92 resultados para Coal-fired power plants

em Universidad Politécnica de Madrid


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Climate change conference was hold in Copenhagen in 2009, global warming became the worldwide focus once again. China as a developing country has paid more attention for this environmental problem. In China, a large part of carbon dioxide is emitted to the atmosphere from combustion of fossil fuels in power plants. How to control emission of the greenhouse gas into atmosphere is becoming an urgent concern. Among numerous methods, CO2 capture is the hope to limit the amount of CO2 emitted into the air. The well-established method for CO2 capture is to remove CO2 by absorption into solutions in conventional equipment. Absorbents used for CO2 and H2S capture are important choice for CO2 capture technology. It is related to the cost and efficiency of plant directly and is essential to investigate the proposed CO2 and H2S absorbents.

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En los últimos quince años se ha producido una liberalización de los mercados eléctricos en los distintos países de ámbito occidental que ha ido acompañado de un incremento por la preocupación por la incidencia de las distintas tecnologías de generación en el entorno medioambiental. Ello se ha traducido en la aparición de un marco regulatorio más restrictivo sobre las tecnologías de generación fósiles, con mayor incidencia en las derivadas de productos petrolíferos y carbón. A nivel mundial han ido apareciendo cambios normativos relativos a las emisiones de distintos elementos contaminantes (CO2, SO2, NOx…), que hacen que en particular las centrales térmicas de carbón vean muy afectadas su rentabilidad y funcionamiento. Esta situación ha supuesto que la tecnología de generación eléctrica con carbón haya avanzado considerablemente en los últimos años (calderas supercríticas, sistemas de desulfuración, gasificación del carbón…). No obstante, el desarrollo de la generación con energías renovables, la generación con gas mediante centrales de ciclo combinado y la opinión social relativa a la generación con carbón, principalmente en Europa, suponen un serio obstáculo a la generación con carbón. Por consiguiente, se hace necesario buscar vías para optimizar la competitividad de las centrales de carbón y el camino más razonable es mejorar el margen esperado de estas plantas y en particular el coste de adquisición del carbón. Ello se hace aún más importante por el hecho de existir numerosas centrales de carbón y un elevado número de nuevos proyectos constructivos de centrales de carbón en países asiáticos. Por consiguiente, el objeto de la presente tesis doctoral se centra en definir una metodología para optimizar la compra de carbón, desde el punto de vista económico y técnico, con destino a su consumo en una central térmica, con ello reducir el coste del carbón consumido y mejorar su competitividad. También se enfoca a determinar que herramientas pueden ser utilizadas para optimizar la gestión del carbón después de su compra y con ello abrir la posibilidad de obtener márgenes adicionales para dicho carbón. De acuerdo con este objetivo, el autor de la presente Tesis Doctoral realiza tres aportaciones novedosas en el ámbito de la contratación de carbón térmico y su optimización posterior: - Evaluación de carbones para su adquisición considerando el efecto de la calidad del carbón en el coste de generación asociado a cada carbón ofertado. - Creación, desarrollo, implantación y utilización de una potente herramienta de planificación de Combustibles. Esta herramienta, está diseñada con el objeto de determinar la solución económica óptima de aprovisionamientos, consumos y niveles de existencias para un parque de generación con centrales de carbón y fuelóleo. - La extensión de una metodología contractual habitual en el mercado spot de Gas Natural Licuado, a la contratación spot de Carbón de Importación. Esta se basa en el desarrollo de Acuerdos Marcos de Compra/Venta de carbón, que por su flexibilidad permitan obtener resultados económicos adicionales después de la compra de un carbón. Abstract In the last fifteen years, a liberalization of the electrical markets has occurred in the western countries. This process has been accompanied by an increasing concern of the impact of the different generation technologies towards the environment. This has motivated a regulated framework restricting the use of fossil fuels, impacting a great deal in coal and oil based products. Worldwide, new legal changes have been arising related to the emissions of the different pollutants (CO2, SO2, NOx…). These changes have had a deep impact in the feasibility, profit and running of coal fired power plants. This situation has motivated the coal electrical generation technologies to move forward in an important way in the last few years (supercritical furnaces, desulphuration plants, coal gasification…). Nevertheless, the development of the renewable generation, the gas combined cycle generation and the social opinion related to the coal electrical generation, mainly in Europe, have created a serious obstacle to the generation of electricity by coal. Therefore it is necessary to look for new paths in order to optimize the competitiveness of the coal fired power plants and the most reasonable way is to improve the expected margin of these plants and particularly the coal purchase cost. All of the above needs to be taken into context with the large number of existing coal fired power plants and an important number of new projects in Asian countries. Therefore, the goal of the current doctoral dissertation is focused to define a methodology to be considered in order to optimize the coal purchase, from an economical and a technical point of view. This coal, destined for power plant consumption, permits the reduction of consumption coal cost and improves the plant’s competitiveness. This document is also focused to define what tools we can use to optimize the coal management after deal closing and therefore open the possibility to get further margins. According to this goal, the author of this doctoral dissertation provides three important new ideas in the ambit of contracting steam coal and the posterior optimization: - Evaluation of coal purchases, considering the effect of coal quality on the cost of generation associated with each type of coal offered. - The creation, development, deployment and use of a strong planning tool of fuels. This tool is designed for the purpose of determining the optimal economic solution of fuel supply, consumption and stock levels for a power generation portfolio using coal and fuel oil fired power plants. - The application of a common contractual methodology in the spot market of Liquid Natural Gas, for the contracting spot imported coal. This is based on the development of Framework Agreements for the Purchasing / Sale of coal, which because of its flexibility allows for the gain of additional financial results after the purchase of coal.

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The utilisation of biofuels in gas turbines is a promising alternative to fossil fuels for power generation. It would lead to significant reduction of CO2 emissions using an existing combustion technology, although significant changes seem to be needed and further technological development is necessary. The goal of this work is to perform energy and exergy analyses of the behaviour of gas turbines fired with biogas, ethanol and synthesis gas (bio-syngas), compared with natural gas. The global energy transformation process (i.e. from biomass to electricity) has also been studied. Furthermore, the potential reduction of CO2 emissions attained by the use of biofuels has been determined, considering the restrictions regarding biomass availability. Two different simulation tools have been used to accomplish the aims of this work. The results suggest a high interest and the technical viability of the use of Biomass Integrated Gasification Combined Cycle (BIGCC) systems for large scale power generation.

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In the present uncertain global context of reaching an equal social stability and steady thriving economy, power demand expected to grow and global electricity generation could nearly double from 2005 to 2030. Fossil fuels will remain a significant contribution on this energy mix up to 2050, with an expected part of around 70% of global and ca. 60% of European electricity generation. Coal will remain a key player. Hence, a direct effect on the considered CO2 emissions business-as-usual scenario is expected, forecasting three times the present CO2 concentration values up to 1,200ppm by the end of this century. Kyoto protocol was the first approach to take global responsibility onto CO2 emissions monitoring and cap targets by 2012 with reference to 1990. Some of principal CO2emitters did not ratify the reduction targets. Although USA and China spur are taking its own actions and parallel reduction measures. More efficient combustion processes comprising less fuel consuming, a significant contribution from the electricity generation sector to a CO2 dwindling concentration levels, might not be sufficient. Carbon Capture and Storage (CCS) technologies have started to gain more importance from the beginning of the decade, with research and funds coming out to drive its come in useful. After first researching projects and initial scale testing, three principal capture processes came out available today with first figures showing up to 90% CO2 removal by its standard applications in coal fired power stations. Regarding last part of CO2 reduction chain, two options could be considered worthy, reusing (EOR & EGR) and storage. The study evaluates the state of the CO2 capture technology development, availability and investment cost of the different technologies, with few operation cost analysis possible at the time. Main findings and the abatement potential for coal applications are presented. DOE, NETL, MIT, European universities and research institutions, key technology enterprises and utilities, and key technology suppliers are the main sources of this study. A vision of the technology deployment is presented.

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In the C02 capture from power generation, the energy penalties for the capture are one of the main challenges. Nowadays, the post-combustion methods have energy penalties 10wer than the oxy combustion and pre-combustion technologies. One of the main disadvantages of the post combustion method is the fact that the capture ofC02at atmospheric pressure requires quite big equipment for the high flow rates of flue gas, and the 10w partial pressure of the CO2generates an important 10ss of energy. The A1lam cyc1e presented for NETPOWER gives high efficiencies in the power production and 10w energy penalties. A simulation of this cyc1e is made together with a simulation of power plants with pre-combustion and post-combustion capture and without capture for natural gas and forcoa1. The simulations give 10wer efficiencies than the proposed for NETPOWER For natural gas the efficiency is 52% instead of the 59% presented, and 33% instead of51% in the case of using coal as fuel. Are brought to light problems in the CO2compressor due the high flow ofC02that is compressed unti1300 bar to be recyc1ed into the combustor.

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In this paper, the dynamic response of a hydro power plant for providing secondary regulation reserve is studied in detail. Special emphasis is given to the elastic water column effects both in the penstock and the tailrace tunnel. For this purpose, a nonlinear model based on the analogy between mass and momentum conservation equations of a water conduit and those of wave propagation in transmission lines is used. The influence of the plant configuration and design parameters on the fulfilment of the Spanish Electrical System Operator requirements is analysed

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In this paper, the dynamic response of a hydro power plant for providing secondary regulation reserve is studied in detail. S pecial emphasis is given to the elastic water column effects both in the penstock and the tailrace tunnel. For this purpose, a nonline ar model based on the analogy between mass and momentum conservation equations of a water conduit and those of wave propagation in transmission lines is used. The influence of the plant configuration and design parameters on the fulfilment of the Spanish Electrical System Operator requirem ents is analysed.

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Europe needs to restructure its energy system. The aim to decrease the reliance on fossil fuels to a higher dependence on renewable energy has now been imposed by The European Commission. In order to achieve this goal there is a great interest in Norway to become "The Green Battery of Europe". In the pursuit of this goal a GIS-tool was created to investigate the pump storage potential in Norway. The tool searches for possible connections between existing reservoirs and dams with the criteria selected by the user. The aim of this thesis was to test the tool and see if the results suggested were plausible, develop a cost calculation method for the PSH lines, and make suggestions for further development of the tool. During the process the tool presented many non-feasible pumped storage hydropower (PSH) connections. The area of Telemark was chosen for the more detailed study. The results were discussed and some improvements were suggested for further development of the tool. Also a sensitivity test was done to see which of the parameters set by the user are the most relevant for the PSH connection suggestion. From a range of the most promising PSH plants suggested by the tool, the one between Songavatn and Totak was chosen for a case study, where there already exists a power plant between both reservoirs. A new Pumped Storage Plant was designed with a power production of 1200 MW. There are still many topics open to discussion, such as how to deal with environmental restrictions, or how to deal with inflows and outflows of the reservoirs from the existing power plants. Consequently the GIS-tool can be a very useful tool to establish the best possible connections between existing reservoirs and dams, but it still needs a deep study and the creation of new parameters for the user.

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Solar thermal power plants are usually installed in locations with high yearly average solar radiation, often deserts. In such conditions, cooling water required for thermodynamic cycles is rarely available. Moreover, when solar radiation is high, ambient temperature is very high as well; this leads to excessive condensation temperature, especially when air-condensers are used, and decreases the plant efficiency. However, temperature variation in deserts is often very high, which drives to relatively low temperatures during the night. This fact can be exploited with the use of a closed cooling system, so that the coolant (water) is chilled during the night and store. Chilled water is then used during peak temperature hours to cool the condenser (dry cooling), thus enhancing power output and efficiency. The present work analyzes the performance improvement achieved by night thermal cool storage, compared to its equivalent air cooled power plant. Dry cooling is proved to be energy-effective for moderately high day–night temperature differences (20 °C), often found in desert locations. The storage volume requirement for different power plant efficiencies has also been studied, resulting on an asymptotic tendency.

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System Advisor Model is a software tool develped by National Renewable Laboratory (NREL), Department Of Energy, USA to design Solar Power Plants.

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The water time constant and mechanical time constant greatly influences the power and speed oscillations of hydro-turbine-generator unit. This paper discusses the turbine power transients in response to different nature and changes in the gate position. The work presented here analyses the characteristics of hydraulic system with an emphasis on changes in the above time constants. The simulation study is based on mathematical first-, second-, third- and fourth-order transfer function models. The study is further extended to identify discrete time-domain models and their characteristic representation without noise and with noise content of 10 & 20 dB signal-to-noise ratio (SNR). The use of self-tuned control approach in minimising the speed deviation under plant parameter changes and disturbances is also discussed.

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The supercritical Rankine power cycle offers a net improvement in plant efficiency compared with a subcritical Rankine cycle. For fossil power plants the minimum supercritical steam turbine size is about 450MW. A recent study between Sandia National Laboratories and Siemens Energy, Inc., published on March 2013, confirmed the feasibility of adapting the Siemens turbine SST-900 for supercritical steam in concentrated solar power plants, with a live steam conditions 230-260 bar and output range between 140-200 MWe. In this context, this analysis is focused on integrating a line-focus solar field with a supercritical Rankine power cycle. For this purpose two heat transfer fluids were assessed: direct steam generation and molten salt Hitec XL. To isolate solar field from high pressure supercritical water power cycle, an intermediate heat exchanger was installed between linear solar collectors and balance of plant. Due to receiver selective coating temperature limitations, turbine inlet temperature was fixed 550ºC. The design-point conditions were 550ºC and 260 bar at turbine inlet, and 165 MWe Gross power output. Plant performance was assessed at design-point in the supercritical power plant (between 43-45% net plant efficiency depending on balance of plantconfiguration), and in the subcritical plant configuration (~40% net plant efficiency). Regarding the balance of plant configuration, direct reheating was adopted as the optimum solution to avoid any intermediate heat exchanger. One direct reheating stage between high pressure turbine and intermediate pressure turbine is the common practice; however, General Electric ultrasupercritical(350 bar) fossil power plants also considered doubled-reheat applications. In this study were analyzed heat balances with single-reheat, double-reheat and even three reheating stages. In all cases were adopted the proper reheating solar field configurations to limit solar collectors pressure drops. As main conclusion, it was confirmed net plant efficiency improvements in supercritical Rankine line-focus (parabolic or linear Fresnel) solar plant configurations are mainly due to the following two reasons: higher number of feed-water preheaters (up to seven)delivering hotter water at solar field inlet, and two or even three direct reheating stages (550ºC reheating temperature) in high or intermediate pressure turbines. However, the turbine manufacturer should confirm the equipment constrains regarding reheating stages and number of steam extractions to feed-water heaters.

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Linear Fresnel collectors are identified as a technology that should play a main role in order to reduce cost of Concentrating Solar Power. An optical and thermal analysis of the different blocks of the solar power plant is carried out, where Fresnel arrays are compared with the most extended linear technology: parabolic trough collectors. It is demonstrated that the optical performance of Fresnel array is very close to that of PTC, with similar values of maximum flux intensities. In addition, if the heat carrier fluid flows in series by the tubes of the receiver, relatively high thermal efficiencies are achieved. Thus, an annual solar to electricity efficiency of 19% is expected, which is similar to the state of the art in PTCs; this is done with a reduction of costs, thanks to lighter structures, that drives to an estimation of LCOE of around 6.5 c€/kWh.

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This article has been extracted from the results of a thesis entitled “Potential bioelectricity production of the Madrid Community Agricultural Regions based on rye and triticale biomass.” The aim was, first, to quantify the potential of rye (Secale Cereale L.) and triticale ( Triticosecale Aestivum L.) biomass in each of the Madrid Community agricultural regions, and second, to locate the most suitable areas for the installation of power plants using biomass. At least 17,339.9 t d.m. of rye and triticale would be required to satisfy the biomass needs of a 2.2 MW power plant, (considering an efficiency of 21.5%, 8,000 expected operating hours/year and a biomass LCP of 4,060 kcal/kg for both crops), and 2,577 ha would be used (which represent 2.79% of the Madrid Community fallow dry land surface). Biomass yields that could be achieved in Madrid Community using 50% of the fallow dry land surface (46,150 ha representing 5.75% of the Community area), based on rye and triticale crops, are estimated at 84,855, 74,906, 70,109, 50,791, 13,481, and 943 t annually for the Campiña, Vegas, Sur Occidental, Área Metropolitana, Lozoya-Somosierra, and Guadarrama regions. The latter represents a bioelectricity potential of 10.77, 9.5, 8.9, 6.44, 1.71, and 0.12 MW, respectively.

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El empleo de nuevas adiciones en el cemento se plantea como una vía para que éste sea un material más sostenible. En este contexto, las cenizas de fondo o cenicero de las centrales termoeléctricas de carbón actualmente se están llevando a vertederos creando un problema medioambiental o se están empleando con usos minoritarios. Sin embargo, la presente Tesis doctoral demuestra cómo este material puede ser empleado como un componente principal de los cementos portland mezclado en una proporción optimizada con las cenizas volantes o solo. Por tanto, este estudio se puede considerar como un trabajo prenormativo que cubre las demandas de la sociedad tanto económicas como ambientales. Se han estudiado las propiedades químicas, físicas y mecánicas de las cenizas de fondo o cenicero de las centrales termoeléctricas de carbón como una adición potencial de los cementos portland (con adiciones) en comparación con los cementos portland con cenizas volantes. En consecuencia, el objeto de la presente Tesis Doctoral es el análisis de las prestaciones de morteros elaborados con clínkeres de cemento portland y cenizas de fondo o cenicero con cenizas volantes de las centrales termoeléctricas de carbón en unos porcentajes similares a los correspondientes a los CEM II/A-V, CEM II/B-V y CEM IV/A (V) de la UNE-EN 197-1:2011. La caracterización de las cenizas de fondo o cenicero y de las cenizas volantes de las centrales termoeléctricas de carbón se ha realizado mediante las técnicas analíticas de FRX, ICP, análisis químicos, DRX, densidad, granulometría láser, superficie específica Blaine, ATD, TG, puzolanicidad, MEB y EDX; mientras que la caracterización de las mezclas se ha realizado mediante análisis químico (análisis químico, FRX e ICP y), DRX, MIP, granulometría láser, puzolanicidad, MEB y EDX, agua de consistencia normal, inicio y final de fraguado, estabilidad de volumen, colorimetría, calor de hidratación, DTA y TG, asícomo ensayos de resistencia; resistencia a flexión y compresión y ensayos de durabilidad (carbonatación natural, resistencia al hielo-deshielo, resistencia a la acción de los sulfatos y resistencia a la reacción árido-álcali). Finalmente, se han comprobado las propiedades de las cenizas de cenicero y cenizas volantes en hormigones, realizando ensayos de resistencia a compresión y resistividad. Los resultados obtenidos indican que la sustitución parcial o completa de las cenizas volantes por las de cenicero no tiene un efecto tecnológicamente importante en las propiedades ni mecánicas ni durables, incluso los mejora en determinados aspectos. Por tanto, se recomienda la normalización de las cenizas de fondo o cenicero de las centrales termoeléctricas de carbón como componente principal de los cementos portland comunes de la UNE-EN 197-1:2011. Actualmente, la mayoría de las cenizas de fondo se consideran como un residuo que no tiene un posible uso. Sólo se han encontrado algunos datos relativos a la aplicación de este material combinado con cenizas volantes como un componente principal de los cementos portland. Por tanto, la realización de un estudio integrado considerando aspectos que van desde la caracterización de las cenizas hasta las mezclas de conglomerante y la hidratación de éstas, desarrollo de resistencias y demás prestaciones y durabilidad (carbonatación natural, resistencia al hielo-deshielo, resistencia a la acción de los sulfatos y resistencia a la reacción árido-álcali), así como los ensayos de resistencia en hormigón es totalmente novedoso. Como resultado final se propone incorporar estas nuevas adiciones en aplicaciones particulares y en la norma más apropiada para ello. Los resultados han demostrado que la sustitución completa o parcial de las cenizas volantes por cenizas de fondo o cenicero de las centrales termoeléctricas de carbón en cementos de los tipos CEM II/A-V, CEM II/B-V y CEM IV/A no afecta de forma significativa en la resistencia a compresión a 1, 3 ,7, 28 ni 90 días ni a la durabilidad. En parte esto se debe a que la composición química de ambas cenizas es muy similar en la mayoría de los elementos tales como Fe2O3, TiO2, P2O5, SrO2, aunque en algún caso, como en el ZnO, se encuentra alguna ligera diferencia. Por tanto, se pueden esperar unas ligeras diferencias en el mecanismo de hidratación de las diferentes mezclas estudiadas. La presencia de los óxidos mencionados afectará a la composición de la fase acuosa y, en consecuencia, podrían ser elementos lixiviables. Asimismo, influyen de distinta manera en propiedades tales como los tiempos de fraguado y en la durabilidad. New additions to the cement are needed to achieve a more sustainable construction material. Within this context, bottom ashes produced in coal-fired power stations are currently wastes which are dumped provoking an environmental problem. Only in few cases are being used in minor applications. However, the present PhD Thesis shows how this material can be used as a main constituent of Portland cement when it is mixed in an optimised proportion with fly ashes or added to the Portland clinker alone. Therefore, this study may also be considered as a pre-standardization work which covers both the environmental and economic demands of society. Chemical, physical and mechanical characteristics of pulverized coal combustion bottom ash used as a potential constituent of Portland cements (with additions) are studied in comparison to Portland cements with fly ashes. Therefore, the aim of this experimental PhD Thesis is the analysis of the performance of mortars made of clinker of Portland cement and bottom and/or fly ashes in similar proportions to those of CEM II/A-V, CEM II/B-V and CEM IV/A (V) according to EN 197-1:2011. Characterisation of bottom and fly ashes has been done by XRF, ICP, chemical analyses, XRD, density, laser granulometry, Blaine, ATD, TG, pozzolanity, SEM and EDS. Characterisation of bottom and fly ashes mixes has been perform by chemical analyses, XRF, ICP, XRD, MIP, laser granulometry, pozzolanity, SEM, EDS, setting time, soundness, colorimetric test, heat of hydration, ATD, TG, compressive strength, and durability tests (natural carbonation, frost-thaw resistance, sulphate resistance and silica-alkali resistance). In conclusion, it can be established that partial or complete replacement of fly ash by bottom ash has neither significant effect on mechanical nor durability properties. Even, they are improved in several aspects. Therefore, it is recommended to standardise the bottom ash as a main cement constituent of the European standard EN 197-1:2011. Nowadays, most bottom ashes are considered as waste without any potential re-use. Only a few papers deal with the study of this material and its use mixed with fly ashes to be employed as a main constituent of Portland cement. Therefore, the execution of an integrated study considering together aspects from the initial characterization of the ashes and blinder mixes to the hydration steps, strength achievement, leading behaviour and durability (natural carbonation, sulphate attack, aggregate-alcali reaction and freeze-thaw resistance) is totally new. As result, it is proposed to include this new addition for particular applications in the appropriate cement standard. The results have shown that with regard to the compressive strength at 1, 3, 7, 28 and 90 days, partial or complete replacement of fly ash by bottom ash in CEM II/A-V, CEM II/B-V and CEM IV/A has no more significant effects. Partially, this can be explained because the bottom ash contains a similar amount of most of the elements, Fe2O3, TiO2, P2O5, SrO2, and so on, instead of ZnO. Therefore, slight hydration differences are expected. The presence of such oxides might have a significant effect on pore solution concentration and so will be leachable constituents. They will also play an important role in the cement properties such as setting times and durability.