Dissertations / Theses on the topic 'Industrial Furnace'
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Ellul, Connie. "Flameless Combustion for Industrial Furnace Heaters." Thesis, University of Leeds, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.505069.
Full textCarlborg, Hampus, and Henrik Iredahl. "Modeling and Temperature Control of an Industrial Furnace." Thesis, Linköpings universitet, Reglerteknik, 2016. http://urn.kb.se/resolve?urn=urn:nbn:se:liu:diva-129617.
Full textHixson, Scott. "Rapid industrial furnace thermal modeling for improved fuel efficiency." Diss., Columbia, Mo. : University of Missouri-Columbia, 2007. http://hdl.handle.net/10355/5091.
Full textThe entire dissertation/thesis text is included in the research.pdf file; the official abstract appears in the short.pdf file (which also appears in the research.pdf); a non-technical general description, or public abstract, appears in the public.pdf file. Title from title screen of research.pdf file (viewed on April 9, 2009) Includes bibliographical references.
Middleton, Kenneth George. "The failure of graphite arc-furnace electrodes." Thesis, Durham University, 1985. http://etheses.dur.ac.uk/7050/.
Full textCorreia, Sara Alexandra Chanoca. "Development of improved mathematical models for the design and control of gas-fired furnaces." Thesis, University of South Wales, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.369080.
Full textBlanden, Zachary F. "Process development for high powered amplifier Au/Sn eutectic die attach via vacuum furnace." Thesis, State University of New York at Binghamton, 2017. http://pqdtopen.proquest.com/#viewpdf?dispub=10250174.
Full textThis research was conducted to develop and qualify a vacuum GaAs semiconductor monolithic microwave integrated circuit die attach process. Research was done to understand the causes and effects of voiding levels on device performance and reliability. Simultaneous investigation was done to qualify vacuum-attach as a successful methodology by which minimal voiding levels were achieved. After an initial vacuum-attach trial was completed to verify the methodology, internal accept/reject criteria were developed to qualify die attach interfaces. A dual phase attachment methodology was created to minimize tolerance stacking resulting in more consistent component placement. MATLAB image processing code was developed to quantify the voiding levels against the accept/reject criteria. Statistical methodologies were employed to troubleshoot root causes for special cause variation of initial attachment failures. A design of experiment was conducted testing three factors each at two levels (process gas [Gas A, Gas B], leaking chamber [yes, no], and carrier supplier [Supplier A, Supplier B]). The DOE identified process gas and its interaction with the carrier supplier to be significant. Further investigation of the carriers identified plating contamination, resulting in the process gas the primary factor of interest. A secondary experiment focusing on process gas identified no statistical difference between Gas A? and Gas B (Gas A? indicating a high purity form of Gas A). With this information, Gas A? was selected as the process gas. A total of 56 attachment interfaces were then produced yielding 0.7485% voiding, on average, following a Weibull distribution (?= 1.04171, ? = 0.75967) with zero rejections. The process?s consistency of minimal voiding levels were deemed a success and the process was released to production.
Hougen, Krysta E. "Long-term Effects of Industrial History on the Forest Flora of Southeastern Ohio." Ohio University / OhioLINK, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1237857409.
Full textBorges, Cláudio Neves. "Modelagem matemática do processo industrial de coqueamento retardado." Universidade de São Paulo, 2016. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-29062016-162519/.
Full textThe delayed coke unit is a thermal conversion process, used by the crude oil refineries, to convert residual feedstocks into products of low molecular weight and high aggregated value (gases, naphtha and gasoil) and green coke. A small increase in the net yield in the delayed coke unit results in considerable economic benefits, particularly in the liquid distillates. The market competition, the restrictions on the product specifications and the operational bottlenecks require a better production planning. Therefore, the development of new strategies and mathematical models, focused in better industrial process operating conditions and product formulations, is essential to achieve better yields and a more precise product quality monitoring. The objective of this work is the development of a furnace-reactor mathematical model of the delayed coke process based on industrial plant information. The proposed model is based on the feed and product characterization as pseudo components, group kinetical models and liquid-vapor equilibrium. Furthermore, the main challenges to develop the furnace and reactor mathematical model are discussed, as well as the vacuum residual and the coke unit products rigorous characterization to determine the parameters that impact the coke morphology and the reaction zone inside the coke reactor.
Stadler, Johan George. "Multi-objective optimisation using the cross-entropy method in CO gas management at a South African ilmenite smelter." Thesis, Stellenbosch : Stellenbosch University, 2012. http://hdl.handle.net/10019.1/71631.
Full textENGLISH ABSTRACT: In a minerals processing environment, stable production processes, cost minimisation and energy efficiency are key to operational excellence, safety and profitability. At an ilmenite smelter, typically found in the heavy minerals industry, it is no different. Management of an ilmenite smelting process is a complex, multi-variable challenge with high costs and safety risks at stake. A by-product of ilmenite smelting is superheated carbon monoxide (CO) gas, or furnace off-gas. This gas is inflammable and extremely poisonous to humans. At the same time the gas is a potential energy source for various on-site heating applications. Re-using furnace off-gas can increase the energy efficiency of the energy intensive smelting process and can save on the cost of procuring other gas for heating purposes. In this research project, the management of CO gas from the Tronox KZN Sands ilmenite smelter in South Africa was studied with the aim of optimising the current utilisation of the gas. In the absence of any buffer capacity in the form of a pressure vessel, the stability of the available CO gas is directly dependent on the stability of the furnaces. The CO gas has been identified as a partial replacement for methane gas which is currently purchased for drying and heating of feed material and pre-heating of certain smelter equipment. With no buffer capacity between the furnaces and the gas consuming plants, a dynamic prioritisation approach had to be found if the CO was to replace the methane. The dynamics of this supply-demand problem, which has been termed the “CO gas problem”, needed to be studied. A discrete-event simulation model was developed to match the variable supply of CO gas to the variable demand for gas over time – the demand being a function of the availability of the plants requesting the gas, and the feed rates and types of feed material processed at those plants. The problem was formulated as a multi-objective optimisation problem with the two main, conflicting objectives, identified as: 1) the average production time lost per plant per day due to CO-methane switchovers; and 2) the average monthly saving on methane gas costs due to lower consumption thereof. A metaheuristic, namely multi-objective optimisation using the cross-entropy method, or MOO CEM, was applied as optimisation algorithm to solve the CO gas problem. The performance of the MOO CEM algorithm was compared with that of a recognised benchmark algorithm for multi-objective optimisation, the NSGA II, when both were applied to the CO gas problem. The background of multi-objective optimisation, metaheuristics and the usage of furnace off-gas, particularly CO gas, were investigated in the literature review. The simulation model was then developed and the optimisation algorithm applied. The research aimed to comment on the merit of the MOO CEM algorithm for solving the dynamic, stochastic CO gas problem and on the algorithm’s performance compared to the benchmark algorithm. The results served as a basis for recommendations to Tronox KZN Sands in order to implement a project to optimise usage and management of the CO gas.
AFRIKAANSE OPSOMMING: In mineraalprosessering is stabiele produksieprosesse, kostebeperking en energie-effektiwiteit sleuteldrywers tot bedryfsprestasie, veiligheid en wins. ‘n Ilmenietsmelter, tipies aangetref in swaarmineraleprosessering, is geen uitsondering nie. Die bestuur van ‘n ilmenietsmelter is ‘n komplekse, multi-doelwit uitdaging waar hoë kostes en veiligheidsrisiko’s ter sprake is. ‘n Neweproduk van die ilmenietsmeltproses is superverhitte koolstofmonoksiedgas (CO gas). Hierdie gas is ontvlambaar en uiters giftig vir die mens. Terselfdertyd kan hierdie gas benut word as energiebron vir allerlei verhittingstoepassings. Die herbenutting van CO gas vanaf die smelter kan die energie-effektiwiteit van die energie-intensiewe smeltproses verhoog en kan verder kostes bespaar op die aankoop van ‘n ander gas vir verhittingsdoeleindes. In hierdie navorsingsprojek is die bestuur van die CO gasstroom wat deur die ilmenietsmelter van Tronox KZN Sands in Suid-Afrika geproduseer word, ondersoek met die doel om die huidige benuttingsvlak daarvan te verbeter. Weens die afwesigheid van enige bufferkapasiteit in die vorm van ‘n drukbestande tenk, is die stabiliteit van CO gas beskikbaar vir hergebruik direk afhanklik van die stabiliteit van die twee hoogoonde wat die gas produseer. Die CO gas kan gedeeltelik metaangas, wat tans aangekoop word vir die droog en verhitting van voermateriaal en vir die voorverhitting van sekere smeltertoerusting, vervang. Met geen bufferkapasiteit tussen die hoogoonde en die aanlegte waar die gas verbruik word nie, was die ondersoek van ‘n dinamiese prioritiseringsbenadering nodig om te kon vasstel of die CO die metaangas kon vervang. Die dinamika van hierdie vraag-aanbod probleem, getiteld die “CO gasprobleem”, moes bestudeer word. ‘n Diskrete-element simulasiemodel is ontwikkel as probleemoplossingshulpmiddel om die vraag-aanbodproses te modelleer en die prioritiseringsbenadering te ondersoek. Die doel van die model was om oor tyd die veranderlike hoeveelhede van geproduseerde CO teenoor die veranderlike gasaanvraag te vergelyk. Die vlak van gasaanvraag is afhanklik van die beskikbaarheidsvlak van die aanlegte waar die gas verbruik word, sowel as die voertempo’s en tipes voermateriaal in laasgenoemde aanlegte. Die probleem is geformuleer as ‘n multi-doelwit optimeringsprobleem met twee hoof, teenstrydige doelwitte: 1) die gemiddelde verlies aan produksietyd per aanleg per dag weens oorgeskakelings tussen CO en metaangas; 2) die gemiddelde maandelikse besparing op metaangaskoste weens laer verbruik van dié gas. ‘n Metaheuristiek, genaamd MOO CEM (multi-objective optimisation using the cross-entropy method), is ingespan as optimeringsalgoritme om die CO gasprobleem op te los. Die prestasie van die MOO CEM algoritme is vergelyk met dié van ‘n algemeen aanvaarde riglynalgoritme, die NSGA II, met beide toepas op die CO gasprobleem. The agtergrond van multi-doelwit optimering, metaheuristieke en die benutting van hoogoond af-gas, spesifiek CO gas, is ondersoek in die literatuurstudie. Die simulasiemodel is daarna ontwikkel en die optimeringsalgoritme is toegepas.
Suopajärvi, H. (Hannu). "Bioreducer use in blast furnace ironmaking in Finland:techno-economic assessment and CO₂ emission reduction potential." Doctoral thesis, Oulun yliopisto, 2015. http://urn.fi/urn:isbn:9789526207063.
Full textTiivistelmä Suurin osa maailmassa tuotetusta teräksestä valmistetaan integroidulla masuuni-konvertteri reitillä, joka perustuu neitseellisten raaka-aineiden käyttöön. Masuuniprosessissa käytetään suuri määrä fossiilisia, lähinnä hiilipohjaisia pelkistimiä, jotka aiheuttavat hiilidioksidipäästöjä ilmakehään. Fossiilisia hiilidioksidipäästöjä voidaan teräksenvalmistuksessa vähentää uusilla teknologioilla tai siirtymällä uusiutumattomista energialähteistä uusiutuviin. Biomassasta valmistetut pelkistimet voisivat olla yksi mahdollinen keino alentaa masuunipohjaisen teräksenvalmistuksen ominaispäästöjä. Tämän työn tavoitteena oli tarkastella biopelkistimien käytön teknistaloudellista potentiaalia masuunikäytössä ja aikaansaatavia hiilidioksidipäästövähenemiä eri systeemirajauksilla. Työssä keskityttiin tarkastelemaan biopelkistimien hyödynnettävyyttä lähinnä Suomen tasolla, vaikka käytetyt tutkimusmetodit ovat sovellettavissa myös laajemmin. Työssä arvioitiin biopelkistimien metallurgisia ominaisuuksia, niiden vaikutusta masuuniprosessiin ja laajemmin muihin terästehtaan prosesseihin, pääpainon ollessa saavutettavan CO₂ päästövähenemän tarkastelussa. Työssä tarkasteltiin biopelkistimien valmistuksen CO₂ päästöjä, energiankulutusta ja tuotantokustannuksia sekä energiapuun saatavuutta biopelkistimien tuotantoon. Tulokset osoittavat, että biomassasta voidaan valmistaa kiinteitä, nestemäisiä ja kaasumaisia pelkistimiä termokemiallisilla konversioteknologioilla, joiden soveltuvuus masuunikäyttöön vaihtelee suuresti. Masuuniprosessissa suurin fossiilisten pelkistimien korvaavuus saavutetaan käyttämällä puuhiili-injektiota. Torrefioidun puun, puuhiilen ja Bio-SNG:n hiilijalanjälki on varsin maltillinen verrattuna fossiilisiin pelkistimiin ja niiden tuotanto on energeettisesti järkevää. Biopelkistimien taloudellinen kannattavuus verrattuna fossiilisiin pelkistimiin on tällä hetkellä heikko, mutta kilpailukykyinen verrattuna muihin CO₂ päästöjen vähennyskeinoihin, kuten hiilidioksidin talteenottoon ja -varastointiin. Energiapuun saatavuus biopelkistimien valmistukseen on suurin alueilla, jotka sijaitsevat lähellä Suomen terästehtaita. Biopelkistimien tuotannon kannattavuutta voitaisiin parantaa tuottamalla useita tuotteita ja hyödyntämällä prosessi-integraatiota
Hrnko, Lukáš. "Návrh koncového efektoru pro manipulaci se skleněnou zátkou." Master's thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2014. http://www.nusl.cz/ntk/nusl-231136.
Full textDiaz, Mateus Fabian Andrey. "Desenvolvimento de modelo computacional para craqueamento termico." [s.n.], 2008. http://repositorio.unicamp.br/jspui/handle/REPOSIP/266222.
Full textDissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Quimica
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Resumo: Neste trabalho é desenvolvida a modelagem matemática e a simulação computacional de um forno para processos de conversão térmica de frações pesadas de petróleo. O modelo cinético das reações de conversão é tomada de Sugaya (1993) a qual consta de uma reação irreversível de primeira ordem com 9 lumps reacionais e 24 pseudocomponentes. Os 24 pseudocomponentes são caracterizados e suas propriedades são calculadas mediante diferentes correlações e métodos encontrados na literatura. À medida que a carga avança pela tubulação do forno, a reação ocorre gerando quantidades maiores de componentes leves alterando as condições de fluxo como decorrência de alterações físico-químicas. Estes efeitos são levados em consideração na modelagem desenvolvida. O estado da mistura é verificado para cada passo de integração mediante a equação Soave Redlich Kwong. No caso de escoamento bifásico, as propriedades do líquido e do vapor são calculadas para determinar o regime de escoamento e calcular o Holdup. Este parâmetro permite estimar as propriedades de transporte, os coeficientes de transferência e a perda de carga. Inicialmente é simulada uma unidade piloto de craqueamento térmico. Esta unidade consta de uma serpentina aquecida isotermicamente, fato pelo qual só balanço de massa é integrado. O programa encontra as constantes cinéticas mediante um algoritmo Newton ¿ Raphson, cuja função objetivo é a diferença entre a conversão calculada e a conversão medida. Finalmente o forno industrial é simulado. Balanços de massa, momento, energia e temperatura de parede são integrados. Os resultados obtidos apresentam boa concordância com os dados do forno 23H ¿ 1 (Refinaria Presidente Bernardes, Cubatão) para craqueamento térmico. Deposição de coque na tubulação é avaliada para analisar o comportamento do processo. O programa desenvolvido permite o estudo do processo de craqueamento térmico para processos de conversão térmica como o coqueamento retardado e visco-redução. Novos parâmetros operacionais podem ser estudados, diferentes cargas e estratégias de controle podem ser simuladas e avaliadas com o software desenvolvido
Abstract: The mathematical modeling and the computational simulation of a process furnace for thermal conversion of heavy oil fractions is developed in this work. Kinetics of conversion reactions is from Sugaya (1993). It is based in a first order irreversible reaction with 9 lumps and 24 pseudocomponents. The 24 pseudocomponents are characterized and their properties calculated by different correlations and methods available in the literature. As walks through the furnace tubes, the feed, initially liquid, reacts generating light fractions and gas. The state of the mixture is checked for each integration step by a subroutine based on the Soave Redlich Kwong equation. When two phases are flowing, properties of the liquid and vapor are calculated to determine the flow regime and the holdup. This parameter allows to calculate the transport properties and the heat transfer and pressure drop coefficients. Initially, a thermal cracking pilot plant is simulated. This unit is formed by a reactor coil that is isothermally quenched; consequently, only mass balance is integrated. The program finds the kinetic constants by a Newton ¿ Raphson algorithm whose objective function is the difference between the calculated and measured conversion. Finally, an industrial furnace is simulated. Mass, momentum, wall temperature and energy balances are integrated. Results show good agreement whit the data reported from the industrial furnace 23-H-1 (Refinery Presidente Bernardes, Cubatão) for thermal cracking. Coke deposition in tubes is tested to analyze the performance of the process. The program developed in this work allows an insight study of thermal cracking processes such as delayed coking and visbreaking. New operational parameters, different feeds, control strategies and many other parameters can be studied.
Mestrado
Desenvolvimento de Processos Químicos
Mestre em Engenharia Química
Runtti, H. (Hanna). "Utilisation of industrial by-products in water treatment:carbon-and silicate-based materials as adsorbents for metals and sulphate removal." Doctoral thesis, Oulun yliopisto, 2016. http://urn.fi/urn:isbn:9789526212630.
Full textTiivistelmä Teollisuuden jätevedet kuten kaivosvedet ja metalliteollisuuden prosessien jätevedet voivat sisältää monenlaisia haitallisia ja jopa myrkyllisiä aineita kuten metalleja ja sulfaattia. Adsorptiota käytetään yleisesti esimerkiksi metallien ja orgaanisten yhdisteiden poistossa vesiliuoksista, koska se on tehokas ja yksinkertainen menetelmä. Aktiivihiili on yleisimmin käytetty adsorbenttimateriaali vedenpuhdituksessa, mutta sen hinta joissain tapauksissa rajoittaa sen käyttöä. Tämän vuoksi on tarvetta kehittää vaihtoehtoisia adsorbenttimateriaaleja edullisista raaka-aineista. Viime vuosien aikana on raportoitu mm. teollisuus- ja mineraalijätteistä, joita voidaan hyödyntää vesien ja jätevesien puhdistuksessa. Tämän työn tavoitteena oli hyödyntää teollisuudesta muodostuvia jätemateriaaleja (hiilijäännös, metakaoliini, masuunikuona ja analsiimi) raudan, kuparin, nikkelin, arseenin, antimonin tai sulfaatin poistossa malli- ja jätevesistä. Materiaaleja käsiteltiin erilaisilla kemikaaleilla (aktivointi, modifiointi tai geopolymerointi), jotta niiden adsorptiotehokkuudet paranisivivat poistettavia aineita kohtaan. Tulokset osoittivat, että raudan, kuparin ja nikkelin poisto oli sekä käsittelemättömällä että sinkkikloridilla aktivoidulla hiilijäännöksellä korkeampi kuin kaupallisella aktiivihiilellä. Arseenin, nikkelin ja antimonin poistoa kaivosvedestä tutkittiin masuunikuona- ja metakaoliinigeopolymeereillä, joista masuunikuonageopolymeeri osoittautui tehokkaimmaksi metallien poistajaksi. Bariumkloridilla modifioitu masuunikuonageopolymeeri puolestaan poisti erittäin tehokkaasti sulfaattia kaivoksen jätevedestä. Rautakloridilla modifioitu hiilijäännös ja happopesty bariumkloridilla modifioitu analsiimi osoittatuivat myös lupaavaksi materiaaliksi sulfaatin poistossa
Dong, Wei. "Design of advanced industrial furnaces using numerical modeling method." Doctoral thesis, KTH, Materials Science and Engineering, 2000. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-2900.
Full textThis doctoral thesis describes the fundamentals ofmathematical modeling for the industrial furnaces and boilersand presents the results from the numerical simulations of sometypical applications in advanced industrial furnaces andboilers. The main objective of this thesis work is to employcomputational fluid dynamics (CFD) technology as an effectivecomputer simulation tool to study and develop the newcombustion concepts, phenomena and processes in advancedindustrial furnaces and boilers. The applications concern onfrom retrofitted conventional grate boilers to the mostadvanced highly preheated and diluted air combustion (HPDAC)furnaces. In this work, several topics are specially concernedwhen applying CFD technology to combustion cases. These topicsare including grate bed model, NOxmodeling, mixing problem, air staging system, andhighly preheated and diluted air combustion technology. In thiswork, a black-box grate bed model is developed and used inmodeling of grate fired furnaces and boilers. It is based onthe thermodynamic calculations and a set of conservationequations of mass, energy of fuel and air on the grate bed. Oneof benefits of this bed model is simple and feasible to be putinto use in industry. For NOxmodeling, besides the thermal NO and prompt NO,the HCN route fuel NO has been employed to predict the fuel NOemissions in coal/biomass fired furnaces. In addition, based onNH3route of fuel NO formation, a SNCR scheme for NOxabatement has been proposed also. For mixingproblem, the concepts of global degree of mixing and individualdegree of mixing have been proposed and used successfully inpractical applications. The new definition of degree of mixingovercomes some shortages of existed mixing parameters, such asthe mixing factor and the degree of non-mixing, which arenon-normalized and may lose physical meaning in some regions ofthe system. A new air staging system has been studied. It isused to improve the secondary or over-fire air configuration,thus to reduce the pollutant emissions and to enhance thecombustion facilities' efficiencies. In this work, the airstaging system has been employed in coal and biomass combustionfor grate fired furnaces/boilers. The performance of the newair staging system has been evaluated and optimized by usingnumerical modeling method together with physical modelingmethod. Results show that the new air staging system has a goodpotential of improving the combustion quality and reducing thepollutant emissions in industrial furnaces and boilers.Recently, the highly preheated and diluted air combustiontechnology has been regarded as the new generation energytechnology for advanced industrial furnaces and boilers. Inthis work, the highly preheated and diluted air combustionphenomena have been studied by using different numericalmodels. A hybrid procedure of both the large eddy simulationusing subgrid-scale stress Smagorinsky model and the Reynoldsstress model with eddy dissipation model has been alsoinvestigated to study the dynamic combustion process under theconditions of highly preheated and diluted air combustion.Results show that HPDAC technology possesses advantages ofsaving energy and low NOxemission, thus it has high potential to be usedfor the next generation of industrial furnaces and boilers. Thelarge eddy simulation using subgrid-scale stress Smagorinskymodel together with Reynolds stress model / eddy dissipationmodel are possible to study the HPDAC dynamic process. Finally,this work shows that numerical modeling method is a verypromising tool to deal with the complicated combustionprocesses even for practical applications in industry.
Keywords: air staging, bed model, boiler, burner,computational fluid dynamics (CFD), Ecotube, fuel staging,furnace, grate combustion, highly preheated and diluted aircombustion (HPDAC), large eddy simulation (LES), mathematicalmodeling, nitrogen oxides (NOx), numerical simulation
Yu, Dingli. "Fault diagnosis for industrial systems with emphasis on bilinear systems." Thesis, Coventry University, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.364163.
Full textStröhle, Jochen [Verfasser]. "Spectral Modelling of Radiative Heat Transfer in Industrial Furnaces / Jochen Ströhle." Aachen : Shaker, 2004. http://d-nb.info/1172612382/34.
Full textBradley, Frederick Joseph. "Thermal shock resistance parameters for the industrial lining problem." Thesis, University of British Columbia, 1985. http://hdl.handle.net/2429/25568.
Full textApplied Science, Faculty of
Mining Engineering, Keevil Institute of
Graduate
Hachem, Elie. "Stabilized finite element method for heat transfer and turbulent flows inside industrial furnaces." Paris, ENMP, 2009. http://pastel.paristech.org/5656/01/EH-These.pdf.
Full textThe development of efficient methods to understand and simulate conjugate heat transfer for multi-components systems appears in numerous engineering applications and still a need for industrials, especially in the case of the heat treatment of high-alloy steel by a continuously heating process inside industrial furnaces. The thermal history of the load and the temperature distribution in the furnace are critical for the final microstructure and the mechanical properties of the treated workpieces and can directly determined their final quality in terms of hardness, toughness and resistance. The main objectives of this thesis is then to understand and better model the heat treatment process at the same time in the furnace chamber and within the workpieces under specified furnace geometry, thermal schedule, parts loading design, initial operation conditions, and performance requirements. The Computational Fluid Dynamics (CFD) simulation provides a useful tool to predict the temperature evolution and such processes. In the first part of this work, various stabilized finite element methods required for computing the conjugate heat transfer and the incompressible flows are proposed and analyzed. Two turbulence models, the k-epsilon and the Large Eddy Simulations (LES) models were introduced and used to simulate and take into account the complex turbulent flows inside the furnace chamber. The effect of thermal radiation was appropriately accounted for by means of a volumetric model known as the P1-model. In the latter part of this work, a multidomain approach referred as the immersed volume method (IVM) is introduced and applied to treat the fluid-solid interactions. It is based on the use of an adaptive anisotropic local grid refinement by means of the level-set function to well capture the sharp discontinuities of the fluid-solid interface. The proposed method showed that it is well suited to treat simultaneously the three modes, convective, conductive and radiative heat transfer that may interfere in both the fluid part and the solid part using anisotropic finite element meshes
Bayer, Steffen Christoph. "Cleaning up the furnace : patterns of environmental management in the British, Czech and German steel industries." Thesis, University of Sussex, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.366107.
Full textBosnjak, Vjekoslav. "Waste Heat Recovery in Intensive Small and Medium Sized Industries : Case Study - Gästrike Härdverkstad." Thesis, Högskolan i Gävle, Avdelningen för bygg- energi- och miljöteknik, 2012. http://urn.kb.se/resolve?urn=urn:nbn:se:hig:diva-13816.
Full textCARVALHO, ELITA F. U. de. "Desenvolvimento de um absorvedor inorganico solido para reduzir a emissao de fluoreto na industria ceramica." reponame:Repositório Institucional do IPEN, 2004. http://repositorio.ipen.br:8080/xmlui/handle/123456789/11180.
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Tese (Doutoramento)
IPEN/T
Instituto de Pesquisas Energeticas e Nucleares - IPEN/CNEN-SP
Mølnås, Håvard. "Compatibility Study of Carbon-Based Refractory Materials utilized in Silicomanganese Production Furnaces." Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for materialteknologi, 2011. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-16345.
Full textGagnon, Éric. "Modélisation de la turbulence dans des ecoulements de plasma en milieu industriel /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1996. http://theses.uqac.ca.
Full textPerron, Jean. "Modélisation mathématique simplifiée d'un four de métal chaud /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1987. http://theses.uqac.ca.
Full textLavoie, Yvon. "Modélisation tri-dimensionnelle et en régime transitoire des fours d'homogénéisation /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1993. http://theses.uqac.ca.
Full textErchiqui, Fouad. "Modelisation mathematique d'une chambre de combustion par la methode des plans imaginaires." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1987. http://theses.uqac.ca.
Full textEn tete du titre: Memoire presente a l'Universite du Queec a Chicoutimi comme exigence partielle pour l'obtention du grade de maitre es sciences appliquees. CaQCU Bibliogr.: ff. 60-61. Document électronique également accessible en format PDF. CaQCU
Menozzi, Sunny. "Preserving the ethos of industry at the Carrie furnaces: the redevelopment of an industrial heritage site and the interpretation of manufacturing culture." Thesis, Massachusetts Institute of Technology, 2015. http://hdl.handle.net/1721.1/99093.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (pages 103-110).
This thesis proposes design principles and a program for site of the Carrie Blast Furnace Plant, a National Historic Landmark in Pittsburgh's Monongahela Valley. The Redevelopment Authority of Allegheny County intends to redevelop this 168-acre former industrial site in the near future. In anticipation of this regionally important redevelopment project, this thesis considers the philosophical commitments of historic preservation, weighs economic growth imperatives, explores how the Carrie Furnaces could be made to cultivate public memory of industrialism, and examines competing visions of significance, authenticity, and interpretation of heritage sites, particularly in the context of deindustrialization. Four cases studies of internationally renowned projects demonstrate best practices in the redevelopment of historic blast furnace plants, ironworks, steelworks, and collieries. The Duisburg-Nord Landscape Park and Zollverein Park in Germany, the Belval City of Science project in Luxembourg, and the Parque Fundidora in Mexico all provide lessons in the preservation and adaptive reuse of derelict industrial infrastructure. Though their contexts differ, these four cases offer a common set of best practices to guide the Carrie Furnaces project. First, through designs and programs, these projects interpret the stories of industrial heritage sites for contemporary audiences, thereby cultivating public memory. Second, these projects' adaptive reuse of historic structures and spaces creates new, contemporary relationships between the sites and their various public audiences. This, as well as the fact that the designs are inspired by site-specific characteristics and are decidedly of their places and times, imparts authenticity. Third, these projects promote local economic revitalization through mixed-use development that engages broad constituencies. Finally, the projects use elements that pay homage to the industrial forms, materials, and culture that characterize their places. This paper's proposed development program and design for the Carrie Furnaces site preserves the site's "ethos of industry" through a 21st century manufacturing and tourism program that interprets the Carrie Blast Furnace Plant as a site of historic, vertically-integrated iron and steel production for the contemporary public consciousness. This program also promotes multi-sectoral economic growth, reconnects ailing nearby communities to the site, and conserves the material and cultural aesthetics of steel production, labor, thrift, and enterprise that made industrial Pittsburgh the center of American heavy manufacturing.
by Sunny Menozzi.
M.C.P.
Jain, Pankaj. "Étude du transfert de chaleur convectif dans un four circulaire /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1996. http://theses.uqac.ca.
Full textMyrstener, Erik. "Environmental impacts of early metallurgy in Moshyttan : A study of one of Europe's oldest blast furnaces, using three lakes records in Nora bergslag." Thesis, Umeå universitet, Institutionen för ekologi, miljö och geovetenskap, 2013. http://urn.kb.se/resolve?urn=urn:nbn:se:umu:diva-64733.
Full textRafaralahy, Hugues. "Modélisation d'un processus thermique et reconstruction de l'état et des défauts pour une classe de systèmes à paramètres distribués de type parabolique." Nancy 1, 1993. http://www.theses.fr/1993NAN10223.
Full textSilva, Anderson Badia da. "Utilização de carepas como componente da carga de um forno elétrico a arco." reponame:Biblioteca Digital de Teses e Dissertações da UFRGS, 2012. http://hdl.handle.net/10183/77730.
Full textIndustrial processes generate several residues and many of them are suitable for recycling. In the steel industry, casting operations and mechanical forming originate a solid brittle layer of oxide known as scale, which is produced by oxidation of the steel surface when exposed to a thermal gradient. Consisting of iron oxides, it therefore holds the essential element for steel manufacturing. This study performed analysis, laboratory trials and industrial tests to investigate scale recycling in an electric arc furnace. Chemical and physical properties of the material were analyzed and, at reducibility laboratory trials, the behavior of the scale was observed when mixed with a reducing agent. In industrial tests, the scale was introduced in an electric arc furnace mixed with the loaded scrap and the behavior of the main process variables was evaluated. By understanding its influence on the process, it was possible to determine the feasibility of scale recycling in steelmaking. The scales generated in the steel plant were distinguished mainly by the particle size and moisture content. Samples were chemically similar, with minimum 70% iron content. In its composition predominate hematite, magnetite and wustita oxides, the latter being the most important. In self-reduction laboratory tests, the best results for fraction reacted and metallization grade were reached with the highest temperatures. In industrial tests, with 1% scale added to the scrap, there was no influence in the electric energy consumption or FeO content of the slag. The liquid steel dephosphorization was positively affected since the average phosphorus percentage was reduced by 15% with the scale utilization. However, the yield indicator suffered negative impact, suggesting the need for further assessments to determine the scale recycling feasibility in electric arc furnace process.
Commandré, Isabelle. "L'artisanat du verre en Bas‐Languedoc du XVIe au XVIIIe siècle." Thesis, Aix-Marseille, 2014. http://www.theses.fr/2014AIXM3041.
Full textThe modern woodlands glassmaking enjoys a particularly siginifant development in the Lower Languedoc region which benefits from a deeply rooted tradition from the thirteenth century on. However, the ways and structures of production are as yet very poorly documented and the historiography generally gives a picture of a modest network of workshops producing objects for daily use.Based on the additionnal information of written archaeological and archeometrical sources, this study favours the analysis of these factories from eight excavated sites. At first place it gives an approach of the people as well as the surrounding area which shows the formal structuring of this ceramic skillset. About a hundred moderns production centres emerged, grouped together in a number of zones with several workshops near each other. Their extent is limited, on the other hand they indicate a certain autonomy in production. From the smallest unit in the woodlands to the big establishments which resembledl proper village settlements, each site ensured the complete cycle of the operational chain of glass production. Generally, the workshops were a relatively simple infrastructure assembled around two or three furnaces with complementary functions: frit, fusion and annealing furnaces.As a region favourable to the establishment of glassmaking due to the rich resources in raw materials, modern Languedoc produced mainly hollow, concave glass.. Basically their production supplied the province which was the biggest of the kingdom. It is only from the first third of the eighteenth century that this woodland craft industry declined progressively as big coal-fired factories took over
Fillion, Claude. "Développement d'un système de contrôle pour un four virtuel par automate programmable /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 2002. http://theses.uqac.ca.
Full textDufour, Amélie. "Multivariate statistical modeling of an anode backing furnace : Modélisation statistique multivariée du four à cuisson des anodes utilisées dans la fabrication d'aluminium primaire." Master's thesis, Université Laval, 2016. http://hdl.handle.net/20.500.11794/26844.
Full textThe aluminum manufacturing process is highly influenced by the anode quality. Several factors affect the anode quality and the actual quality control strategy is inadequate to detect faulty anodes before setting them in the electrolytic cells. A soft-sensor model developed from historical carbon plant data and multivariate statistical methods was proposed in past work to obtain quick predictions of individual anode properties right after baking for quality control purposes. It could only be used for anodes baked at the coldest and hottest positions within the furnace due to the core sampling strategy used at the partner’s plant. To complement the soft-sensor, this work proposes a method for taking into account the thermal history of anodes baked at eventually any position and to allowing for the prediction of properties for all anodes. It is shown that combining categorical variables for pit and baking positions and routinely available firing equipment data is sufficient for predicting the temperature profiles of anodes baked in different positions (measured during pit surveys) and account for its impact on anode properties. Prediction results were validated using core sampling and good performance was obtained for LC, apparent and real density, compressive strength and air reactivity.
Samuelsson, Peter. "Management of technology in the process industries: Matching market and machine." Doctoral thesis, KTH, 2017. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-199705.
Full textQC 20170116
Bagatini, Maurício Covcevich. "Estudo de reciclagem da carepa através de briquetes autorredutores para uso em forno elétrico a arco." reponame:Biblioteca Digital de Teses e Dissertações da UFRGS, 2011. http://hdl.handle.net/10183/37372.
Full textThis dissertation aimed to provide theoretical and experimental basis for recycling of mill scale generated in mini-mill plants through the use of self-reducing briquettes in EAF. To reach these goals, the work was structured around four main topics: characterization and reducibility study of scale, choice and characterization of the reductant to use in briquettes, elaboration and characterization of the mixture and laboratory tests to performance evaluation of self-reducing briquettes. The characterization studies of mill scale have indicated that this waste is composed mainly of wustite and is stratified into three layers with different morphologies: fine porous external layer composed of hematite and magnetite, intermediate layer of dense wustite and inner layer of porous wustite. The kinetics of scale reduction was investigated in thermobalance in a temperature range from 830 to 1200°C with pure CO and a mixture of 90% CO and 10% CO2. The apparent activation energy obtained in these tests ranged from 71 to 80 kJ/mol and the microscopic observations showed that the mill scale reduction corresponds to a topochemical model. The choice of the reductant for composing the briquette was made through tests of gasification with CO2 and of self-reduction in thermobalance with three different carbonaceous materials. From the results, it was observed the following decreasing reactivity order and the related apparent activation energy: Charcoal (Ea = 237 kJ/mol), Mineral Coal (Ea = 214 kJ/mol) and Petroleum Coke (Ea = 335 kJ/mol). Due to the higher reactivity of Charcoal in relation to the others, this reducer was chosen to be used in the briquettes. The main constituents of the mixture used in the manufacture of self-reducing briquettes were scale, charcoal and binders (melasse and lime). The characterization tests in thermobalance with oxidizing athmosfere and rapid heating indicated a mass loss of about 40%, referring to the stages of drying, devolatilization and self-reduction of the mixture. During these tests, it were observed high rates of mixture loss mass and a remarkable complexity of the phenomena, with simultaneous combustion, self-reduction and iron oxidation reactions, where their importance changes according to temperature and fractional reaction of the sample. Through the procedures that aimed to reduce the complexity of the related phenomena in oxidant conditions, it was possible to estimate that the self-reduction apparent activation energy ranges between 62 to 69 kJ/mol. The briquettes produced in the industrial plant were submitted to isothermal and nonisothermal tests of high temperatures. Such tests aimed to determine the thermal gradients into the briquette, the apparent activation energy and kinetic performance of the agglomerate in temperature conditions similar to the ones used in industrial practice. Based on the findings concerning the individual rates of chemical reactions (reduction and gasification), the measures of the temperature profile inside the briquettes, the activation energy estimated (93 kJ/mol) and the reduction model found in high-temperature tests, it is assumed that both the kinetics of mill scale reduction and heat transfer limit the overall kinetic rates of these briquettes. Finally, the results of metallization obtained in the tests conducted at high temperatures indicate the possibility of using these briquettes into the EAF.
Larouche, Andre. "Couplage de la methode des plans imaginaires en trois dimensions et du logiciel phoenics pour la modelisation de la chambre de combustion de fours industriels." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1988. http://theses.uqac.ca.
Full textEn tete du titre : Memoire presente a l'Universite du Quebec a Chicoutimi comme exigence partielle de la maitrise en ressources et systemes. CaQCU Document électronique également accessible en format PDF. CaQCU
Alekseev, Kirill. "Hazardous bauxite residue, blast furnace slag, and foundry sand application as the main components for environmentally friendly red ceramics production." Universidade Tecnológica Federal do Paraná, 2017. http://repositorio.utfpr.edu.br/jspui/handle/1/2868.
Full textIn the presented research were used residues of aluminum and iron production. Bauxite residue, which is also called bauxite tailings or red mud, and blast furnace slag are the key wastes of metallurgical industry. There was also used foundry sand, which is a residue of casting process. These three components were used together to develop ceramic construction material. The main idea was to use industrial wastes only, no traditional natural materials. The waste glass and wood ash were added to the compositions in order to decrease melting point of the samples. In the research 24 compositions were sintered at 800-1225°C and their properties were studied. Their mechanical characteristics were analyzed using flexural strength test, measuring water absorption, density, and linear shrinkage. Physicochemical properties were studied by XRF, XRD, AAS, SEM, EDS, LAMMA, mapping, DTA, and TGA. The main reason for high results of flexural strength (19.78 MPa) of the samples was identified as a development of new amorphous formations. As a result of research, some compositions were suggested for specific construction materials production. Compositions containing red mud (40-100%), blast furnace slag (0-50%), foundry sand (0-50%), waste glass (0-20%), and wood ash (0-20%), according to Brazilian Norms and regulations for construction materials, may substitute traditional ceramic materials, which involve enormous exploration of natural resources.
Hadid, Baya. "Développement de capteurs logiciels pour procédés industriels par estimation paramétrique." Thesis, Poitiers, 2014. http://www.theses.fr/2014POIT2305.
Full textThis thesis was funded by the ANR through the Energy Efficiency and reduction of CO2 emissions in industrial systems program. The CHIC - CHaîne de mesure Innovante à bas Coût - project initiated and supported by EDF R&D aims to develop and test an innovative low cost and nonintrusive measuring system to monitor and analyze the consumption of energy fluids used in industrial sites in order to detect consumption drifts with a measurement accuracy of about 5%. This thesis focuses on the soft sensors implementation for power and flow measurements. Three subsets were used to carry out experiments in an almost industrial situation: an electric furnace, a gas boiler and an air compressor. The electric furnace application was on the electric power estimation and fault detection using a closed-loop estimation of the furnace model from the set and inner temperatures and the control signal of free-load and load tests. The flows estimation was conducted on an industrial boiler and an air compressor. Since the models parameters depend on other variables, a static LPV approach is proposed. On the boiler, the gas flow is estimated from the valve control and the gas pressure and temperature using different valve types. A non-parametric approach using Gaussian processes is also studied on this subset. The gas flow sensor has been validated on-site using a direct implementation in C# on the PLC process control. On the compressor, the parametric variation study according to the air temperature, humidity and discharge pressure has been conducted on simulation and real data. These early studies have shown the feasibility of the different soft sensors to achieve the fixed objectives
Dubuisson, Carine. "Cinétique de la calcination du coke de pétrole en atmosphére oxydante /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1993. http://theses.uqac.ca.
Full textAlp, Baris. "Utilization Of Ggbfs Blended Cement Pastes In Well Cementing." Master's thesis, METU, 2012. http://etd.lib.metu.edu.tr/upload/12614683/index.pdf.
Full textRacková, Eliška. "Areál bývalého šamotového závodu MŠLZ Mladějov na Moravě - funkční využití areálu pro potřeby Průmyslového muzea Mladějov." Master's thesis, Vysoké učení technické v Brně. Fakulta architektury, 2010. http://www.nusl.cz/ntk/nusl-215644.
Full textEl, Jannoun Ghina. "Adaptation anisotrope précise en espace et temps et méthodes d’éléments finis stabilisées pour la résolution de problèmes de mécanique des fluides instationnaires." Thesis, Paris, ENMP, 2014. http://www.theses.fr/2014ENMP0077/document.
Full textNowadays, with the increase in computational power, numerical modeling has become an intrinsic tool for predicting physical phenomena and developing engineering designs. The modeling of these phenomena poses scientific complexities the resolution of which requires considerable computational resources and long lasting calculations.In this thesis, we are interested in the resolution of complex long time and large scale heat transfer and fluid flow problems. When the physical phenomena exhibit sharp anisotropic features, a good level of accuracy requires a high mesh resolution, hence hindering the efficiency of the simulation. Therefore a compromise between accuracy and efficiency shall be adopted. The development of space and time adaptive adaptation techniques was motivated by the desire to devise realistic configurations and to limit the shortcomings of the traditional non-adaptive resolutions in terms of lack of solution's accuracy and computational efficiency. Indeed, the resolution of unsteady problems with multi-scale features on a prescribed uniform mesh with a limited number of degrees of freedom often fails to capture the fine scale physical features, have excessive computational cost and might produce incorrect results. These difficulties brought forth investigations towards generating meshes with local refinements where higher resolution was needed. Space and time adaptations can thus be regarded as essential ingredients in this recipe.The approach followed in this work consists in applying stabilized finite element methods and the development of space and time adaptive tools to enhance the accuracy and efficiency of the numerical simulations.The derivation process starts with an edge-based error estimation for locating the regions, in the computational domain, presenting sharp gradients, inner and boundary layers. This is followed by the construction of nodal metric tensors that prescribe, at each node in the spatial mesh, mesh sizes and the directions along which these sizes are to be imposed. In order to improve the efficiency of computations, this construction takes into account a fixed number of nodes and generates an optimal distribution and orientation of the mesh elements. The approach is extended to a space-time adaptation framework, whereby optimal meshes and time-step sizes for slabs of time are constructed in the view of controlling the global interpolation error over the computation domain
Zacharie, Célien. "Modélisation des transferts thermiques instationnaires par modèles paramétriques : application à un four industriel de brasage d’échangeur sous vide." Electronic Thesis or Diss., Université de Lorraine, 2020. http://www.theses.fr/2020LORR0264.
Full textIn the brazed aluminium heat exchanger manufacturing process at Fives Cryo (88, France), the brazing operation in an electric vacuum furnace consists of assembling a stack of aluminum parts of several cubic meters by making it reach the melting temperature of the braze. The control of heat transfer during this operation is necessary to ensure production quality. The long-term challenge for the company is to develop a new simulation tool based on reduced models, adaptable to all heat exchanger geometries, and to implement it on the real process to optimize the control of the furnace. Within the framework of the thesis, it was shown that parametric models ARX can reproduce the behaviour of the studied system composed of the furnace and its load under certain conditions. ARX models can be interpreted as a by-product of heat transfer functions that can recalculate temperatures at relevant points of the load: at its surface and its core. To verify their identifiability, these behavior laws were studied from numerical modeling of the system using FlexPDE® (1D and 2D) and Simfurnace® (internal 3D software). In parallel, a characterization of the process metrology was carried out. The evaluation and control of measurement errors in a device under vacuum and subjected to high radiative fluxes are essential to obtain reliable temperature measurements in transient and stationary states. The research of instrumentation conditions guaranteeing this reliability is a major challenge to make the brazing process reproducible. This property is also required to properly identify transfer functions from experimental data and to exploit them afterwards
Bourgeois, Thierry. "Couplage du logiciel Phoenics et de la méthode de zones en vue de la modélisation du transfert de chaleur dans des fournaises industrielles /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1988. http://theses.uqac.ca.
Full textReis, Walter Luiz da Costa. "Otimização da reciclagem de resíduos siderúrgicos por redução carbotérmica." Universidade Federal de São Carlos, 2008. https://repositorio.ufscar.br/handle/ufscar/663.
Full textThe evolution of the world-wide production of steel in rates superior to 7% per year in the last five years, strongly driven by China, which got off 222,4 millions in 2003 for 489,0 million tons in 20071, leads to a strong increase in the demand of iron ore. Therefore, fine ore price of Carajás for Asia went out from 28,14 in 2003 for 73,20 US$ cents for unity of iron in 2007. An increase of 160%. These facts, when related to the layer exhaustion and the growing environmental pressures on Iron and Steel Plants of the whole world, have been taking to a series of studies to the use of the residues bearers from iron produced in these factories. Up to that time, there has not been consolidated any technology which is technically and economically viable for the recycling of these residues so far. The present work is about the usage of the blast furnace mud, the mill scale and the iron oxide produced in the pickling lines of Companhia Siderúrgica Nacional (CSN) in self reduction pellets shape. It starts the productions in scale laboratorial and industrial after the chemical and physical characterizations from these raw materials. As soon as the most appropriated formulation was defined, the production in experimental scale began. These tests were carried out in the residues palletizing pilot plant, developed by CSN. There were also tests of self reduction and of meltreduction. In the first one, the formation of a metal drop inside a hallow sphere was obtained, and in the second one a metal profit of 99,1%. In sequence, the alternatives were valued for internal recycling of these pellets. The use of the heat contained in the empty hot-metal torpedo-cars for self-reduction showed the most economical route. This technology of recycling was introduced industrially in CSN. Thus, in the present work of doctorate, it was developed an unpublished route for industrial recycling for iron and steel residues, which was technically and economically feasible.
O crescimento da produção mundial de aço bruto em taxas superiores a 7% ao ano nos últimos cinco anos, fortemente impulsionado pela China, que saltou de 222,4 milhões em 2003 para 489,0 milhões de toneladas em 20071, gerou um forte aumento na demanda de minério de ferro. Com isso, o preço do minério fino de Carajás para a Ásia saiu de 28,14 em 2003 para 73,20 US$ cents por unidade de ferro em 2007. Um aumento de 160%. Estes fatos, associados à exaustão das jazidas e as crescentes pressões ambientais sobre as Siderúrgicas de todo o mundo, têm levado a uma série de estudos para o aproveitamento dos resíduos portadores de ferro gerados nestas Usinas. Até então, não se consolidou nenhuma tecnologia viável técnica e economicamente para esta reciclagem. O presente trabalho trata da utilização da lama de alto-forno, da carepa de laminação e do óxido de ferro gerado nas linhas de decapagem da Companhia Siderúrgica Nacional CSN na forma de pelotas auto-redutoras. Após as caracterizações químicas e físicas destas matérias-primas, partiu-se para as produções em escala laboratorial e industrial. Definida laboratorialmente a formulação mais adequada, partiu-se para a produção experimental. Esta foi realizada na planta piloto de pelotização de resíduos, desenvolvida pela CSN. Foram realizados ensaios de auto-redução e de fusão-redução. No primeiro, o resultado foi a formação de uma gota metálica dentro de uma esfera oca e no segundo, um rendimento metálico de 99,1%. Em seqüência, foram avaliadas as alternativas para reciclagem interna destas pelotas. A utilização do calor contido nos carrostorpedo vazios para a auto-redução se mostrou como a rota mais econômica. Esta tecnologia de reciclagem já se encontra implantada industrialmente na CSN. Portanto, no presente trabalho de doutoramento, desenvolveu-se uma rota inédita de reciclagem industrial dos resíduos siderúrgicos portadores de ferro, viável técnica e economicamente.
Piquemal, Philippe. "Élaboration d'un nouveau matériau isolant phonique et thermique en verre expansé et mise au point d'un procédé utilisant un chauffage diélectrique." Nancy 1, 1988. http://www.theses.fr/1988NAN10203.
Full textGarrofé, Paulo Henrique Simas. "Uma perspectiva pós-fordista na operação de sistemas elétricos." reponame:Repositório Institucional do FGV, 2004. http://hdl.handle.net/10438/8056.
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This work intends to show, through a case study, that the implementation of a production and work organization model based on process management could be seen through a post-Fordist perspective in the operation of power systems. Large brazilian companies in the power industry have adopted, since their creation, an organizational model based on management rules proposed by Henri Fayol, in a vertical and hierarchical structure fashion. On the other hand, the tasks performed in the control rooms of their Operation Centers follow the schemes established by Frederick Taylor's Scientitic Administration system and the principIes proposed by Henry Ford. Nevertheless, due to changes in the institutional model of the power industry that took place in the mid-nineties and the increasing awareness of society toward its rights along with the workers' urge for the democratization of social relations in their working environment, these power industry companies were driven to seek for fresher styles of management, more suitable for the new cultural, political, social and economic scenario. The System Operation Department in FURNAS decided to embrace, as a new form of production and work organization, a system based on process management, yet respecting the functional structure of the company, thus creating a matrix organizational structure. Notwithstanding, it has been observed that, depending on the implementation form and the adopted management mechanisms, this new system could be seen through a post-Fordist perspective in the operation activity of bulk power systems, typically carried out in Brazil by Fayolist companies, according to a Taylorist-Fordist perspective. To verify the outcome of this implementation, a research was carried out in alI tive Operation Centers of the System Operation Department in FURNAS Centrais Elétricas S.A., having as a key element the following characterization of the post-Fordist paradigm: integrated differentiation of production and work organization under the trajectory of technological innovation toward the democratization of social relations in enterprise-systems. The paper presents the perception both of the evolution in the workers' interpersonal relations and of the managerial actions taken to introduce this new system and shows the occurred changes regarding the democratization of social relations in the Department as well, among other factors which substantiate the research, whose results point to a new form of work and production management where these social relations tend to follow dialogical managerial actions that characterize the post-Fordist perspective.
O objetivo deste trabalho é mostrar através de um estudo de caso que a implantação de um modelo de organização da produção e do trabalho baseado na gestão por processos pode acenar com uma perspectiva pós-fordista para a atividade de operação de sistemas de energia elétrica. As grandes empresas brasileiras do setor de energia elétrica adotaram, desde a sua criação, um modelo organizacional com base nas funções gerenciais propostas por Henri Fayol, sendo estruturadas de forma vertical e hierárquica. Por outro lado, as tarefas realizadas nas salas de controle dos Centros de Operação dessas empresas se processam de acordo com a forma preconizada pelo sistema de Administração Científica de Frederick Taylor e pelos princípios propostos por Henry Ford. Porém, em decorrência da mudança do modelo institucional do setor de energia, ocorrida em meados da década de 90, além da maior conscientização da sociedade a respeito dos seus direitos de cidadania e também da busca dos trabalhadores pela democratização nas relações sociais em seu ambiente de trabalho, as empresas de energia elétrica foram compelidas a buscar novas formas de gestão mais adequadas ao novo cenário cultural, político, social e econômico. Em FURNAS, como nova forma de organização da produção e do trabalho, o Departamento de Operação do Sistema resolveu adotar um sistema baseado na gestão por processos que respeita a estrutura funcional da Empresa, formando, assim, uma estrutura organizacional matricial. Por outro lado, observou-se que, dependendo da forma de implantação e dos mecanismos de gestão adotados, esse novo sistema podia acenar com uma perspectiva pós-fordista para a atividade de operação de sistemas elétricos de grande porte que, tipicamente, no Brasil, é desenvolvida por empresas fayolistas, segundo uma perspectiva taylorista-fordista. Para verificar se essa possibilidade se concretizou foi realizada uma pesquisa que abrangeu os cinco Centros de Operação do Departamento de Operação do Sistema de FURNAS Centrais Elétricas S.A., tomando como elemento-chave a seguinte caracterização do paradigma do pós-fordismo: diferenciação integrada da organização da produção e do trabalho sob a trajetória de inovação tecnológica em direção à ~ democratização das relações sociais nos sistemas-empresa. O trabalho apresenta a percepção da evolução nos relacionamentos interpessoais e a percepção das ações gerenciais empreendidas visando a implantação do novo sistema, bem como também mostra as transformações ocorridas no tocante à democratização das relaçõe~ sociais no Departamento, entre outros fatores que substanciam a pesquisa, cujo resultado aponta para uma nova forma de gestão do trabalho e da produção em que essas relações sociais tendem a ser pautadas por ações gerenciais dialógicas que caracterizam a perspectiva pós-fordista.
Ntuli, Anthony Cebisa, and 安東尼. "Modelling of heat transfer in industrial furnace walls." Thesis, 2016. http://ndltd.ncl.edu.tw/handle/84532419092604966526.
Full text崑山科技大學
機械工程研究所
104
Heat transfer through a multi-layer domain can depend on the individual thermal conductivity of the materials and their layer thickness. Thus to minimize heat flux, the thickness should be increased while choosing a material with low thermal conductivity. The heat flux also depends on the temperature difference between the layer, large temperature differences can lead to high heat flux across the layer. Also it can greatly depend on the contact between the layers, either a perfect contact or a rough surface. Usually, rough layers lead to minimized heat transfer across the domain, that depends on the gas in the gaps of the rough surfaces, contact pressure, hardness of the materials in contact and the mean slope of the rough surfaces. It is known that most gases have very low thermal conductivity. This allows them to be used as an insulator in many industrial and general designs. But as much as it is a good insulator, a gas has a tendency of developing a velocity field, either a laminar flow or turbulent flow, depending on the parameters and conditions. This velocity field can, in turn increase the thermal conductance of the gas, and cause inconsistent temperature and heat flux distribution profiles. This study aims to research and simulate heat transfer in industrial furnace walls. Different structures of walls are studied. A three-layer multi-refractory furnace is considered. Vertical wall, upside wall and bottom walls are studied. At the surfaces, cooling by natural convection can make the surface to be non-isothermal. This is because there are different local heat transfer coefficients along the surface of the vertical or horizontal plate. The effect of natural convection to the temperature distribution and heat flux distribution is studied. Major cases that are observed are adding a layer of a gas between the walls and studying when two of the wall linings are rough surfaces, with a gas inside the gaps of the rough surfaces, contact thermal heat transfer. Air is used for the air gap. The effect of the gas layer thickness to the temperature profile and heat flux profile is studied. Computational Fluid Dynamics software is used to carry out the simulations. The advantages and disadvantages of the study are discussed.
(5930321), Guangwu Tang. "Modeling of Steel Heating and Melting Processes in Industrial Steelmaking Furnaces." Thesis, 2019.
Find full textSteel heating and melting processes consume the majority of the energy used in advanced short-process steelmaking practices. Economic and environmental pressures from energy consumption drive the research to improve the furnace operation efficiency and energy efficiency. The goal of this research is to utilize computational fluid dynamics (CFD) modeling to provide useful tools and recommendations on the steel heating and melting practices in the steelmaking process. The steel slab reheating process, the steel scrap preheating process and the steel scrap melting process are studied.
A transient three-dimensional (3-D) CFD model was developed to simulate the flow characteristics, combustion process and multi-scale, multi-mode heat transfer inside the reheating furnace. The actual geometry of an operating industrial furnace was used and typical operating conditions were simulated. Specific walking speeds of slabs in production were modeled using a dynamic mesh model which is controlled by a user-defined function (UDF) solved using ANSYS Fluent. Fuel variations at different zones with respect to time were also considered. The model was validated with instrumented slab trials conducted at the SSAB Mobile (Alabama) mill. The temperature field in the furnace and the temperature evolution of a slab predicted by the CFD model are in good agreement with those obtained from the instrumented slab trials. Based on the simulation results, the slab reheating process and the temperature uniformity of a slab at discharge were able to be properly evaluated. In addition, a comprehensive two-dimensional (2-D) numerical heat transfer model for slab reheating in a walking beam furnace was developed using the finite difference method. An in-house code was developed. The model is capable of predicting slab temperature evolution during a reheating process based on real time furnace conditions and steel physical properties. The model was validated by using mill instrumented slab trials and production data. The results show that the temperature evolution predicted by the model is in good agreement with that measured by the thermocouples embedded in the instrumented slab. Compared with 3-D CFD simulation of a reheating process, this 2-D heat transfer model used for predicting slab temperature evolution requires less computing power and can provide results in a few seconds. A graphical user interface was also developed to facilitate the input and output process. This is a very convenient and user-friendly tool which can be used easily by mill metallurgists in troubleshooting and process optimization.
CFD models for steel scrap preheating and melting processes by the combined effects of the heat source from both oxy-fuel combustion and electric arc were also developed. The oxy-fuel burners firing natural gas (NG) are widely used in EAF operation during the scrap preheating and melting stages. In order to understand the role of oxy-fuel combustion and potentially increase the energy input from NG while decreasing the electricity consumption, numerical simulation of scrap preheating by oxy-fuel combustion in an EAF was firstly conducted. A 3-D CFD model was developed with detailed consideration of gas flow, oxy-fuel combustion, heat transfer between gas and solid scrap and scrap oxidation. The model was validated by a small-scale experimental study and applied onto a real-scale EAF.
Scrap melting in bath is comprehensively studied with a CFD model developed to simulate the melting in bath process under given operating conditions. Two sub-models were developed for model integration: steel melting model and coherent jet model. The multiphase volume of fluid (VOF) model and the enthalpy-porosity technique are applied to describe the steel melting process. The coherent jet model calculates the gas jet momentum and is integrated into the flow model to calculate its effect on the fluid flow in the bath. The electric arc was treated as a heat flux to represent the heat transfer from the electric arc during the melting process. Model validations were conducted for each sub-model to ensure their accuracy. Parametric studies were also carried out to obtain useful information for real practice.
Overall, the CFD models developed in this research work have demonstrated value in improving energy efficiency in the energy-intensive steelmaking processes. The developed CFD models also provide insights for better understanding of the multi-physics processes.