storage tank and distribution loop. The contact time between the water purification system (WPS) and the sanitary agents should be reviewed to reach sufficient bioburden reduction (over 6 log10).

La explotación del acuífero de la Aldea (Gran Canaria) desde el punto de vista de la directiva marco del agua

[ES] El valle de La Aldea, al oeste de Gran Canaria, se dedica a la agricultura intensiva en un clima semi-árido. El agua de riego proviene de aguas superficiales y subterráneas. El acuífero está aislado del resto de la isla por el borde impermeable de la Caldera de Tejeda. El aluvial principal de La Aldea se comporta como un depósito de almacenamiento de agua que se llena y vacía, con un tiempo medio de renovación de aproximadamente 2 años. Las aguas subterráneas muestran una alta salinidad de origen natural, debido a la evapoconcentración de la deposición atmosférica y la interacción agua-roca, y antropogénica debida a los retornos de riego que producen contenidos en nitratos que pueden alcanzar los 700 mg/L. Se ha establecido un modelo conceptual de funcionamiento del acuífero y se han cuantificado los términos del balance de agua. El uso actual del acuífero está en conflicto con los requerimientos de la Directiva Marco del Agua (DMA). Sin embargo, dado que su uso es clave para el desarrollo económico del valle de La Aldea en particular, cabe plantear las excepciones legales específicas previstas en la DMA.

Post-project assessment and follow-up support for community managed rural water systems in Panama

The Environmental Health (EH) program of Peace Corps (PC) Panama and a non-governmental organization (NGO) Waterlines have been assisting rural communities in Panama gain access to improved water sources through the practice of community management (CM) model and participatory development. Unfortunately, there is little information available on how a water system is functioning once the construction is complete and the volunteer leaves the community. This is a concern when the recent literature suggests that most communities are not able to indefinitely maintain a rural water system (RWS) without some form of external assistance (Sara and Katz, 1997; Newman et al, 2002; Lockwood, 2002, 2003, 2004; IRC, 2003; Schweitzer, 2009). Recognizing this concern, the EH program director encouraged the author to complete a postproject assessment of the past EH water projects. In order to carry out the investigation, an easy to use monitoring and evaluation tool was developed based on literature review and the author’s three years of field experience in rural Panama. The study methodology consists of benchmark scoring systems to rate the following ten indicators: watershed, source capture, transmission line, storage tank, distribution system, system reliability, willingness to pay, accounting/transparency, maintenance, and active water committee members. The assessment of 28 communities across the country revealed that the current state of physical infrastructure, as well as the financial, managerial and technical capabilities of water committees varied significantly depending on the community. While some communities are enjoying continued service and their water committee completing all of its responsibilities, others have seen their water systems fall apart and be abandoned. Overall, the higher score were more prevalent for all ten indicators. However, even the communities with the highest scores requested some form of additional assistance. The conclusion from the assessment suggests that the EH program should incorporate an institutional support mechanism (ISM) to its sector policy in order to systematically provide follow-up support to rural communities in Panama. A full-time circuit rider with flexible funding would be able to provide additional technical support, training and encouragement to those communities in need.

Tanque de almacenamiento de GNL para la ampliación de la planta de regasificación de Barcelona

ENAGAS tiene la intención de ampliar el Terminal de Regasificación de GNL que tiene en el puerto de Barcelona. El presente Proyecto Básico define las instalaciones de uno de los Tanques de almacenamiento de GNL que se van a construir dentro del Alcance de dicha ampliación, con el suficiente detalle como para permitir a ENAGAS acometer las tareas previas a la ejecución del proyecto, a saber: 1. Planificar y presupuestar la fase de ejecución 2. Solicitar los Permisos y Autorizaciones necesarias de los Organismos competentes 3. Lanzar la Petición de Ofertas para el concurso llave en mano del EPC. Los trabajos de Ingeniería contenidos en el Proyecto Básico son los siguientes: Antecedentes y Datos básicos, Criterios de diseño, Descripción de instalaciones, Cálculos estructurales, Planos del Tanque de GNL, Definición de equipos y materiales a utilizar, Plan de ejecución del proyecto, Especificaciones técnicas para Ingeniería, Compras y Construcción, Paquete para Petición de Ofertas del EPC, Condiciones técnicas particulares, Programa de ejecución y Presupuesto de inversiones. ABSTRACT ENAGAS is expanding its LNG Regasification Terminal located in Barcelona Port (Spain). This Document reports the Front End Engineering and Design (FEED) works undertaken in relation to one of the LNG Storage Tanks to be built within the scope of that expansion. The Project FEED hereby presented comprehensively defines the LNG Storage Tank so as to allow ENAGAS to perform next stages of the Works, namely: 1. Plan and budget the Project Execution phase 2. Request Regulatory authorizations 3. Invite Contractors to bid for the LNG Tank EPC. Main components of the FEED Document contents are as follow:Background and Basic Data, Design Criteria, Description of LNG Tank elements, Engineering Calculations, LNG Tank Drawings, Equipment and Materials definition, Project Execution Plan (PEP), Technical Conditions, EPC Invitation to Tender (ITT) package, Execution Schedule and Cost Estimate.

Análisis de la viabilidad técnica de las aerobombas para el riego localizado

Actualmente la agricultura cubana, por ser un sector estratégico en la economía del país, incorpora en su desarrollo y gestión las energías renovables como criterio básico para su viabilidad futura. Sin embargo existen un número de problemas que limitan el desarrollo de estas fuentes energéticas en Cuba, entre los que se encuentran el conocimiento incompleto de su potencial de utilización. Por esta razón, la presente investigación tiene como objetivo la maximización de la superficie regada de un cultivo dado y la determinación del volumen de regulación mínimo, usando una aerobomba tipo, en condiciones ambientales dadas. Se desarrolla una metodología para predecir la máxima potencialidad de las aerobombas para un sistema de riego localizado, basada en el cálculo del balance diario entre las necesidades de agua del cultivo y la disponibilidad de agua. Mediante un ejemplo que ilustra el uso de esta metodología en el cultivo de tomate (Solanum lycopersicum L. var. FL - 5) bajo invernadero en Ciego de Ávila, Cuba, se hace una descripción de los elementos de la instalación propuesta para el suministro de agua por parte de la aerobomba. Se estudiaron varios factores, tales como la serie de velocidad del viento trihoraria ( h V3 , m s-1) para un año medio de viento y para un año medio de poco viento; el caudal suministrado por la aerobomba en función de la altura de elevación ( H , m); y la evapotranspiración diaria del cultivo en invernadero en función de la fecha de siembra. A partir de los factores mencionados se determinaron los volúmenes de agua mensuales necesarios para el riego ( r D , m3 ha-1), la capacidad del depósito de almacenamiento ( dep. V , m3), así como las áreas máximas regables ( r A , ha) para cada variante. Los resultados muestran que el período óptimo de bombeo eólico para el riego del cultivo de tomate en invernadero bajo las condiciones ambientales estudiadas es de noviembre a febrero, y que los factores que más influyen en la superficie que se puede regar con el bombeo eólico son la fecha de plantación y el volumen de depósito. Abstract Currently Cuban agriculture, as a strategic sector in the economy of the country, incorporates in its development and renewable energy management as a basic criterion for its future viability. However, there are a number of problems that limit the development of these energy sources in Cuba, among which are the incomplete knowledge of their potential use. For this reason, this research aims at maximizing the irrigated area of a given culture and determination of minimum control volume, using a type Windpump in given environmental conditions. We develop a methodology to predict the maximum potential of windmills for irrigation system, based on the daily balance calculation between the crop water needs and water availability. Through an example that illustrates the use of this methodology in the cultivation of tomato (Solanum lycopersicum L. var. FL - 5) under greenhouse in Ciego de Avila, Cuba, is a description of the elements of the proposed facility to supply water from the windmill. We studied several factors such as the number of trihoraria wind speed ( h V3 , m s- 1) for an average wind year and an average year with little wind, the flow supplied by the windmill depending on the lift height ( H , m) and daily crop evapotranspiration in greenhouse based on planting date. From the above factors were determined monthly water volumes needed for irrigation ( r D , m3 ha-1), the storage tank capacity ( dep. V , m3) and peak areas irrigated ( r A , ha) for each variant. The results show that the optimal period wind pumping for irrigation of greenhouse tomato crop under the environmental conditions studied is from November to February, and that the factors that influence the surface that can be irrigated with wind pumping are planting date and amount of deposit.

Diseño de una hoja Excel para un tanque de almacenamiento de gasóleo de automoción

El presente proyecto, consiste en el diseño básico de una hoja Excel para un tanque de almacenamiento de gasóleo de automoción (gasóleo A). El presente tanque se ha situado en el parque de almacenamiento de Loeches (Comunidad de Madrid). Se han realizado los cálculos necesarios para el diseño de todas las partes de dicho tanque, la envolvente, el fondo de tanque y el techo. Al igual que el cálculo de peso de éste, y un listado de accesorios adicionales necesarios para su puesta en marcha. Se ha desarrollado la programación en Excel, de una ficha para calcular los parámetros principales del tanque diseñado. Se ha llevado a cabo el diseño y fabricación de un tanque de acero, vertical, cilíndrico, de fondo plano, no enterrado, soldados, para el almacenamiento de líquidos a temperatura ambiente. La capacidad del tanque es de un volumen nominal de 25.000 m3 y una altura de 20 metros, se almacenará gasóleo de automoción, con una densidad de 835 kg/m3. Este tipo de gasóleo es el producto derivado del petróleo más consumido en España.This project consists of the basic design of an Excel spreadsheet to a storage tank of diesel fuel (oil A). This tank is located in the storage yard Loeches (Madrid). It have been made the necessary calculations for the design of all parts of the tank, the envelope, the tank bottom and roof. As the weight calculation thereof, and a list of additional accessories required for its implementation and location. It has been developed programming Excel, a record key parameters to calculate tank designed. It has been carried out the design and manufacture of a steel tank, vertical, cylindrical, flat bottom, not buried, soldiers, for storing liquids at room temperature. The tank capacity is of a nominal capacity of 25,000 m3 and a height of 20 meters, diesel fuel is stored, with a density of 835 kg/m3. This type of oil is the oil product most consumed in Spain.

Criterios de selección de tecnologías sostenibles de generación de energía para el riego en invernaderos

Esta tesis desarrolla una metodología para comparar la viabilidad económica de distintas tecnologías de suministro energético para el bombeo de agua de riego en invernaderos tanto en España, Cuba o Pakistán (países con diferentes estados de desarrollo). En concreto, se analiza el bombeo directo eólico, el bombeo solar fotovoltaico, el bombeo con generadores diesel, y mediante conexión a la red eléctrica. El análisis tuvo en cuenta los recursos eólicos y solar, la altura de elevación, el tamaño de invernadero, la distancia al punto de conexión a la red, las necesidades de almacenamiento de agua y las fechas de siembra. Las comparaciones se realizaron usando un criterio técnico-económico basado en el coste normalizado de la energía de cada tecnología. En los tres países, el bombeo directo eólico no sería económicamente recomendable, en el caso de existir una conexión a la red. Allí donde no existe conexión a la red, la distancia a la red y los recursos eólico y solar disponibles son los factores clave a tener en cuenta a la hora de decidir entre las diferentes tecnologías. Por otro lado, la altura del bombeo del agua tiene una gran influencia sobre la viabilidad económica del bombeo directo eólico, mucho más que, por ejemplo, en el caso del bombeo solar fotovoltaico. En general, los resultados revelan que los factores críticos a tener en cuenta a la hora de elegir la solución energética óptima son diferentes en cada uno de los países. En el caso de España, la proximidad a los puntos de conexión de la red eléctrica determina que ésta sea la mejor opción. El limitado potencial eólico es el factor limitante en Pakistán. En Cuba, la altura del bombeo, la distancia al punto de conexión de la red eléctrica y el almacenamiento de agua necesario son los factores críticos para determinar la tecnología más apropiada para el bombeo al disponer de buenos recursos solar y eólico. ABSTRACT This thesis develops a methodology for comparing the economic feasibility of wind pump technology, solar photovoltaic pumping, diesel generators, and connection to the electrical grid to provide energy for pumping irrigation water in commercial greenhouses in Spain, Cuba and Pakistan (countries with different developmental backgrounds). The analysis studied the importance of the wind and solar resource, the water elevation, the greenhouse size, the distance to the grid, the pumping elevation, the water storage tank volume requirements, and the planting dates. Comparisons were made in terms of the levelised cost of energy associated with each technology. For all three countries, if a grid connection was already in place, installing wind pumps would be economically unwise. Where no grid connection exists, the distance to the grid and the wind and solar resources available are key factors to be taken into consideration when deciding between options. Finally, the water elevation has a major influence on the economic feasibility of wind pump technology, much more than, for example, on solar photovoltaic pumping technology. The results reveal that, generally, the critical factors to consider when making energy management decisions differ depending between countries. In Spain, the proximity of the electrical grid makes the connection to it the best option. In Pakistan, scarce wind resources are a serious limiting factor. Cuba, however, has good wind and solar resources; water elevation, distance to the grid, and water storage needed are the critical factors when determining the economic feasibility of wind pumping.

Investigation of Performance Enhancements for a Liquid-Desiccant Solar Air-Conditioner

Thermally driven liquid-desiccant air-conditioners (LDAC) are a proven but still developing technology. LDACs can use a solar thermal system to reduce the operational cost and environmental impact of the system by reducing the amount of fuel (e.g. natural gas, propane, etc.) used to drive the system. LDACs also have a key benefit of being able to store energy in the form of concentrated desiccant storage. TRNSYS simulations were used to evaluate several different methods of improving the thermal and electrical coefficients of performance (COPt and COPe) and the solar fraction (SF) of a LDAC. The study analyzed a typical June to August cooling season in Toronto, Ontario. Utilizing properly sized, high-efficiency pumps increased the COPe to 3.67, an improvement of 55%. A new design, featuring a heat recovery ventilator on the scavenging-airstream and an energy recovery ventilator on the process-airstream, increased the COPt to 0.58, an improvement of 32%. This also improved the SF slightly to 54%, an increase of 8%. A new TRNSYS TYPE was created to model a stratified desiccant storage tank. Different volumes of desiccant were tested with a range of solar array system sizes. The largest storage tank coupled with the largest solar thermal array showed improvements of 64% in SF, increasing the value to 82%. The COPe was also improved by 17% and the COPt by 9%. When combining the heat recovery systems and the desiccant storage systems, the simulation results showed a 78% increase in COPe and 30% increase in COPt. A 77% improvement in SF and a 17% increase in total cooling rate were also predicted by the simulation. The total thermal energy consumed was 10% lower and the electrical consumption was 34% lower. The amount of non-renewable energy needed from the natural gas boiler was 77% lower. Comparisons were also made between LDACs and vapour-compression (VC) systems. Dependent on set-up, LDACs provided higher latent cooling rates and reduced electrical power consumption. Negatively, a thermal input was required for the LDAC systems but not for the VC systems.

Guidance manual for petroleum-related LUST cleanups in Illinois /

"Spring 1990."

Investigation of Performance Enhancements for a Liquid-Desiccant Solar Air-Conditioner

Thermally driven liquid-desiccant air-conditioners (LDAC) are a proven but still developing technology. LDACs can use a solar thermal system to reduce the operational cost and environmental impact of the system by reducing the amount of fuel (e.g. natural gas, propane, etc.) used to drive the system. LDACs also have a key benefit of being able to store energy in the form of concentrated desiccant storage. TRNSYS simulations were used to evaluate several different methods of improving the thermal and electrical coefficients of performance (COPt and COPe) and the solar fraction (SF) of a LDAC. The study analyzed a typical June to August cooling season in Toronto, Ontario. Utilizing properly sized, high-efficiency pumps increased the COPe to 3.67, an improvement of 55%. A new design, featuring a heat recovery ventilator on the scavenging-airstream and an energy recovery ventilator on the process-airstream, increased the COPt to 0.58, an improvement of 32%. This also improved the SF slightly to 54%, an increase of 8%. A new TRNSYS TYPE was created to model a stratified desiccant storage tank. Different volumes of desiccant were tested with a range of solar array system sizes. The largest storage tank coupled with the largest solar thermal array showed improvements of 64% in SF, increasing the value to 82%. The COPe was also improved by 17% and the COPt by 9%. When combining the heat recovery systems and the desiccant storage systems, the simulation results showed a 78% increase in COPe and 30% increase in COPt. A 77% improvement in SF and a 17% increase in total cooling rate were also predicted by the simulation. The total thermal energy consumed was 10% lower and the electrical consumption was 34% lower. The amount of non-renewable energy needed from the natural gas boiler was 77% lower. Comparisons were also made between LDACs and vapour-compression (VC) systems. Dependent on set-up, LDACs provided higher latent cooling rates and reduced electrical power consumption. Negatively, a thermal input was required for the LDAC systems but not for the VC systems.

Exergetic, energetic, economic and environmental evaluation of concentrated solar power plants in Libya

The PhD project addresses the potential of using concentrating solar power (CSP) plants as a viable alternative energy producing system in Libya. Exergetic, energetic, economic and environmental analyses are carried out for a particular type of CSP plants. The study, although it aims a particular type of CSP plant – 50 MW parabolic trough-CSP plant, it is sufficiently general to be applied to other configurations. The novelty of the study, in addition to modeling and analyzing the selected configuration, lies in the use of a state-of-the-art exergetic analysis combined with the Life Cycle Assessment (LCA). The modeling and simulation of the plant is carried out in chapter three and they are conducted into two parts, namely: power cycle and solar field. The computer model developed for the analysis of the plant is based on algebraic equations describing the power cycle and the solar field. The model was solved using the Engineering Equation Solver (EES) software; and is designed to define the properties at each state point of the plant and then, sequentially, to determine energy, efficiency and irreversibility for each component. The developed model has the potential of using in the preliminary design of CSPs and, in particular, for the configuration of the solar field based on existing commercial plants. Moreover, it has the ability of analyzing the energetic, economic and environmental feasibility of using CSPs in different regions of the world, which is illustrated for the Libyan region in this study. The overall feasibility scenario is completed through an hourly analysis on an annual basis in chapter Four. This analysis allows the comparison of different systems and, eventually, a particular selection, and it includes both the economic and energetic components using the “greenius” software. The analysis also examined the impact of project financing and incentives on the cost of energy. The main technological finding of this analysis is higher performance and lower levelized cost of electricity (LCE) for Libya as compared to Southern Europe (Spain). Therefore, Libya has the potential of becoming attractive for the establishment of CSPs in its territory and, in this way, to facilitate the target of several European initiatives that aim to import electricity generated by renewable sources from North African and Middle East countries. The analysis is presented a brief review of the current cost of energy and the potential of reducing the cost from parabolic trough- CSP plant. Exergetic and environmental life cycle assessment analyses are conducted for the selected plant in chapter Five; the objectives are 1) to assess the environmental impact and cost, in terms of exergy of the life cycle of the plant; 2) to find out the points of weakness in terms of irreversibility of the process; and 3) to verify whether solar power plants can reduce environmental impact and the cost of electricity generation by comparing them with fossil fuel plants, in particular, Natural Gas Combined Cycle (NGCC) plant and oil thermal power plant. The analysis also targets a thermoeconomic analysis using the specific exergy costing (SPECO) method to evaluate the level of the cost caused by exergy destruction. The main technological findings are that the most important contribution impact lies with the solar field, which reports a value of 79%; and the materials with the vi highest impact are: steel (47%), molten salt (25%) and synthetic oil (21%). The “Human Health” damage category presents the highest impact (69%) followed by the “Resource” damage category (24%). In addition, the highest exergy demand is linked to the steel (47%); and there is a considerable exergetic demand related to the molten salt and synthetic oil with values of 25% and 19%, respectively. Finally, in the comparison with fossil fuel power plants (NGCC and Oil), the CSP plant presents the lowest environmental impact, while the worst environmental performance is reported to the oil power plant followed by NGCC plant. The solar field presents the largest value of cost rate, where the boiler is a component with the highest cost rate among the power cycle components. The thermal storage allows the CSP plants to overcome solar irradiation transients, to respond to electricity demand independent of weather conditions, and to extend electricity production beyond the availability of daylight. Numerical analysis of the thermal transient response of a thermocline storage tank is carried out for the charging phase. The system of equations describing the numerical model is solved by using time-implicit and space-backward finite differences and which encoded within the Matlab environment. The analysis presented the following findings: the predictions agree well with the experiments for the time evolution of the thermocline region, particularly for the regions away from the top-inlet. The deviations observed in the near-region of the inlet are most likely due to the high-level of turbulence in this region due to the localized level of mixing resulting; a simple analytical model to take into consideration this increased turbulence level was developed and it leads to some improvement of the predictions; this approach requires practically no additional computational effort and it relates the effective thermal diffusivity to the mean effective velocity of the fluid at each particular height of the system. Altogether the study indicates that the selected parabolic trough-CSP plant has the edge over alternative competing technologies for locations where DNI is high and where land usage is not an issue, such as the shoreline of Libya.

UST news

The Underground Storage Tank program at the South Carolina Department of Health and Environmental Control publishes a biannual publication of compliance, technical, and financial information to supply outreach to tank owners, contractors, and the general public.