Дисертації з теми "Circulating fluidized bed boiler"
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Karppanen, E. (Erkki). "Advanced control of an industrial circulating fluidized bed boiler using fuzzy logic." Doctoral thesis, University of Oulu, 2000. http://urn.fi/urn:isbn:9514255194.
Повний текст джерелаNiva, L. (Laura). "Self-optimizing control of oxy-combustion in circulating fluidized bed boilers." Doctoral thesis, Oulun yliopisto, 2018. http://urn.fi/urn:isbn:9789526221304.
Повний текст джерелаTiivistelmä Energiantuotanto polttovoimalaitoksissa on merkittävä hiilidioksidipäästöjen lähde. Kansainväliset ilmastotavoitteet edellyttävät kaikkien käytettävissä olevien teknologioiden hyödyntämistä päästövähennysten aikaansaamiseksi nopeasti ja kustannustehokkaasti. Hiilidioksidin talteenotto on yksi mahdollisista teknisistä ratkaisuista polttovoimalaitoksissa. Kiertoleijukattilat ovat saavuttaneet kasvavaa suosiota etuinaan hyvä käytettävyys, tehokas päästöjen hallinta, soveltuvuus erilaisten haastavienkin polttoaineiden hyödyntämiseen ja mahdollisuus tehokkaiden höyrykiertojen käyttöön. Uudessa happipolttoprosessissa palamisilma korvataan hapen ja kierrätetyn savukaasun seoksella, mikä mahdollistaa hiilidioksidin talteenoton savukaasuista. Kiertoleijupolton säädön kannalta vapausasteet lisääntyvät, sillä leijutukseen ja polttamiseen käytettävän kaasun määrää ja koostumusta voidaan säätää erikseen. Väitöstutkimuksessa käytettiin itseoptimoivaa säätöä kiertoleijukattilan säätörakenteiden suunnitteluun. Itseoptimoiva säätö tarjoaa systemaattisen menetelmän säätösuunnittelun alkuvaiheeseen, jossa päätöksenteko on perinteisesti tehty esimerkiksi intuition, heuristiikan ja aiempien ratkaisujen perusteella. Menetelmän tavoitteena on löytää säädettävät muuttujat, joiden asetusarvot eivät vaadi jatkuvaa optimointia, vaikka prosessiin vaikuttavat erilaiset häiriöt ja mittausvirheet. Väitöstutkimuksen tulokset osoittavat, että itseoptimoiva säätö soveltuu kiertoleijupolton säätörakenteiden suunnitteluun. Erilaisten säätörakenteiden toimivuutta arvioitiin käyttäen validoidun prosessimallin tasapainotilan approksimaatioita. Uudelle happipolttoprosessille löydettiin lupaavia säätörakenteita, joiden toimintaa voitiin demonstroida myös dynaamisesti
Biruk, David D. "Neural Network Based Control of Integrated Recycle Heat Exchanger Superheaters in Circulating Fluidized Bed Boilers." UNF Digital Commons, 2013. http://digitalcommons.unf.edu/etd/470.
Повний текст джерелаFusey, Isabelle. "A novel circulating fluidized bed." Thesis, University of British Columbia, 1985. http://hdl.handle.net/2429/25094.
Повний текст джерелаApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Huang, Yue. "Dynamic model of circulating fluidized bed." Morgantown, W. Va. : [West Virginia University Libraries], 2006. https://eidr.wvu.edu/etd/documentdata.eTD?documentid=4823.
Повний текст джерелаTitle from document title page. Document formatted into pages; contains ix, 133 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 103-114).
Gogebakan, Yusuf. "Simulation Of Circulating Fluidized Bed Combustors." Phd thesis, METU, 2006. http://etd.lib.metu.edu.tr/upload/2/12607775/index.pdf.
Повний текст джерелаwhereas outputs include transient values of combustor temperatures, gas concentrations, char and inert hold-ups and their size distributions. The solution procedure employs method of lines approach for the governing non-linear partial differential equations and combined bisection and secant rule for non-linear algebraic equations. The initial conditions required for the model are provided from the simultaneous solution of governing equations of dynamic model with all temporal derivatives set to zero. By setting all temporal derivatives to zero, model can also be utilized for steady state performance prediction. In order to assess the validity and predictive accuracy of the model, it was applied to the prediction of the steady state behavior of Technical University of Nova Scotia 0.3 MWt CFBC Test Rig and predictions were compared with measurements taken on the same rig. Comparison of model predictions at steady state conditions revealed that the predictions of the model are physically correct and agree well with the measurements and the model is successful in qualitatively and quantitatively simulating the processes taking place in a circulating fluidized bed combustor.
Courbariaux, Yann. "Heat transfer in a circulating fluidized bed." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0006/MQ46243.pdf.
Повний текст джерелаRedemann, Kai. "Ash management in circulating fluidized bed combustors." Aachen Shaker, 2008. http://d-nb.info/991096231/04.
Повний текст джерелаWu, Richard Lap. "Heat transfer in circulating fluidized beds." Thesis, University of British Columbia, 1989. http://hdl.handle.net/2429/31037.
Повний текст джерелаApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Herbert, Peter M. "Hydrodynamic study of a downflow circulating fluidized bed." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0005/NQ32310.pdf.
Повний текст джерелаMoran, James C. (James Christopher). "Gas phase hydrodynamics inside a circulating fluidized bed." Thesis, Massachusetts Institute of Technology, 2001. http://hdl.handle.net/1721.1/89304.
Повний текст джерелаIncludes bibliographical references (p. 165-171).
Circulating Fluidized Beds (CFB's) offer many advantages over traditional pulverized coal burners in the power generation industry. They operate at lower temperatures, have better environmental emissions and better fuel flexibility. The motion of solids inside a CFB has been studied extensively over the previous twenty years. However the motion of gas is less well understood. There has previously only been indirect measurements of gas velocities and fluctuations. The gas phase is important as the motion of the particles is controlled by the gas. Accurate simulations of CFB's are not possible without accurate information on the gas phase. Instrumentation was developed for use in measuring gas phase fluctuations inside a scale model CFB. Results were unexpected in that gas fluctuations were substantially larger than expected. The fluctuation level without particle flow was around 0.15m/s. This was expected to stay constant or decrease with the introduction of particles. However with particle introduction the fluctuation level increased to 0.7m/s, an increase of over 400%. This is more than likely due to the clustering of particles which produces large scale structures with the resulting vortex shedding. A smaller riser was built which allowed the introduction of single individual clusters into the unit. The effect of single clusters on the surrounding gas flow was studied and modeled. These results indicate a mechanism by which, previously unknown, large scale fluctuations are generated inside a CFB.
by James C. Moran.
Ph.D.
Wischnewski, Reiner. "Simulation of large-scale circulating fluidized bed combustors." Aachen Shaker, 2008. http://d-nb.info/993341691/04.
Повний текст джерелаOzkan, Mert. "Simulation Of Circulating Fluidized Bed Combustors Firing Indigenous Lignite." Master's thesis, METU, 2010. http://etd.lib.metu.edu.tr/upload/12612686/index.pdf.
Повний текст джерелаStewart, Michael C. "Sulfation Phenomena Under Oxy-Fuel Circulating Fluidized Bed Conditions." Thèse, Université d'Ottawa / University of Ottawa, 2011. http://hdl.handle.net/10393/20024.
Повний текст джерелаLa combustion avec de l’oxygène pur (i.e., oxy-combustible) en lit fluidisé circulant (LFC) permet de produire de l'électricité tout en réduisant les émissions anthropiques de CO2 ainsi que le précurseur des pluies acides, du SO2, en utilisant du calcaire de façon in-situ. Bien que la technologie existe depuis 30 ans, il a récemment pris de l'attention avec l’opération de quelques unités à l'échelle pilote dans le monde. La combustion avec de l’oxygène pur est en grande partie semblable à la combustion standard avec de l’air, mais diffère sur quelques points clés, dont l'un est les concentrations élevées de CO2 et H2O (jusqu'à 90% et 30%, respectivement). Les effets et le mécanisme d'action de ces gaz sur la sulfatation du calcaire ont longtemps été un sujet de débat dans la littérature. A l’aide d'un analyseur thermogravimétrique (ATG) et un four tubulaire (FT), les effets de concentrations élevées de gaz sur la sulfatation du calcaire sont étudiées en utilisant des gaz d’échappement typiques de la combustion à l’air et à l’oxygène pur (SO2: 3800 ppm, CO2: de 12,5 à 82,5% , O2: 2,5%, H2O: 0 à 30%) à 850 ° C. Une explication est fournie pour les résultats contradictoires dans la littérature en termes de résultats obtenues avec les ATG/FT. Une analyse microstructurale des échantillons sulfatés utilisant la microscopie électronique à balayage (MEB), l'analyse d'adsorption d'azote et la pycnométrie d'hélium est utilisée pour soutenir un mécanisme basé sur la diffusion à l'état solide. D'autres expériences dans le FT sont utilisées pour élucider les effets et le mécanisme d'action de H2O et CO2 sur l'agglomération des particules de calcaire au cours de la sulfatation dans des conditions d'oxy-combustible. Enfin, en utilisant un LFC à l’échelle pilote, les observations des expériences en laboratoire ont été testés dans un environnement réaliste de combustion. Les effets de concentrations élevées de CO2 et H2O associés à la combustion oxycombustible du coke de pétrole sur la formation catalytique de NOx sur du calcaire sont discutés et reliés au mécanisme proposé de H2O et CO2 sur la sulfatation.
Burkell, James J. "Solids circulation rate measurement in a circulating fluidized bed." Thesis, University of British Columbia, 1986. http://hdl.handle.net/2429/26217.
Повний текст джерелаApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Zheng, Ying. "Flow structure in a liquid-solids circulating fluidized bed." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0013/NQ42560.pdf.
Повний текст джерелаSajjakulnukit, Boonrod. "Hydrodynamics and heat transfer in a circulating fluidized bed." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0018/NQ46298.pdf.
Повний текст джерелаRedemann, Kai [Verfasser]. "Ash Management in Circulating Fluidized Bed Combustors / Kai Redemann." Aachen : Shaker, 2008. http://d-nb.info/1161313621/34.
Повний текст джерелаAlmond, Robert R. "Small particle separation in a circulating fluidized bed riser system." Morgantown, W. Va. : [West Virginia University Libraries], 2005. https://eidr.wvu.edu/etd/documentdata.eTD?documentid=4342.
Повний текст джерелаTitle from document title page. Document formatted into pages; contains xiii, 104 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 86-87).
Gupta, Suneel Krishan. "Modeling the hydrodynamics of large-scale circulating fluidized bed risers." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0025/MQ31388.pdf.
Повний текст джерелаPuchyr, David Michael John. "A predictive model for a circulating fluidized bed riser reactor." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0030/NQ38498.pdf.
Повний текст джерелаWischnewski, Reiner [Verfasser]. "Simulation of Large-Scale Circulating Fluidized Bed Combustors / Reiner Wischnewski." Aachen : Shaker, 2009. http://d-nb.info/1126378720/34.
Повний текст джерелаBischi, Aldo. "Chemical Looping Reactor System Design : Double Loop Circulating Fluidized Bed (DLCFB)." Doctoral thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-16972.
Повний текст джерелаBoyd, David Anthony. "Internally circulating fluidized bed membrane reactor for high-purity hydrogen production." Thesis, University of British Columbia, 2007. http://hdl.handle.net/2429/30745.
Повний текст джерелаApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Cruz, Torres Elizabet Ananay. "Modelling of a circulating fluidized bed using computational fluid dynamics software." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0007/MQ46244.pdf.
Повний текст джерелаPanday, Rupendranath. "Modeling, identification and control of a cold flow circulating fluidized bed." Morgantown, W. Va. : [West Virginia University Libraries], 2008. https://eidr.wvu.edu/etd/documentdata.eTD?documentid=5833.
Повний текст джерелаTitle from document title page. Document formatted into pages; contains xiii, 99 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 94-99).
Hensler, Timo [Verfasser]. "Fluid Dynamic Characterization of Circulating Fluidized Bed Riser Reactors / Timo Hensler." München : Verlag Dr. Hut, 2020. http://d-nb.info/1219474754/34.
Повний текст джерелаGoldblatt, William M. "Electromagnetic induction sensing of individual tracer particles in a circulating fluidized bed." Thesis, University of British Columbia, 1990. http://hdl.handle.net/2429/30918.
Повний текст джерелаApplied Science, Faculty of
Chemical and Biological Engineering, Department of
Graduate
Ma, Ying L. "Heat transfer studies in a gas-solids downflow circulating fluidized bed, downer." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0003/MQ30689.pdf.
Повний текст джерелаHassan, Mohamed. "Modelling and simulation of biomass gasification in a circulating fluidized bed reactor." Thesis, Aston University, 2013. http://publications.aston.ac.uk/20858/.
Повний текст джерелаValmari, Tuomas. "Potassium behaviour during combustion of wood in circulating fluidised bed power plants /." Espoo [Finland] : Technical Research Centre of Finland, 2000. http://www.vtt.fi/inf/pdf/publications/2000/P414.pdf.
Повний текст джерелаPetersen, Inga [Verfasser]. "Sewage Sludge Gasification in the Circulating Fluidized Bed : Experiments and Modeling / Inga Petersen." Aachen : Shaker, 2004. http://d-nb.info/1172612110/34.
Повний текст джерелаNoymer, Peter Daniel. "Heat transfer by particle convection at the wall of a circulating fluidized-bed." Thesis, Massachusetts Institute of Technology, 1997. http://hdl.handle.net/1721.1/10435.
Повний текст джерелаRatschow, Lars. "Three-dimensional simulation of temperature distributions in large scale circulating fluidized bed combustors." Aachen Shaker, 2009. http://d-nb.info/99450196X/04.
Повний текст джерелаSarra, Angela M. "Particle-wall shear stress measurements within the standpipe of a circulating fluidized bed." Morgantown, W. Va. : [West Virginia University Libraries], 2001. http://etd.wvu.edu/templates/showETD.cfm?recnum=2078.
Повний текст джерелаTitle from document title page. Document formatted into pages; contains xi, 137 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 136-137).
Johansson, William. "Experimental Study to Reduce CO Emissions in Skellefteå Kraft's 16 MW Bubbling Fluidized Bed Boiler." Thesis, Luleå tekniska universitet, Institutionen för teknikvetenskap och matematik, 2019. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-74398.
Повний текст джерелаDe, Fonseca Pimentel Vittoria. "Technical comparison and economic evaluations of moving grate and circulating fluidized bed combustion technologies." Master's thesis, Alma Mater Studiorum - Università di Bologna, 2019.
Знайти повний текст джерелаWang, Yi-Ning. "CFD investigation of gas-solid flow dynamics in monolithic micro-circulating fluidized bed reactors." Thesis, Université Laval, 2008. http://www.theses.ulaval.ca/2008/25760/25760.pdf.
Повний текст джерелаSalvaterra, Antonio de Barros R. L. A. "Hydrodynamics of gas-solid suspension in a circulating fluidized bed riser : a comparative study." Thesis, Heriot-Watt University, 2003. http://hdl.handle.net/10399/418.
Повний текст джерелаTan, Richard Hing-Fung. "Experimental simulation of the hydrodynamics of dissimilar solids in a pressurized circulating fluidized bed." Thesis, Massachusetts Institute of Technology, 1997. http://hdl.handle.net/1721.1/10483.
Повний текст джерелаMahmoudi, Shiva. "The circulating fluidized bed (CFB) combustion of biomass and the control of gaseous emissions." Thesis, University of Warwick, 2011. http://wrap.warwick.ac.uk/45425/.
Повний текст джерелаWang, Yining. "CFD investigation of gas-solid flow dynamics in monolithic micro-circulating fluidized bed reactors." Master's thesis, Université Laval, 2008. http://hdl.handle.net/20.500.11794/20312.
Повний текст джерелаMcIntyre, Christopher. "CPFD Modeling of a Novel Internally Circulating Bubbling Fluidized Bed for Chemical Looping Combustion." Thesis, Université d'Ottawa / University of Ottawa, 2021. http://hdl.handle.net/10393/42054.
Повний текст джерелаPugalia, Neeraj. "Numerical modeling of cold flow and hot gas desulfurization in a circulating fluidized bed." Morgantown, W. Va. : [West Virginia University Libraries], 2001. http://etd.wvu.edu/templates/showETD.cfm?recnum=2056.
Повний текст джерелаTitle from document title page. Document formatted into pages; contains xvi, 119 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 103-106).
Seachman, Steven M. "Application of a reflective optical probe to measure solids fractions in a circulating fluidized bed." Morgantown, W. Va. : [West Virginia University Libraries], 2007. https://eidr.wvu.edu/etd/documentdata.eTD?documentid=4988.
Повний текст джерелаTitle from document title page. Document formatted into pages; contains xiii, 97 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 72-74).
Batu, Aykan. "Investigation Of Combustion Characteristics Of Indigenous Lignite In A 150 Kwt Circulating Fluidized Bed Combustor." Phd thesis, METU, 2008. http://etd.lib.metu.edu.tr/upload/12609432/index.pdf.
Повний текст джерелаFluidized Bed Combustion&rsquo
technology. Applications of circulating fluidized bed combustion (CFB) technology have been steadily increasing in both capacity and number over the past decade for the utilization of this resource. Designs of these units have been based on the combustion tests carried out in pilot scale facilities to determine the combustion and desulfurization characteristics of the coals and limestones in CFB conditions. However, utilization of Turkish lignites with high ash, volatile matter and sulfur contents in CFB boilers necessitates adaptation of CFB combustion technology to these resources. Therefore, it has been the objective of this study to investigate combustion characteristics of an indigenous lignite in a circulating fluidized bed combustor. In this study, a 150 kWt Circulating Fluidized Bed (CFB) Combustor Test Unit was designed and constructed in Chemical Engineering Department of Middle East Technical University, based on the extensive experience acquired at the existing 0.3 MWt Bubbling Atmospheric Fluidized Bed Combustor (AFBC) Test Rig. Following the commissioning tests, combustion tests were carried out for investigation of combustion characteristics of Ç
an lignite in CFB conditions and for comparison of the design of the test unit with experimental findings. The steady state results of the combustion tests reveal that Ç
an lignite is fired with high combustion efficiency. Temperature profile along the riser is achieved to be almost uniform by good control of cooling system. Pressure drop through the dilute zone is found to be negligible because of low solid hold up in this zone. CO and NO concentrations within the flue gas are fairly lower, whereas N2O concentration is higher compared to the ones obtained in the bubbling AFBC test rig firing the same lignite. The deviation of particle size distributions of bottom ash and circulating ash among the tests are in line with the deviation of superficial velocity. In order to assess the validity and predictive accuracy of the pressure balance model, it was reapplied to the test unit utilyzing the revised input data based on the results of the combustion tests. Comparison of the model predictions with experimental results revealed that the predictions have acceptable agreement with the measurements. In conclusion, the performance of 150 kW CFBC Test Unit was found to be satisfactory to be utilized for the long term research studies on combustion and desulfurization characteristics of indigenous lignite reserves in circulating fluidized bed combustors.
Chevrier, Solène. "Development of subgrid models for a periodic circulating fluidized bed of binary mixture of particles." Phd thesis, Toulouse, INPT, 2017. http://oatao.univ-toulouse.fr/19905/1/CHEVRIER_Solene.pdf.
Повний текст джерелаRatschow, Lars [Verfasser]. "Three-Dimensional Simulation of Temperature Distributions in Large-Scale Circulating Fluidized Bed Combustors / Lars Ratschow." Aachen : Shaker, 2009. http://d-nb.info/1156518016/34.
Повний текст джерелаEbert, Todd Alan. "An experimental investigation of particle and gas convection heat transfer in a circulating fluidized bed." Thesis, Massachusetts Institute of Technology, 1991. http://hdl.handle.net/1721.1/13833.
Повний текст джерелаLan, Qingdao. "Development of a continuous ion exchange system for protein recovery using liquid-solid circulating fluidized bed." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2001. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp04/NQ58401.pdf.
Повний текст джерела