Comparison Between Existing Rankine Cycle Refrigeration Systems and Hygroscopic Cycle Technology (HCT) †
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Contracción Territorial Y Ordenación Urbana Para Encarar El Ciclo Post‐Minero En Mieres (Asturias‐España)
Contracción territorial y ordenación urbana para encarar el ciclo post‐minero en Mieres (Asturias‐España) Shrinkage and urban planning to face the post‐mining cycle in Mieres (Asturias‐Spain) FERMÍN RODRÍGUEZ GUTIÉRREZ Catedrático de Análisis Geográfico Regional Departamento de Geografía y CeCodet Universidad de Oviedo, España [email protected] ORCID: 0000-0002-6068-7858 RAFAEL MENÉNDEZ FERNÁNDEZ Doctor en Geografía CeCodet Universidad de Oviedo, España [email protected] ORCID: 0000-0002-4644-0066 Recibido/Aceptado: 29-09-2018 / 04-04-2019. Cómo citar: Rodríguez Gutiérrez, Fermín y Menéndez Fernández, Rafael (2019): “Contracción territorial y ordenación urbana para encarar el ciclo post-minero en Mieres (Asturias-España)”, en Ciudades, 22, pp. 99-122. DOI: https://doi.org/10.24197/ciudades.22.2019.99-122 Resumen: Mieres es uno de los centros que originaron al área metropolitana de Asturias. Creció con la primera industrialización y alcanzó su techo en 1970. La crisis de sus bases no ha sido equilibrada por la reestructuración del sistema, marcado por dos procesos que se retroalimentan: la desvitalización social y la descapitalización física; su acción conjunta configura la fase actual, de contracción urbana, para la que se prescribe una metodología de intervención, basada en la regeneración urbana integrada, de la que se concretan acciones de recualificación, financiadas con recursos obtenidos por un programa elaborado con esta misma perspectiva. Palabras clave: Ciudad minera, contracción urbana, desvitalización social, regeneración urbana integrada, diseño regional. Abstract: The city of Mieres is a urban component of the metropolitan area of Asturias. It grew up with the first industrialization, and reached its ceiling in 1970. -
Transcritical Pressure Organic Rankine Cycle (ORC) Analysis Based on the Integrated-Average Temperature Difference in Evaporators
Applied Thermal Engineering 88 (2015) 2e13 Contents lists available at ScienceDirect Applied Thermal Engineering journal homepage: www.elsevier.com/locate/apthermeng Research paper Transcritical pressure Organic Rankine Cycle (ORC) analysis based on the integrated-average temperature difference in evaporators * Chao Yu, Jinliang Xu , Yasong Sun The Beijing Key Laboratory of Multiphase Flow and Heat Transfer for Low Grade Energy Utilizations, North China Electric Power University, Beijing 102206, PR China article info abstract Article history: Integrated-average temperature difference (DTave) was proposed to connect with exergy destruction (Ieva) Received 24 June 2014 in heat exchangers. Theoretical expressions were developed for DTave and Ieva. Based on transcritical Received in revised form pressure ORCs, evaporators were theoretically studied regarding DTave. An exact linear relationship be- 12 October 2014 tween DT and I was identified. The increased specific heats versus temperatures for organic fluid Accepted 11 November 2014 ave eva protruded its TeQ curve to decrease DT . Meanwhile, the decreased specific heats concaved its TeQ Available online 20 November 2014 ave curve to raise DTave. Organic fluid in the evaporator undergoes a protruded TeQ curve and a concaved T eQ curve, interfaced at the pseudo-critical temperature point. Elongating the specific heat increment Keywords: fi Organic Rankine Cycle section and shortening the speci c heat decrease section improved the cycle performance. Thus, the fi Integrated-average temperature difference system thermal and exergy ef ciencies were increased by increasing critical temperatures for 25 organic Exergy destruction fluids. Wet fluids had larger thermal and exergy efficiencies than dry fluids, due to the fact that wet fluids Thermal match shortened the superheated vapor flow section in condensers. -
El Camino De San Salvador Por Mieres
El camino de San Salvador por Mieres Tramo Arroxo –El Padrún José Antonio Vega Álvarez Título: El Camino de Santiago a su paso por Mieres Textos: José Antonio Vega Álvarez Fotografías: José Luís Moratinos – Rozadas de La Peña Pedro Martínez Cruz - facebook. Mieres recuerdos José Antonio Vega Álvarez Editorial: HiFer Editor Impresión: HiFer Artes Gráficas - www.hifer.com ISBN: 978-84-17130-39-8 Dep. Legal: AS-00604-2018 www.elsastredeloslibros.es No está permitida la reproducción total o parcial de este libro, ni su tratamiento informático, ni la transmisión de ninguna forma o por cualquier medio, ya sea electrónico, mecánico, por fotocopia, por registro u otros métodos, ni su préstamo o alquiler o cualquiera otra forma de cesión de uso del ejemplar, sin permiso previo y por escrito del titular del Copyright. © El Copyright y todos los demás derechos son propiedad del autor y está debidamente registrado en el Registro General de la Propiedad Intelectual de Asturias. EL CAMINO DE SAN SALVADOR Tramo Arroxo - El Padrún Índice INTRODUCCIÓN ........................................................................................................................... 5 El peregrino ................................................................................................................................... 7 Mieres en el tiempo .................................................................................................................... 8 El camino de Santiago a su paso por el concejo ............................................................10 -
Rankine Cycle Definitions
Rankine Cycle Reading Problems 11.1 ! 11.7 11.29, 11.36, 11.43, 11.47, 11.52, 11.55, 11.58, 11.74 Definitions • working fluid is alternately vaporized and condensed as it recirculates in a closed cycle • the standard vapour cycle that excludes internal irreversibilities is called the Ideal Rankine Cycle Analyze the Process Device 1st Law Balance Boiler h2 + qH = h3 ) qH = h3 − h2 (in) Turbine h3 = h4 + wT ) wT = h3 − h4 (out) Condenser h4 = h1 + qL ) qL = h4 − h1 (out) Pump h1 + wP = h2 ) wP = h2 − h1 (in) 1 The Rankine efficiency is net work output ηR = heat supplied to the boiler (h − h ) + (h − h ) = 3 4 1 2 (h3 − h2) Effects of Boiler and Condenser Pressure We know the efficiency is proportional to T η / 1 − L TH The question is ! how do we increase efficiency ) TL # and/or TH ". 1. INCREASED BOILER PRESSURE: • an increase in boiler pressure results in a higher TH for the same TL, therefore η ". • but 40 has a lower quality than 4 – wetter steam at the turbine exhaust – results in cavitation of the turbine blades – η # plus " maintenance • quality should be > 80 − 90% at the turbine exhaust 2 2. LOWER TL: • we are generally limited by the T ER (lake, river, etc.) eg. lake @ 15 ◦C + ∆T = 10 ◦C = 25 ◦C | {z } resistance to HT ) Psat = 3:169 kP a. • this is why we have a condenser – the pressure at the exit of the turbine can be less than atmospheric pressure 3. INCREASED TH BY ADDING SUPERHEAT: • the average temperature at which heat is supplied in the boiler can be increased by superheating the steam – dry saturated steam from the boiler is passed through a second bank of smaller bore tubes within the boiler until the steam reaches the required temperature – The value of T H , the mean temperature at which heat is added, increases, while TL remains constant. -
Diagnóstico Ambiental Con El Formato De Una Matriz DAFO
integral Diagnóstico 1 INTRODUCCIÓN GENERAL ..................................................................... 3 Metodología de implantación de la Agenda 21 Local ................................... 6 Reuniones previas: ................................................................................................... 8 Aprobación del prediagnóstico:................................................................................. 8 Debate del Sistema Medioambiental Local: ............................................................... 9 Sesiones tutoriales y reuniones monográficas: ........................................................... 9 Diagnóstico Integral: .............................................................................................. 10 Plan de calidad ambiental: ...................................................................................... 11 Agenda 21 Local del municipio de Mieres ................................................. 12 Foro de Mieres: ...................................................................................................... 12 Secretaría técnica ................................................................................................... 13 Proceso de implantación ......................................................................................... 14 Situación actual ...................................................................................................... 14 II. PREDIAGNÓSTICO DE LA AGENDA 21 LOCAL DE MIERES ..... 15 III. SISTEMA MEDIOAMBIENTAL LOCAL -
Comparison of ORC Turbine and Stirling Engine to Produce Electricity from Gasified Poultry Waste
Sustainability 2014, 6, 5714-5729; doi:10.3390/su6095714 OPEN ACCESS sustainability ISSN 2071-1050 www.mdpi.com/journal/sustainability Article Comparison of ORC Turbine and Stirling Engine to Produce Electricity from Gasified Poultry Waste Franco Cotana 1,†, Antonio Messineo 2,†, Alessandro Petrozzi 1,†,*, Valentina Coccia 1, Gianluca Cavalaglio 1 and Andrea Aquino 1 1 CRB, Centro di Ricerca sulle Biomasse, Via Duranti sn, 06125 Perugia, Italy; E-Mails: [email protected] (F.C.); [email protected] (V.C.); [email protected] (G.C.); [email protected] (A.A.) 2 Università degli Studi di Enna “Kore” Cittadella Universitaria, 94100 Enna, Italy; E-Mail: [email protected] † These authors contributed equally to this work. * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel.: +39-075-585-3806; Fax: +39-075-515-3321. Received: 25 June 2014; in revised form: 5 August 2014 / Accepted: 12 August 2014 / Published: 28 August 2014 Abstract: The Biomass Research Centre, section of CIRIAF, has recently developed a biomass boiler (300 kW thermal powered), fed by the poultry manure collected in a nearby livestock. All the thermal requirements of the livestock will be covered by the heat produced by gas combustion in the gasifier boiler. Within the activities carried out by the research project ENERPOLL (Energy Valorization of Poultry Manure in a Thermal Power Plant), funded by the Italian Ministry of Agriculture and Forestry, this paper aims at studying an upgrade version of the existing thermal plant, investigating and analyzing the possible applications for electricity production recovering the exceeding thermal energy. A comparison of Organic Rankine Cycle turbines and Stirling engines, to produce electricity from gasified poultry waste, is proposed, evaluating technical and economic parameters, considering actual incentives on renewable produced electricity. -
Concejo De Ponga. Consultorio Local
10984 BOLETIN OFICIAL DEL PRINCIPADO DE ASTURIAS 16–VIII–2001 Zona Especial de Salud 6.1: Concejo de Ponga. Zona Básica de Salud VIII.2: La Felguera-Tuilla-Lada: Consultorio Local: S. Juan de Beleño. Comprende el territorio del concejo de Langreo formado por las parroquias de Lada, La Felguera y Tuilla. Limita: Zona Especial de Salud 6.2: Concejos de Cabrales, Peña- al Noroeste, con la Zona Básica de Salud VIII.1; al Suroeste, mellera Alta y Peñamellera Baja. con el concejo de Mieres del Camino; al Norte, con el concejo Consultorios Locales: Arenas de Cabrales, Carreñade de Siero, y al Este, por el río Nalón que la separa de la Cabrales, Alles (Peñamellera Alta) y Panes (Peñamellera Zona Básica de Salud VIII.3. Baja). Centro de Salud: La Felguera. Consultorios Periféricos: Tuilla y Lada. AREA VII Zona Básica de Salud VIII.3: Sama-Ciaño: Comprende Zona Básica de Salud VII.1: Mieres-Norte: Comprende el territorio del concejo de Langreo formado por las parro- el territorio del concejo de Mieres del Camino limitado al quias de Sama y Ciaño. Limita: al Noroeste, con la Zona Norte por los concejos de Ribera de Arriba y Oviedo; al Básica de Salud VIII.2; al Sur, con el concejo de Mieres Oeste, por el concejo de Morcín y la Zona Básica de Salud del Camino; al Oeste, con el concejo de San Martín del Rey VII.2; al Este, por el concejo de Langreo, y al Sur, por la Aurelio, y al Norte, con el concejo de Siero. calle Manuel Llaneza que la separa de la Zona Básica de Centro de Salud: Sama de Langreo. -
Rankine Cycle
MECH341: Thermodynamics of Engineering System Week 13 Chapter 10 Vapor & Combined Power Cycles The Carnot vapor cycle The Carnot cycle is the most efficient cycle operating between two specified temperature limits but it is not a suitable model for power cycles. Because: • Process 1-2 Limiting the heat transfer processes to two-phase systems severely limits the maximum temperature that can be used in the cycle (374°C for water) • Process 2-3 The turbine cannot handle steam with a high moisture content because of the impingement of liquid droplets on the turbine blades causing erosion and wear. • Process 4-1 It is not practical to design a compressor that handles two phases. The cycle in (b) is not suitable since it requires isentropic compression to extremely high pressures and isothermal heat transfer at variable pressures. 1-2 isothermal heat addition in a boiler 2-3 isentropic expansion in a turbine 3-4 isothermal heat rejection in a condenser 4-1 isentropic compression in a compressor T-s diagram of two Carnot vapor cycles. 1 Rankine cycle: The ideal cycle for vapor power cycles •Many of the impracticalities associated with the Carnot cycle can be eliminated by superheating the steam in the boiler and condensing it completely in the condenser. •The cycle that results is the Rankine cycle, which is the ideal cycle for vapor power plants. The ideal Rankine cycle does not involve any internal irreversibilities. Notes: • Only slight change in water temp through pump • The steam generator consists of boiler (two-phase heat transfer) and superheater • Turbine outlet is high-quality steam • Condenser is cooled by water (eg. -
Chapter 7 Vapor and Gas Power Systems
Chapter 7 Vapor and Gas Power Systems In this chapter, we will study the basic components of common industrial power and refrigeration systems. These systems are essentially thermodyanmic cycles in which a working fluid is alternatively vaporized and condensed as it flows through a set of four processes and returns to its initial state. We will use the first and second laws of thermodynamics to analyze the performance of ower and refrigeration cycles. 7.1 Rankine Cycle We can use a Rankine cycle to convert a fossil-fuel, nuclear, or solar power source into net electrical power. Figure 7.1-1a shows the components of a Rankine cycle and Figure 7.1-1b identifies the states of the Rankine cycle on a Ts diagram. Wt Turbine 1 2 Fuel QC air QH Rankine cycle Boiler 4 Condenser 3 Wp Pump Figure 7.1-1a The ideal Rankine cycle Figure 7.1-1b The path of an ideal Rankine cycle1 1 Moran, M. J. and Shapiro H. N., Fundamentals of Engineering Thermodynamics, Wiley, 2008, pg. 395 7-1 In the ideal Rankine cycle, the working fluid undergoes four reversible processes: Process 1-2: Isentropic expansion of the working fluid from the turbine from saturated vapor at state 1 or superheated vapor at state 1’ to the condenser pressure. Process 2-3: Heat transfer from the working fluid as it flows at constant pressure through the condenser with saturated liquid at state 3. Process 3-4: Isentropic compression in the pump to state 4 in the compressed liquid region. Process 4-1: Heat transfer to the working fluid as it flows at constant pressure through the boiler to complete the cycle. -
Organic Rankine Cycle Integration and Optimization for High Efficiency CHP Genset Systems
Organic Rankine Cycle Integration and Optimization for High Efficiency CHP Genset Systems Combined heat and power (CHP) systems Current Organic Rankine Cycle (ORC) systems operate at relatively low temperatures provide both electricity and heat for their and are used as a bottoming cycle waste heat recovery solution (top figure). The ORC host facilities. CHP systems have mostly system being developed can operate at higher temperatures and can thus be the saturated the large industrial facility primary recipient of the heat from a reciprocating engine (bottom figure). market, where economies of scale and the presence of needed technical staff make Photo credit ElectraTherm. the deployment of large systems greater than 20 megawatt (MW) electrical capacity a reciprocating engine to achieve total manufacturing sector analysis conducted cost effective and practical. There remains, CHP system efficiencies of 85% or more for the U.S. Department of Energy, however, substantial room for growth of at both its rated electrical capacity and at widespread deployment of flexible CHP smaller CHP systems suited for small and 50% capacity. To achieve this goal, the systems that are able to provide grid mid-size manufacturing facilities. system will be capable of operating in services could result in annual financial higher temperatures and pressures than benefits of approximately $1.4 billion In addition to manufacturing facility typical ORC systems. in the state of California alone. These energy benefits, the needs of the modern savings consist of lower industrial site electric grid are other potential drivers Benefits for Our Industry and energy costs, reduced grid operating costs, for further deployment of CHP systems. -
Boletín Oficial Del Principado De Asturias
BOLETÍN OFICIAL DEL PRINCIPADO DE ASTURIAS NÚM. 167 DE 19-VII-2018 1/32 IV. Administración Local AYUNTAMIENTOS DE MIERES EDICTO. Aprobación definitiva del I Plan de Infancia y Adolescencia de Mieres. Edicto Por Acuerdo Plenario adoptado en la sesión ordinaria celebrada el día 26 de abril de 2018 se aprobó inicialmente el I Plan de Infancia y Adolescencia de Mieres, publicándose anuncio del citado Acuerdo en el Boletín Oficial del Principado de Asturias de fecha 16 de mayo, a efectos de reclamaciones, durante el plazo de 30 días; transcurrido el mencionado plazo sin haberse presentado reclamaciones o sugerencias, se entiende aprobado el mismo de forma definitiva. Asimismo y en cumplimiento del citado acuerdo, se procede a la publicación íntegra del referido plan. I PLAN DE INFANCIA Y ADOLESCENCIA DE MIERES 1.—Personas y entidades que han colaborado en la elaboración del plan de infancia. Agradecimiento a las personas e instituciones que participaron en la elaboración del plan de infancia Mayores de 18 años. A todo el personal de UNICEF y el Observatorio de Infancia del Principado, de centros y dependencias municipales, porque de una forma directa o indirecta colaboraron en la realización de este Plan. Menores de 18 años. A todos los niños y niñas de Mieres que han colaborado con el Ayuntamiento nada más lanzarles la idea de lo que se pretendía hacer con este Plan, siendo ellos los verdaderos protagonistas. Grupo de trabajo coordinador del Plan. — Itziar Vicente Llaneza Concejala de Juventud del Ayuntamiento de Mieres. — M.ª de las Mercedes Castañón Pereda Coordinadora técnica de Plan de Infancia del Ayuntamiento de Mieres. -
Review of Experimental Research on Supercritical and Transcritical Thermodynamic Cycles Designed for Heat Recovery Application
CORE Metadata, citation and similar papers at core.ac.uk Provided by Ghent University Academic Bibliography applied sciences Review Review of Experimental Research on Supercritical and Transcritical Thermodynamic Cycles Designed for Heat Recovery Application Steven Lecompte 1,2,* , Erika Ntavou 3, Bertrand Tchanche 4, George Kosmadakis 5 , Aditya Pillai 1,2 , Dimitris Manolakos 6 and Michel De Paepe 1,2 1 Department of Flow, Heat and Combustion Mechanics, Ghent University–UGent, Sint-Pietersnieuwstraat 41, 9000 Gent, Belgium; [email protected] (A.P.); [email protected] (M.D.P.) 2 Flanders Make, the Strategic Research Centre for the Manufacturing Industry, 3920 Lommel, Belgium 3 Department of Natural Resources and Agricultural Engineering, Agricultural University of Athens, Iera Odos 75, 11855 Athens, Greece; [email protected] 4 Department of Physics, Université Alioune Diop de Bambey, P.O. Box 30 Bambey, Senegal; [email protected] 5 Laboratory of Thermal Hydraulics and Multiphase Flow, INRASTES, National Center for Scientific Research “Demokritos”, Patriarchou Grigoriou and Neapoleos 27, 15341 Agia Paraskevi, Greece; [email protected] 6 Department of Natural Resources and Agricultural Engineering, Agricultural University of Athens, Iera Odos 75, 11855 Athens, Greece; [email protected] * Correspondence: [email protected]; Tel.: +32-470045524 Received: 21 May 2019; Accepted: 17 June 2019; Published: 25 June 2019 Abstract: Supercritical operation is considered a main technique to achieve higher cycle efficiency in various thermodynamic systems. The present paper is a review of experimental investigations on supercritical operation considering both heat-to-upgraded heat and heat-to-power systems. Experimental works are reported and subsequently analyzed.