DOCSLIB.ORG

Hearth Coke Bed Buoyancy in the Blast Furnace: Experimental Study with A

Total Page：16

File Type：pdf, Size：1020Kb

Download full-text PDF Read full-text
Hearth Coke Bed Buoyancy in the Blast Furnace: Experimental Study with A 2006:235 CIV MASTER’S THESIS Hearth Coke Bed Buoyancy in the Blast Furnace Experimental study with a 3-dimensional cold model PÄR SEMBERG MASTER OF SCIENCE PROGRAMME Luleå University of Technology Department of Chemical Engineering and Geosciences Division of Process Metallurgy 2006:235 CIV • ISSN: 1402 - 1617 • ISRN: LTU - EX - - 06/235 - - SE Abstract ABSTRACT The effect of buoyancy forces acting on the hearth coke bed or the “deadman” of the blast furnace has attracted a great deal of interest during recent years of blast furnace research. This thesis presents an effort to elucidate the particle movement patterns connected to formation of a coke free layer in the hearth. In the work, the impact of different pressure distributions on the behaviour of the particle bed was studied with an experimental 3D-cold blast furnace hearth model. The bases for the work were the results from tests along with two different numerical models from a previous study, Hearth coke bed buoyancy, a preliminary investigation, made in 2004 at Bluescope Steel Research, Port Kembla, Australia. In the model, a bed of plastic particles in water were subjected to different pressure distributions, and float-sink motions induced by accumulation and drainage of the water through a valve in the bottom. The results showed that the bed was quite resistant to internal particle movements, when subjected to different linear pressure distributions along the radius. However, previous studies have suggested the downward pressure under the raceways to be severely reduced, and when going below 15:85 in pressure ratio between the peripheral and central area, it was observed that the particles moved internally. As the central load was descending in the bed, upward particle movements were observed along the walls, as well as from the centre towards the walls on the bottom. Particle movements were strongly dependent on the sink-float motions, and moved relative to one another only during drainage, when particles under the central weight moved down faster than under the peripheral reduced pressure area. This mechanism resulted in formation of a peripheral free space in the bottom of the hearth. Addition of an agglomerate of particles to the bottom of the particle bed, resulted in less particle movements and retarded formation of the peripheral free space. Initially it was intended to carry out these tests also numerically using Bluescope Steel’s particle simulation package DPSim. Because of problems with validating DPSim for the application with float-sink motions induced by buoyancy forces, this section was constrained to a sensitivity analysis on the program. The study showed that the float-sink behaviour of the particle bed was insensitive to friction parameter adjustments in the tested range. It was also discovered that the assigned simulation time was of significant importance. This indicates that the common practise of reducing the runtime may not be valid for this application. i ii Acknowledgements ACKNOWLEDGEMENTS This Thesis was carried out at Bluescope Steel Research, Port Kembla, Australia, as the final step on my way to a master’s degree in Chemical Engineering at Luleå University of Technology, LTU. First, I would like to express my sincere gratitude to Doctor Paul Zulli at Bluescope Steel Research and Professor Bo Björkman at the faculty of process metallurgy, LTU, for making this numerable experience in Australia possible for me. I would also like to thank Paul for supervising, for inspiration and encouragement, and for the freedom I have been given throughout my work. I would like to thank Bryan Wright, David Pinson and Ian Bean. Bryan and David for supervising and support with the numerical work, and Ian for helping with the experimental equipment. Thanks to Bryan also for helping me with everything and anything from the first day of my work until the last. Finally, I would like to thank all the others in the unit for six very rewarding months as a member in the group. I have very much appreciated the open door policy, all valuable discussions and feedback, and your longsuffering patience with my almost never ending questions. Pajala, March 2006 Pär Semberg iii iv Table of contents TABLE OF CONTENTS INTRODUCTION 1 1 LITERATURE REVIEW 3 1.1 Overview of the blast furnace 3 1.1.1 The upper zone 3 1.1.2 The cohesive zone 4 1.1.3 Force modelling in the upper- and cohesive zone 4 1.1.4 The lower zone 4 1.1.5 Force balance in the lower zone 7 1.2 Conclusion 12 2 EXPERIMENTAL 15 2.1 Introduction 15 2.2 Equipment 15 2.3 Experiments conducted 16 2.4 Uniform, central and peripheral pressure distributions 17 2.4.1 Equipment 17 2.4.2 Results 18 2.4.3 Discussion 21 2.5 Laser tracking of bed movement 21 2.5.1 Equipment 22 2.5.2 Results 23 2.5.3 Discussion 25 2.6 Tests with extreme distributions 27 2.6.1 Equipment 27 2.6.2 Results 28 2.6.3 Discussion 32 2.7 Bottom profile 33 2.7.1 Equipment 33 2.7.2 Results 34 2.7.3 Discussion 35 2.8 Faoled bed 36 2.8.1 Equipment 36 2.8.2 Results 37 2.8.3 Discussion 38 3 NUMERICAL WORK 39 3.1 Introduction 39 3.2 Method 40 3.3 DPSim Buoyancy model and modelling parameters 40 v 3.4 Experimental equipment and procedure 42 3.4.1 Box test for estimating the angle of repose 42 3.4.2 Experimental buoyancy model 43 3.5 Results 44 3.5.1 Box tests 44 3.5.2 Buoyancy tests 45 3.6 Discussion 54 CONCLUSIONS AND RECOMMENDATIONS 57 REFERENCES 59 APPENDIX 1 APPENDIX 2 vi Introduction INTRODUCTION The blast furnace has been used for producing iron from ore since at least the 14 th century in the Nordic countries, and the process is still today responsible for the majority of the steel production in the world. In the past, “know how” of the blast furnace process most probably was limited, and obtained by practical experiences. Not until recently, during the 20th century, have efforts in terms of applied research been made. The process is capital intensive, and in order to be cost efficient the furnace must be run at long operational lifetime, high availability and high efficiency(Wright, 2002). Today there is a fairly good understanding of the general principles governing the blast furnace ironmaking process. The blast furnace is basically a high temperature, counter current, multiphase reactor where descending iron oxides are reduced by ascending carbon monoxide gases, produced in the lower level of the vessel. The ore and coke are packed in discrete layers to maintain sufficient permeability in the bed, even after the ore loses its permeability due to softening and melting further down in the shaft. From the softening/melting zone where all the ore has smelted, only coke remains intact with the molten metal on the bottom of the vessel, which is known as the hearth. Based on temperature variations in the refractory lining of the hearth, it has been suggested that the coke bed under some conditions is floating on the molten metal and slag, and sometimes sitting on the bottom of the furnace. During recent years, quite a lot of effort has been made to explain the principles underlying the floating/sitting state of the hearth coke bed. However, the mechanisms proposed are novel, and not yet well understood. At Bluescope steel research, a preliminary study, “Hearth Coke Bed Buoyancy- a preliminary investigation” was carried out experimentally, and numerically in order to shed some light on the fundamental principles governing the hearth behaviour. This work was an approach to model the hearth coke bed by force balances, with results indicating that bouyancy forces, and the casting cycle possibly could explain sitting and floating behavior of the dead man. The aim of this thesis is to use the findings from the preliminary study and take a step further towards a deeper understanding for the physical phenomenas and conditions of the blast furnace hearth. Of particular interest, is the force balance of the hearth and the importance of buoyancy forces on the proposed floating and sitting states of the hearth coke bed or “deadman”. The previous work included preliminary evaluations by both experimental and numerical methods, and both these paths will be considered in this work as well . 1 2 1 Literature review 1 LITERATURE REVIEW 1.1 OVERVIEW OF THE BLAST FURNACE The question of whether the coke in the hearth is floating or sitting during operation can be answered by a complete force balance on the whole furnace. In order to gain some understanding of the parameters possibly affecting the state of the deadman, the different parts of the furnace are first explained. 1.1.1 The upper zone The principal raw materials of iron ore, coke and limestone are fed from above through a chute that distributes the raw materials into discrete layers of coke and iron ore, see fig 1.1. The ore layers are blends of sinter, lump and pellets. The coke is usually fed to make the coke layer slightly thicker in the center in order to enhance productivity and obtain optimum gas utilisation. As coke is combusted in the blast zones known as raceways in the bottom of the shaft, the bed slowly moves down as the iron oxides are reduced by the ascending CO-gases. The ore, mainly hematite, in the reduction process goes through the oxidic states magnetite and wustite before formation of iron and melting occur further down. The residence time in the upper zone is usually 4-6 hours depending on radial location in the furnace.
Load more

Recommended publications
  • National Register of Historic Places Multiple Property
    NFS Form 10-900-b 0MB No. 1024-0018 (Jan. 1987) United States Department of the Interior National Park Service National Register of Historic Places Multipler Propertyr ' Documentation Form NATIONAL This form is for use in documenting multiple property groups relating to one or several historic contexts. See instructions in Guidelines for Completing National Register Forms (National Register Bulletin 16). Complete each item by marking "x" in the appropriate box or by entering the requested information. For additional space use continuation sheets (Form 10-900-a). Type all entries. A. Name of Multiple Property Listing ____Iron and Steel Resources of Pennsylvania, 1716-1945_______________ B. Associated Historic Contexts_____________________________ ~ ___Pennsylvania Iron and Steel Industry. 1716-1945_________________ C. Geographical Data Commonwealth of Pennsylvania continuation sheet D. Certification As the designated authority under the National Historic Preservation Act of 1966, as amended, J hereby certify that this documentation form meets the National Register documentation standards and sets forth requirements for the listing of related properties consistent with the National Register criteria. This submission meets the procedural and professional requiremerytS\set forth iri36JCFR PafrfsBOfcyid the Secretary of the Interior's Standards for Planning and Evaluation. Signature of certifying official Date / Brent D. Glass Pennsylvania Historical & Museum Commission State or Federal agency and bureau I, hereby, certify that this multiple
    [Show full text]
  • Hopewell Village
    IRONMAKING IN EARLY AMERICA the Revolutionary armies, is representative of (such as Valley Forge) to be made into the tougher the hundreds of ironmaking communities that and less brittle wrought iron. This was used to Hopewell In the early days of colonial America, iron tools supplied the iron needs of the growing nation. make tools, hardware, and horseshoes. and household items were brought over from Europe by the settlers or imported at a high cost. Until surpassed by more modern methods, cold- HOPEWELL FURNACE Village The colonists, early recognizing the need to manu­ blast charcoal-burning furnaces, such as that NATIONAL HISTORIC SITE • PENNSYLVANIA facture their own iron, set up a number of iron­ at Hopewell, supplied all the iron. These furnaces In an age when most businesses were operated by works, notably at Falling Creek, Va., and Saugus, consumed about 1 acre of trees a day for fuel, one or two men in a shop, Hopewell employed at Mass. Operations gradually spread throughout so they had to be located in rural areas close to least 65 men, with some responsible for two or the colonies, and by the end of the 1700's, south­ a timber supply. more jobs. As the nearest town was many miles eastern Pennsylvania had become the industry's away, the ironmaster built a store to supply his center. Hopewell Village, founded by Mark Bird Since the pig iron produced by these furnaces workers, many of whom lived in company-owned in 1770 in time to supply cannon and shot for had a limited use, much of it was sent to forges homes.
    [Show full text]
  • What a Blast Furnace Is and How It Works
    VOLUME II SATURDAY, NOVEMBER I, 1902 NUMBER 18 What a Blast Furnace Is and How It Works Popular Article for the Scientifically Uneducated on the Parts of a Furnace and How Pig Iron Is Made. 1 HE following article on the construc- may be accepted as an accurate statement of how tion and operations of blast furnaces pig iron is made. The editor wishes to take this was written especially for Camp and opportunity to thank these gentlemen for their Plant Mr. A of the by Harry Deuel, painstaking and careful work. Engineering Department of the Min- have articles nequa Works. It was afterwards Arrangements been madefor other carefully revised, and approved in all in "popular," though accurate, form, descriptive details by Mr R. H. Lee, superin- of other departments of the coal, coke, iron and tendent of the Blast Furnace Department, and steel industry. " Boiler House. Engine House. Furnace Stack. Stoves. Blast furnace B. Blast Furnace "A," Minnequa Steel Works, Pueblo. This view well illustrates the different external parts of "A" Furnace of which, except for minor modifica- tions, "D," "E" and "F" are duplicates Each of these furnaces is 20 feet x 95 feet, is fitted with automatic skip hoists and with the very b st and most modern equipment. This vi-w was taken, however, before the ore. coke and limestone bins, from which the skip is now automatically loaded, were installed. There are four stoves to each furnace. 21 feet in diameter by 106 feet high. Each of the tall draft stacks is 12 feet 6 inches in diameter in the clear, by 210 feet high.
    [Show full text]
  • Using Cooled Mirror Hygrometers to Optimize Cold & Hot Blast Furnace
    Application Note Using Cooled Mirror Hygrometers to optimize Cold & Hot Blast Furnace processes Application Background The purpose of a blast furnace is to chemically reduce and physically convert iron oxides into liquid iron. The blast furnace is a huge, steel stack lined with brick. Iron ore, coke and limestone are dumped into the top, and preheated “hot blast” air is blown into the bottom. The raw materials gradually descend to the bottom of the furnace where they become the final products of liquid slag and liquid iron. These liquid products are drained from the furnace at regular intervals. The hot air that was blown into the bottom of the furnace ascends to the top in 6 to 8 seconds after going through numerous chemical reactions. These hot gases exit the top of the blast furnace and proceed through gas cleaning equipment where Cold Blast, Hot blast & Stoves particulate matter is removed from the gas and the gas is cooled. This gas has a considerable energy value so it is burned as a fuel in the "hot blast stoves" which are used to preheat the air entering the blast furnace to become "hot blast". Any of the gas not burned in the stoves is sent to the boiler house and is used to generate steam which turns a turbo blower that generates the compressed air known as "cold blast" that comes to the stoves. Why is Moisture Critical? This process can be optimized by proper control of the flame temperature, which is in turn affected by the moisture content of the blast air.
    [Show full text]
  • Refractory & Engineering
    Refractory & Engineering Solutions for Hot Blast Stoves and Blast Furnace Linings Blast Furnace Technologies Refractory & Engineering The Company – The Program Paul Wurth Refractory & Engineering GmbH has been integrated into the Paul Wurth Group in ` Blast furnace linings for extended service life December 2004. This alliance offers, on a turnkey ` Blast furnace cooling systems basis, single source supply and procurement options for complete blast furnace plants. ` Turnkey hot blast stoves with internal or external combustion chamber Originally, Paul Wurth Refractory & Engineering ` Ceramic burners with ultra-low CO emission GmbH has been founded as DME in 1993 through the merger of departments of Didier-Werke AG ` Highly effective stress corrosion protection and Martin & Pagenstecher GmbH. Customers systems benefit from the unsurpassed experience and ` Complete hot blast main systems know-how that both companies have developed in the field of hot blast stove engineering, refractory ` Complete heat recovery systems lining design, and hot metal production. ` Refractory linings for smelting and direct reduction vessels Paul Wurth Refractory & Engineering GmbH is always striving for world class stove and refractory ` Refractory linings for coke dry quenching designs to meet demanding market requirements, ` Refractory linings for pellet plants such as larger production capacity, extended ser- vice life, optimized refractory selection, and high Highly experienced and motivated teams of engineers, energy efficiency. designers and project managers
    [Show full text]
  • 1Natalija Dolic.Qxd
    Journal of Mining and Metallurgy, 38 (3‡4) B (2002) 123 - 141 STATE OF THE DIRECT REDUCTION AND REDUCTION SMELTING PROCESSES A.Markoti}*, N.Doli}* and V.Truji}** * Faculty of Metallurgy, Aleja narodnih heroja 3, 44 103 Sisak, Croatia ** Copper Institute, Bor, Yugoslavia (Received 5 October 2002; accepted 24 December 2002 ) Abstract For quite a long time efforts have been made to develop processes for producing iron i.e. steel without employing conventional procedures – from ore, coke, blast furnace, iron, electric arc furnace, converter to steel. The insufficient availability and the high price of the coking coals have forced many countries to research and adopt the non-coke-consuming reduction and metal manufacturing processes (non-coke metallurgy, direct reduction, direct processes). This paper represents a survey of the most relevant processes from this domain by the end of 2000, which display a constant increase in the modern process metallurgy. Keywords: iron, coal, direct reduction, reduction smelting, main processes, reduction. 1. Introduction The processes that produce iron by reduction of iron ore below the melting point of the iron produced are generally classified as direct reduction processes, and the product is referred to as direct reduced iron. The processes that produce molten metal, similar to blast furnace liquid metal, directly from ore are referred to as direct smelting processes. In some of the processes the objective is to produce liquid steel directly from ore and these processes are classified as direct steelmaking processes. J. Min. Met. 38 (3 ‡ 4) B (2002) 123 A. Markoti} et al. These broad categories are clearly distinguished by the characteristics of their respective products, although all of these products may be further treated to produce special grades of steel in the same steelmaking or refining process [1].
    [Show full text]
  • NASSAWANGO IRON FURNACE Ca1828-1850 NEAR SNOW HILL, MARYLAND
    NASSAWANGO IRON FURNACE ca1828-1850 NEAR SNOW HILL, MARYLAND A NATIONAL HISTORIC MECHANICAL ENGINEERING LANDMARK OCTOBER 19, 1991 The American Society of Mechanical Engineers FURNACE DelMarVa Group TOWN Nassawango Iron Furnace HISTORY OF NASSAWANGO IRON FURNACE Bog iron was first discovered in the swamps produced over 700 tons of pig iron per year at along Nassawango Creek in the 1780’s and in Nassawango; Spence was also credited with 1828 the Maryland Iron Company was the installation of the hot-blast stove on top of incorporated to extract and process it. In the furnace. 1830, the Company constructed a furnace along the creek at a point roughly four miles Iron was produced at Nassawango until 1847 northwest of its confluence with the when lack of labor and poor market Pocomoke River near Snow Hill, MD. Shortly conditions caused Spence (who fell into thereafter, the Nassawango furnace began financial ruin) to shut down the furnace. The producing pig iron by the cold-blast process. property sat idle from that time forward and was used by successive owners mostly for In 1836, two of the Company’s creditors, the timber rights. In 1962, the heirs of Arthur Milby and Joseph Waples, foreclosed Georgia Smith Foster donated the property to on the property; that same year they sold it to the Worcester County Historical Society Benjamin Jones, a Philadelphia ironmonger. which undertook a systematic long range Jones, who owned other furnaces and had a program to stabilize the furnace and cut back formidable business that bought and sold the plant growth of the previous 100 years.
    [Show full text]
  • Energy Efficiency Improvement and Cost Saving Opportunities for the U.S
    LBNL-4779E ERNEST ORLANDO LAWRENCE BERKELEY NATIONAL LABORATORY Energy Efficiency Improvement and Cost Saving Opportunities for the U.S. Iron and Steel Industry An ENERGY STAR® Guide for Energy and Plant Managers Ernst Worrell, Paul Blinde, Maarten Neelis, Eliane Blomen, and Eric Masanet Environmental Energy Technologies Division Sponsored by the U.S. Environmental Protection Agency October 2010 Disclaimer This document was prepared as an account of work sponsored by the United States Government. While this document is believed to contain correct information, neither the United States Government nor any agency thereof, nor The Regents of the University of California, nor any of their employees, makes any warranty, express or implied, or assumes any legal responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by its trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof, or The Regents of the University of California. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof, or The Regents of the University of California. Ernest Orlando Lawrence Berkeley National Laboratory is an equal opportunity employer. LBNL-Report Energy Efficiency Improvement and Cost Saving Opportunities for the U.S. Iron and Steel Industry An ENERGY STAR® Guide for Energy and Plant Managers Ernst Worrell, Paul Blinde, Maarten Neelis, Eliane Blomen, and Eric Masanet Energy Analysis Department Environmental Energy Technologies Division Ernest Orlando Lawrence Berkeley National Laboratory University of California Berkeley, CA 94720 October 2010 This work was funded by U.S.
    [Show full text]
  • Hot Stove Oxygen-Enriched Combustion in an Iron-Making Plant
    The Swedish and Finnish National Committees of the International Flame Research Foundation – IFRF HOT STOVE OXYGEN-ENRICHED COMBUSTION IN AN IRON-MAKING PLANT Chuan Wang1,*, Andy Cameron2, Axel Bodén1, Jonny Karlsson3, Patrick Lawrence Hooey1,4 1,*Centre for process integration in steelmaking Swerea MEFOS, Luleå, Sweden [email protected] 2Linde Gas, The Priestley Centre, 10 Priestley Road Guildford, Surrey England [email protected] 3SSAB EMEA Luleå Sweden [email protected] 4University of Oulu (Adjunct Professor) Oulun Yliopisto Finland * corresponding author ABSTRACT The presented paper investigates the application of oxygen-enriched combustion in hot stoves in an iron-making plant. The enriched oxygen is used to reduce the consumption of the high calorific value gas of COG while maintaining the same flame temperature in the hot stoves as the reference case. The investigation is carried by using a spreadsheet hot stove model. Compared to the conventional oxygen-enriched combustion, higher stove efficiency can be achieved when heat exchanger is installed to recover the sensible heat in flue gas by preheating combustion air and BFG; higher stove efficiency can also be achieved when parts of flue gas are recirculated to hot stoves. For the studied plant, it indicates that heat exchanger has a better effect than flue gas recirculation in terms of stove efficiency. However, it has been noticed that flue gas recirculation can help to concentrate CO2 content in the flue gas, which will be essential for the carbon capture in the BF iron-making process. Keywords: oxygen-enriched; hot stoves; blast furnace (BF); flue gas recirculation 1.
    [Show full text]
  • On the Application of the Hot Blast, in the Manufacture of Cast- Iron. by THOMAS CLARK, M. D., Professor of Chemistry in Marischal College, Aberdeen
    ( 373 ) On the Application of the Hot Blast, in the Manufacture of Cast- Iron. By THOMAS CLARK, M. D., Professor of Chemistry in Marischal College, Aberdeen. (Read Uth March 1835J AMONG persons interesting themselves in the progress of Bri- tish manufactures, it can scarce fail to be known, that Mr NEIL- SON of Glasgow, manager of the Gas Works in that city, has taken out a patent for an important improvement in the working of such furnaces as, in the language of the patent, " are supplied with air by means of bellows, or other blowing apparatus." In Scotland, Mr NEILSON'S invention has been extensively applied to the making of cast-iron, insomuch that there is only one Scotch iron-work where the invention is not in use, and in that work, apparatus is under construction to put the invention into operation. Apart from the obvious importance of any consider- able improvement in the manufacture of so valuable a product as cast-iron, the invention of Mr NEILSON would merit attention, were it only for the singular extent of the improvement effected, compared with the apparent simplicity—I had almost said inadequacy—of the means employed. Having therefore, by the liberality of Mr DUNLOP, proprietor of the Clyde Iron-Works, where Mr NEILSON'S invention was first put into operation, ob- tained full and free access to all information regarding the results of trials of the invention in those works, on the large scale of manufacture, I cannot help thinking that an authentic notice of these results, together with an attempt to explain the cause of them, will prove acceptable to the Royal Society of Edinburgh.
    [Show full text]
  • Making ^Anthracite Iron N the Eighteenth Century Charcoal Was the Principal Fuel Used for Smelting Iron
    discovery of the ^Process for (^Making ^Anthracite Iron N THE eighteenth century charcoal was the principal fuel used for smelting iron. When in the course of time the demand for I iron increased and the hardwood forests used for making charcoal became smaller, ironmasters looked for other fuels. In Britain and continental Europe they turned to soft coal, which was generally located near deposits of iron ore and from which coke could be made. Anthracite deposits were more scarce. Only a few of the many blast furnaces in Europe—those located near the veins of anthracite—would benefit if a way could be found to use this "stone coal/' as anthracite was then commonly called.1 The situation in the United States was far different, with the development of an entire industry at stake. Deposits of bituminous coal lay for the most part beyond the mountains, far from the centers of population and the extant means of transportation. The iron-rich ridges and valleys of eastern Pennsylvania and New Jersey, however, lay near extensive fields of anthracite. The canals which penetrated into the anthracite regions in the second quarter of the nineteenth century linked cities, towns, and deposits of iron ore, limestone, and anthracite like beads on a chain, 1 The first description of the discovery of the anthracite process appeared in 1841 in the form of a book and may have helped to advertise the process among ironmasters: Walter R. Johnson, Notes on the Use of Anthracite in the Manufacture of Iron with Some Remarks on Its Evaporating Power (Boston, 1841).
    [Show full text]
  • Optimization of Blast Furnace Parameters Using Artificial Neural Network
    View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by ethesis@nitr Optimization of blast furnace parameters using artificial neural network A THESIS SUBMITTED IN PARTIAL FULLFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF Master of Technology In Metallurgical and Materials Engineering (Steel Technology) By Dhirendra Kumar Roll No- 213MM2479 Department of Metallurgical and Materials Engineering National Institute of Technology Rourkela-769008 May’2015 Optimization of blast furnace parameters using artificial neural network A THESIS SUBMITTED IN PARTIAL FULLFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF Master of Technology In Metallurgical and Materials Engineering (Steel Technology) By Dhirendra Kumar Roll No- 213MM2479 Under the Guidance of Dr S. K. Sahoo Department of Metallurgical and Materials Engineering National Institute of Technology Rourkela-769008 May’2015 National Institute of Technology Rourkela CERTIFICATE This is to certify that the work in this thesis report entitled “Optimization of blast furnace parameters using artificial neural network” which is being submitted by Mr. Dhirendra Kumar (Roll no: 213MM2479) of Master of Technology, National Institute of Technology Rourkela, has been carried out under my supervision in partial fulfilment of the requirements for the degree of Master of Technology and is an original work. To the best of my knowledge, the matter embodied in the thesis has not been submitted to any other University / Institute for the award of any Degree or Diploma. Prof. S. K. Sahoo Department of Mechanical Engineering National Institute of Technology, Rourkela-769008 ACKNOWLEDGEMENT With deep regards and profound respect, I avail this opportunity to express my deep sense of gratitude and indebtedness to Dr S.K.
    [Show full text]