ANNUAL REPORT 2002 DEPARTMENT OF PROCESS AND ENVIRONMENTAL ENGINEERING Laboratory of Process Metallurgy ANNUAL REPORT 2002 Editor: MARKO PETÄJÄJÄRVI UNIVERSITY OF OULU LABORATORY OF PROCESS METALLURGY P.O. BOX 4300 FIN-90014 UNIVERSITY OF OULU OULU UNIVERSITY PRESS OULU 2003 3 4 ANNUAL REPORT 2002 LIST OF USED ABBREVIATIONS AOD Argon Oxygen Decarburization; Converter used for stainless steelmaking by Avesta Polarit BF Blast Furnace BOF Basic Oxygen Furnace CFD Computational Fluid Dynamics CMU Carnagie Mellon University CRC Chrome Converter; Converter used for stainless steelmaking by AvestaPolarit D.Phil. (Geol. Min.) Doctor of Philosophy (Geology and Mineralogy) D.Sc. (Tech.) Doctor of Technology, Dr. Tech. EDS-SEM Energy Dispersive Spectrometer - Scanning Electron Microscope GSCE Graduate School in Chemical Engineering (Academy of Finland) HUT/TKK Helsinki University of Technology ISIJ Iron and Steel Institute of Japan KTH Kungl Tekniska Högskolan Lic. (Tech.) Licentiate of Science (Technology) LD-KG Linz-Donau - Kawasaki Gas; Basic Oxygen Furnace (converter) used for steelmaking by Rautaruukki Steel M.Sc. (Chem.) Master of Science (Chemistry) M.Sc. (Geol. Min.) Master of Science (Geology and Mineralogy) M.Sc. (Math) Master of Science (Mathematics), M.Sc. (Tech.) Master of Science (Technology), M.Sc.Eng, Dipl.Eng. NTNU Norges teknisk-naturvitenskepelige universitet ANNUAL REPORT 2002 5 SEM Scanning Electron Microscope TEKES National Technology Agency of Finland TGA-DTA Thermogravimetry and Differential Thermal - Analyzer XRD X-ray Dissruction Spectrometer VTT Technical Research Centre of Finland PGM Platinum-group minerals PGE Primary platinum-group elements (Ru, Rh, Pd, Os, Ir, Pt) EOL Institute of Electron Optics EFTEM Energy Filtered Transmission Electron Microscope FESEM Field Emission Scanning Electron Microscope STEM Scanning Transmission Electron Microscope EPMA Electron Probe Microanalyzer DCP-AES Direct Current Plasma Atomic Emission Spectrometry ICP-AES Induction Coupled Plasma Atomic Emission Spectrometry ICP-MS Induction Coupled Plasma Mass Spectrometry OES Optical Emission Spectroscopy OMBKE Hungarian Metallurgical and Mining Society IOM Institute of Materials IISI International Iron and Steel Society ESIC European Steel Institutes Federation SINTEF The Foundation for Scientific and Industrial Research at the Norwegian Institute of Technology SIMS Scandinavian Simulation Society 6 ANNUAL REPORT 2002 PREFACE The year 2002 was the eleventh full calendar year in the history of the Process Metallurgy professorship. During those years the professorship has exceeded both the education and research goals established upon foundation. Over 60 Diploma Engineers have qualified and 12 Licentiates of Science and Doctors have graduated.The number of graduates exceeded 100 in 2002, if those that attended the special courses of updating training, during 1989-1991, are included in the count. These hundred graduates are placed, as a rule, along the coast of the Gulf of Bothnia in the services of the metallurgical industry (AvestPolarit, Rautaruukki, Outokumpu).The professorship education has thus alleviated the shortage of engineers within the industry in accordance with foundation aims. Research activities have over the last three years been very lively.The most important reason for this has been TEKES’s technology programme “Frontiers of Metallurgy”. Within this framework and with the support of the industry, over half the laboratory’s external research funding has come from this technological programme. At its height the laboratory’s workforce totalled 46 during 2002. The laboratory’s research commitments have continued unbroken over several years, so that the reces- ANNUAL REPORT 2002 sion that has troubled industry has not for the time being affected our operations in its extensiveness. During the past year the increase in projects relating to environmental questions was clearly discernible. It is presumable that the university’s focal point: environmental technology and accordingly process metallurgy research will in future be, more than ever, strongly directed towards minimizing the environmental effects of the industry. The laboratory has actively taken part in the development of both teaching and research activities of the Department of Process and Environmental Engineering. At departmental level also we metallurgists experience as our goal the creation of a unified, open and functional department. The possibility of our own active development enables collaboration that has been and will be good also in the future. We have in 2002 once again succeeded exceptionally in our actions. Thanks to all our personnel – I am proud of you! Jouko Härkki Professor Head of the Laboratory 7 8 ANNUAL REPORT 2002 TABLE OF CONTENTS Page LIST OF USED ABBREVIATIONS 4 PREFACE 6 TABLE OF CONTENTS 8 1 LABORATORY STAFF AND STUDENTS 12 2 EDUCATIONAL ACTIVITIES 16 2.1 University Courses Held by the Laboratory 16 2.1.1 Metallurgical Processes 16 2.1.2 Metallurgical Thermodynamics 17 2.1.3 Theory of Pyrometallurgical Processes 17 2.1.4 Laboratory Working 17 2.1.5 Casting and Solidification 18 2.1.6 Construction Materials of High Temperature Processes 18 2.1.7 Steel Industry’s Challenges 18 ANNUAL REPORT 2002 9 Page 3 RESEARCH ACTIVITIES 3.1 Reduction Metallurgy 19 20 3.1.1 Development of the Steel Belt Sintering Technology for Ferroalloys 20 3.1.2 PANAMA 21 3.1.3 Reduction of Chromites 21 3.1.4 Control of BF Hearth and Tuyere Level Operation and Extension of Hearth Duration 24 3.1.5 Coke 25 3.1.6 OPTIDUST II 26 3.2 Refining Metallurgy 27 3.2.1 CONVERTO 27 3.2.2 TASK 29 3.2.3 AHA 30 3.2.4 Inclusion Control 31 3.2.5 INGROS 3.2.6 TTJV 32 33 3.2.7 MMX 34 10 ANNUAL REPORT 2002 TABLE OF CONTENTS Page 4 RESEARCH DEVICES AND ANALYTIC INSTRUMENTS 4.1 High Temperature Devices 35 35 4.1.1 TGA 35 4.1.2 High Temperature Viscosimeter 36 4.1.3 Finger Test Device 36 4.1.4 Optical Dilatometer 36 4.1.5 Gradient Furnace 37 4.1.6 Pressure Furnace 37 4.1.7 Alkali Test 37 4.2 Other Devices 38 4.2.1 Watermodels 38 4.2.2 Coulter Omnisorp 360 cx 38 4.2.3 Computational Fluid Dynamics Software 38 4.2.4 Thermodynamic Calculation Programmes 38 4.2.5 Gas Chromatograph 38 4.2.6 Microscopes 38 4.2.7 Materialographic Surface Preparation of Solid Materials 39 4.3 Other Available Facilities 40 ANNUAL REPORT 2002 11 Page 5 PUBLICATIONS 2002 41 5.1 Papers 41 5.2 Conferences and Symposiums 42 5.3 Reports 43 5.4 Annuals and Final Reports 44 6 THESIS 45 6.1 Licenciate in Technology Theses 45 6.2 Diploma Engineer Theses (Master of Science in Technology) 45 7 CONFERENCE VISITS 46 8 LABORATORY FREE-TIME ACTIVITIES 47 9 CONTACT INFORMATION 49 Map of the University of Oulu 50 12 1 ANNUAL REPORT 2002 LABORATORY STAFF AND STUDENTS Academic Staff Härkki, Jouko D.Sc. (Tech.), Professor, Head of the Laboratory Taskinen, Pekka D.Sc.(Tech.), Docent in thermodynamics, Outokumpu Research Centre, Pori Seppänen, Matti D.Sc.(Tech.), Docent in processmetallurgy, Rautaruukki Steel, Raahe Heinänen, Kyösti D. Phil (Geol. Min.), Docent in mineralogy, Rautaruukki Steel, Raahe Jonsson, Lage D.Sc.(Tech.), Docent in macro modelling, Luleå, Sweden Heino, Jyrki Lic. (Tech.), Senior Assistant Heikkinen, Eetu-Pekka Lic.(Tech.), Assistant Kallio, Sauli M.Sc.(Geol. Min.), Part-time teacher Kokkonen, Tommi M.Sc.(Chem.), Part-time teacher Makkonen, Hannu M.Sc.(Geol. Min.), Part-time teacher Mattila, Riku M.Sc.(Tech.), Part-time teacher Paananen, Timo M.Sc.(Tech.), Part-time teacher Tanskanen, Pekka M.Sc.(Geol. Min.), Part-time teacher Angerman, Mikko Student, Part-time teacher Ikäheimonen, Topi Student, Part-time teacher Virtanen, Esa Student, Part-time teacher Teachers from the Industry Hooli, Paavo M.Sc. (Tech.), Part-time teacher, AvestaPolarit, Tornio Päätalo, Mika M.Sc. (Tech.), Part-time teacher, AvestaPolarit, Tornio Co-lecturers: Researchers from the laboratory, Rautaruukki Steel and AvestaPolarit ANNUAL REPORT 2002 Researchers Angerman, Mikko Student, Project Manager Aspegren, Pasi M.Sc. (Tech.) Erkkilä, Helena M.Sc. (Tech.), MGS, Project Manager Fabritius, Timo Lic. (Tech.), Special Researcher, Research Manager Fedory, Paul Exchange Student Gornostayev, Stanislav S. Ph.D. Harju, Markus M.Sc. (Math.) Heikkinen, Eetu-Pekka Lic. (Tech.) Hiltunen, Rita M.Sc. (Geol. Min.) Huttunen, Satu M.Sc. (Chem.), GSCE, Leave of absence. Höynälä, Arto M.Sc. (Phys.) Kallio, Kimmo M.Sc. (Tech.), Project Manager, GSCE Kallio, Sauli M.Sc. (Geol. Min.), Researcher Luomala, Matti M.Sc. (Tech.), Project Manager, GSCE Makkonen, Hannu M.Sc. (Geol. Min.), Project Manager Mattila, Olli M.Sc. (Tech.), Project Manager, GSCE Mattila, Riku M.Sc. (Tech.) Määttä, Hanski M.Sc. (Tech.) Paananen, Timo M.Sc. (Tech.), Researcher Rantapirkola, Kristian Sippola, Jukka Student Talonen, Anna-Maija M.Sc.(Chem.) Tang, Yong Dr. (Tech.) Tanskanen, Pekka M.Sc. (Geol. Min.), Project Manager 13 14 ANNUAL REPORT 2002 Research Assistants Aho, Jani Student Hekkala, Lauri Student Ikäheimonen, Topi Student Kaijalainen, Antti Student Kokkonen, Tommi M.Sc. (Chem.) Kurkinen, Petri Student Kyllönen, Toni Student Leinonen, Virpi Student Mure, Petri Student Mäenpää, Jani1 Student Olenius, Elina Student Petäjäjärvi, Marko Student Pöyhtäri, Samuli Student Siivola, Tero Student Virtanen, Esa Student Vähäoja, Pekka Student Diploma Thesis Workers Franssila Laura Karjalainen, Eveliina Hekkala, Lauri Leinonen, Mervi Halmeenpää, Riina Mure, Petri Hurme, Rauno Mäenpää, Jani Isokääntä, Jani Olenius, Elina Kangas, Jyrki Siivola, Tero Karhulahti, Timo Sola, Petri Karekivi, Pasi Virtanen, Esa ANNUAL REPORT 2002 15 Technical Staff Kokkonen, Tommi M.Sc. (Chem.), Research Assistant Luukkonen, Jarno Laboratory Technician Mattila, Riku M.Sc.(Tech.), Laboratory Manager Penttinen, Jorma Special Laboratory Technician, part-time Virkkala, Jouko Laboratory Technician Administration Zinovjev, Berith Project Secretary, Financial Manager Puolakka, Ritva Secretary, part-time Heikkinen, Kaisa Secretary, Web-master, part-time Postgraduate Students Erkkilä, Helena (in MGS) Luomala, Matti (in GSCE) Fabritius, Timo Makkonen, Hannu Heikkinen Eetu-Pekka Mattila, Olli (in GSCE) Heino, Jyrki Mattila, Riku Hiltunen, Rita Niemi, Tommi Huttunen, Satu (in GSCE) Paananen, Timo Kallio, Kimmo (in GSCE) Tanskanen, Pekka New students from 1.9.2002 Ajanki, Teemu Pieksä, Vesa Kangas, Ossi Pyykkönen, Juha Kasala, Markku Rainto, Ilkka Liisanantti, Ville Tauriainen, Jukka Mansikka, Jukka Tuominen, Petri Pekki, Mikko 16 2 ANNUAL REPORT 2002 EDUCATIONAL ACTIVITIES Eetu-Pekka Heikkinen As a part of the Department of Process and Environmental Engineering, the Laboratory of Process Metallurgy organizes its education in a way that serves the educational objectives of the whole department as well as possible while trying to fulfil the goals of its own strategy at the same time. The primary goal of the laboratory’s education is to educate people with masters’ and doctoral degrees (M.Sc.Eng. and D.Sc.Tech.) into the service of metallurgical industry whereas the department’s aims are to equip students with the ability to understand, model and control the phenomena inside the processes no matter what the process in question is. In order to achieve the understanding and control of the processes, many general skills in favour of special knowledge are emphasized in the education.These general skills include fundamental knowledge of natural sciences, problem solving skills and ability to approach problems from different viewpoints and to apply general knowledge to different matters. Although the emphasis of the laboratory’s education is in the metallurgical processes of iron, steel and ferroalloys production, the aims of the laboratory and the department are not contradictory, because it is not the laboratory’s only goal to teach people to understand the metallurgical processes as thoroughly as possible. It is equally important to give students different viewpoints and perspectives to the phenomena and problems concerning metallurgical processes as well as other challenges which a freshly graduated M.Sc.Eng. may encounter in his or her future job. From this point of view the aims of the laboratory are in good accord with the aims of the whole department. It is noteworthy that students graduating from the laboratory of process metallurgy are primarily experts in process engineering. For them process metallurgy is a subject to which general knowledge of process engineering is applied; not the main focus itself. 2.1 UNIVERSITY COURSES HELD BY THE LABORATORY 2.1.1 Metallurgical Processes Metallurgical processes is the laboratory’s only course which is directed at all the students of process; not just the metallurgists. The aim of the course is to teach students the fundamentals of the metallurgical unit processes and metal production ANNUAL REPORT 2002 17 in Finland as well as the basics of thermodynamics and its applications in metallurgy. Some environmental aspects are considered, too. Although the emphasis of the laboratory’s education is on the production of iron, steel and ferroalloys, the production of other metals (e.g. copper, nickel, zinc and aluminium) is also considered during this course. The course is carried out with lectures, exercises and industrial excursions which are directed either at Rautaruukki’s steel works in Raahe or at AvestaPolarit’s steel works in Tornio.The course was lectured in 2002 by Senior Assistant Jyrki Heino (Tech.Lic.), Researcher Timo Paananen (M.Sc.Eng.) and Professor Jouko Härkki (D.Sc.Tech.). 2.1.2 Metallurgical Thermodynamics The aim of the course is to equip the students with tools that are needed while examining the phenomena inside metallurgical processes in the forthcoming courses. It means that after this course students are required to have a sufficient knowledge of physical chemistry for thermodynamic calculations which involve gas and liquid (slag and metal) phases. The most important topics are thermodynamics of solutions, phase diagrams and the use of commercial software in thermodynamic equilibria calculations. The course was lectured in 2001-2002 by Assistant Eetu-Pekka Heikkinen (Tech.Lic.) and Researcher Hannu Makkonen (M.Sc.Geol.Min.) and in 2002-2003 by Assistant Eetu-Pekka Heikkinen (Tech.Lic.) and Part-time Teacher Topi Ikäheimonen. 2.1.3 Theory of Pyrometallurgical Processes During this course the phenomena inside the pyrometallurgical processes are considered using thermodynamics, kinetics, heat transfer, mass transfer and fluid dynamics. The purpose of education is not only to teach metallurgy, but also develop students’ ability to present their ideas and opinions both literally and verbally. The course is carried out with lectures, seminars and industrial excursions which are directed at Rautaruukki’s and AvestaPolarit’s steel works in Raahe and Tornio. The course was lectured in 2002 by Professor Jouko Härkki (D.Sc.Tech.) and researchers from the laborator y; e.g. Timo Fabritius (Tech. Lic.) and Pekka Tanskanen (M.Sc.Geol.Min.). 2.1.4 Laboratory Working Until 2001, laboratory exercises were a part of the “Theory of pyrometallurgical processes” -course.The purpose of the course is to teach students how experimental laboratory scale research is carried out by using the experimental equipment at 18 ANNUAL REPORT 2002 the university and industry’s research centres. In addition to this, some safety aspects are considered during the lectures. The course was lectured in 2002 by Research Assistants Esa Virtanen and Tommi Kokkonen (M.Sc.Chem.) as well as Laboratory Manger Riku Mattila (M.Sc.Eng.).The exercises were supervised by Researchers Sauli Kallio (M.Sc.Geol.Min.) and Timo Paananen (M.Sc.Eng.). 2.1.5 Casting and Solidification The aim of the course is to equip students with the ability to study casting and solidification using both phenomenon- and process-based viewpoints.The contents of this course have been updated and kept close to practice due to skilled lecturers from the industry. In 2002 the course was lectured by Paavo Hooli (M.Sc.Eng.) and Mika Päätalo (M.Sc.Eng.) from AvestaPolarit Stainless. 2.1.6 Construction Materials of High Temperature Processes This course is focused on ceramic refractory materials and their use as construction materials in metallurgy and other high temperature processes.The aim of the course is to present different kind of refractory materials, their physical and chemical properties as well as interaction mechanisms between refractories and metallurgical melts (slag and metal). The course was lectured in 2002 by Researcher Hannu Makkonen (M.Sc.Geol.Min.) and Professor Jouko Härkki (D.Sc.Tech.). 2.1.7 Steel Industry’s Challenges The aim of the last course of metallurgy is to represent metallurgical processes and industry as a part of a larger economic-technical environment in which environmental aspects are also considered. The contents feature for example main ideas of technology roadmaps, challenges of metallurgical research and development, review of the development state of alternative metallurgical processes, steel industry’s effects on the environment and visions of future business environment of the steel industry. In 2002 the course was lectured by Researcher Mikko Angerman, Professor Jouko Härkki (D.Sc.Tech.) and several lecturers from the industrial field. The use of visiting lecturers ensures that the contents of the course are always updated and close to practice. ANNUAL REPORT 2002 3 19 RESEARCH ACTIVITIES Timo Fabritius The research activities of the Laboratory of Process Metallurgy contain the whole process chain of steelmaking focusing on the process units where steel is not yet solidified (blast furnace, converter, ladle, continuous casting). The research actions in the Laboratory of Process Metallurgy have divided into three divisions: reduction metallurgy, refining metallurgy and refractory materials. Furthermore, the research activities on the field of high temperature chemistry of recycling and waste treatments have increased during year 2002. Detailed information of research subjects is presented in the following chapter. Developing and building of research devices and analytical instruments for laboratory experiments was furthermore one of the most important investment targets. Now we have good possibilities to carry out many kind of metallurgical experiments as well as numerical simulations of fluid flows and thermodynamic equilibrium calculations. The year 2002 was economically difficult for the metallurgical industry and this showed in decreased financing of academic research. Several research projects finished at the end of last year and the accumulation of scientific knowledge and competence of research groups became complicated. Despite that, the production of scientific publications in referee journals increased remarkably amongst the whole research personnel. Some doctoral theses are awaiting graduation during the forthcoming year. Despite of above-mentioned difficulties, the near future looks quite positive because scientific knowledge and competence in the peak research areas have further strengthened. 20 3.1 ANNUAL REPORT 2002 REDUCTION METALLURGY 3.1.1 Development of the Steel Belt Sintering Technology for Ferroalloys Project Manager: Timo Fabritius Researcher: Lauri Hekkala Research Assistant: Elina Olenius The steel belt sintering technology is used for manufacturing chromite pellets that are charged in the smelting furnace for ferrochromium production. Hot air is blown through the moving bed of raw pellets. Direct temperature and flow measurements are difficult to do in the bed of a real scale belt sintering process.Therefore, a tested and reliable mathematical model would be a valuable help for optimising operational parameters of the process and designing new constructional improvements. The aim of this project was to present a mathematical model that calculates the gas flow and temperature distribution in the bed of pellets and the atmosphere. Computational fluid dynamics programme FLUENT is used to calculate the gas flow, composition and temperature of the gas in the sintering bed during processing. Lots of laboratory experiments (drying of pellets, specific heat and heat conductivity of pellets, oxidation of carbon and chromite etc.) were done for verification of the mathematical model. As a result of the project the simplified mathematical model, which takes account of all main chemical and physical phenomena, was developed. This 3-year co-operation project finished at the end of 2002. Picture 1. Comparison between measured and modelled gas temperature in batch sintering experiment with chemically inert and dry pellets. ANNUAL REPORT 2002 21 3.1.2 PANAMA Panama: Novel Analysis and Optimisation of Blast Furnace Burden Materials for Cost-Effective and High-Iron Capacity Production. Project Manager: Pekka Tanskanen Researchers: Sauli Kallio and Anna-Maija Talonen PANAMA is a subcontract project (1.7.2001-30.6.2004) for Rautaruukki Raahe Steel. Final target of this project is to develop a mineralogy-based optimization method for iron burden materials to enable more stable and cost-effective blast furnace operation. The research includes determination of the mineralogical evolution of ferrous burden in the blast furnace shaft. Further, formation and evolution of liquid slags from the cohesive zone down to the final blast furnace slag will be traced. A special issue of the project is to characterise the alkali capture of different solid mineral systems and the alkali retention capacity of different primary liquids.The alkali retention during the liquid evolution path to the final slag will be determined as well. The research is realised as laboratory-scale experiments. Different iron burden materials are used in the mineralogical part of the research.The chemistry mineralogy interrelations between the iron oxides and slag phases and the initial liquid formation are determined in equilibrium-state at certain reduction stages. The further evolution and properties of the liquid slags will be determined with synthetic slag systems.The research methods include chemical analysis, optical microscopy, TGA, SEM, XRD, DTA, viscometer, optical dilatometer, and thermodynamic equilibrium calculation. 3.1.3 Reduction of Chromites Project Manager: Rita Hiltunen The project was started on 15th of May 2000 and ended on 31st of December 2002. The project included two different sections, which were funded by TEKES. The Reduction Behaviour of Mg-poor Chromites of the Akanvaara Layered Intrusion, Northern Finland Project Manager: Rita Hiltunen The Akanvaara intrusion (surface area of 50-55 km2) in Savukoski, Northern Finland, hosts 23 distinct monocumulate layers of small euhedral chromite crystals enclosed in silicate matrix. Chromitite layers in Akanvaara intrusion have been divided into 22 ANNUAL REPORT 2002 four groups; UC (upper chromitite), ULC (uppermost lower chromitite) LC (lower chromitite) and LLC (lowermost lower chromitite). The driving force to investigate the Akanvaara chromites and their reduction behaviour originates from the very low content of MgO and relatively low content of Al2O3.Thus Akanvaara chromites have a unique quality which based on thermodynamics should facilitate the reduction. Another interesting feature is the high amount of V2O3 especially in the upper chromitite. The chromites included in this study are from the UC and ULC layers (24,9 % and 22,7 % Cr2O3 respectively).To get a better understanding of the reduction behaviour of the Akanvaara samples in comparison to Mg-bearing chromitites, Kemi chromite of the ferrochrome works in Tornio Finland, was included in the study as a reference material. Reduction experiments were isothermal in temperature range of 1000-1400˚C and in various atmospheres. Experiments were also conducted with coke addition in pellets and briquettes. According to the results of the reduction experiments complemented with microanalytical research, the Akanvaara chromites do reduce to a higher degree than Kemi chromite. Although the aim of the study was to characterize the mechanisms of reduction focused on gas-solid-reactions, the nature and the amount of the gangue minerals was such, that a considerable amount of slag phase was formed and effected reduction mechanisms extensively. Gangue minerals and structural features together with low MgO and high FeO content in both Akanvaara chromites are important factors resulting in better reducibility compared to Kemi chromite. Mineralogical Research on Chromites of the Akanvaara Deposit and Products of their Processing with Emphasis on PGM/PGE Researcher: Stanislav Gornostayev The objectives of this project were: to re-examine selected samples of chromite ore from Akanvaara on platinum-group minerals (PGM), to determine their occurrence and nature and to see how the PGM, if any, behave under the conditions originally set for processing and reduction of the ores. The main research tools were: optical microscope, SEM/EDS with Jeol JSM-6400 (University of Oulu) and Cameca SX-50 microprobe with TURBO-SCAN programme (Geological Survey of Finland). It was found that the metallurgical-type chromite ores of Akanvaara contain a range of PGM. The mineralogy, mineral chemistry and mineral assemblages of PGM indicate primary platinum-group elements (PGE: Ru, Rh, Pd, Os, Ir, Pt) fractionation and ANNUAL REPORT 2002 23 late-stage PGE redistribution within the deposit and, possibly, the extent of PGE mineralization outside the intrusive body. The investigations of chromite concentrates have shown that the amount of PGM in the concentrates is less than in ore samples. Detailed study of reduced chromite pellets have led to a conclusion that the PGM may have been oxidized during sintering process. Picture 2a. Crystal of RuS2. Scale bar 10 um. Picture 2b. Two-phase grain of Pt3Fe (white) and Rh2S3 (grey). Scale bar 6 um. Pictures 2a and 2b. The platinum-group minerals in chromite from the Akanvaara deposit. Selected results of the project together with data on reduction behaviour of the ores obtained earlier have been presented at the international conference Applied Mineralogy’03. 24 ANNUAL REPORT 2002 3.1.4 Control of BF Hearth and Tuyere Level Operation and Extension of Hearth Duration Project Manager: Olli Mattila (chemical reactions in the hearth) Researcher: Hanski Määttä (wear of lining material) Project started on 1st of January 1999 and ended on 30th of April 2002.The goal of the project was to control the blast furnace hearth and to increase the life time of the hearth. Additional goals were to develop new models to control the blast furnace tuyere level, to estimate the wear of blast furnace and to predict the hearthcoke voidage and to develop an expert system of blast furnace tapping strategy. Three complementary laboratories were involved in the project, due to the complicity of the process and the challenging nature of measurements and control engineering involved. The competence areas of these three laboratories were automation and modelling (Control Engineering, University of Oulu), heat engineering and modelling (Heat Engineering, Åbo Akademi) and chemical metallurgy (Process Metallurgy, University of Oulu). In the project, phenomena in the lower region of a blast furnace were investigated with thermodynamical calculation and pressure-furnace experiments. Melt flows on a blast furnace hearth had been investigated with physical modeling and in the cases of floating and sitting deadman the results were compared with the numerical model made at Åbo Akademi.Taking into account the flows on a blast furnace hearth, the wear of lining material and shielding of the blast furnace were investigated by using thermodynamic calculations and chemical stress experiments. It was found that in the case of floating deadman the iron melt flows completely in the coke bed only through the V-shaped area. In case of sitting deadman iron melt flows completely through the coke bed. The wear tendency of hearth lining materials increase in the order of carbon-brick, semigraphite and graphite and the wear rate of lining material is affected mostly by carbon content of metal phase -silicon and manganese content have only a little influence. In the pressure furnace experiments it was found that through the interfacial turbulence high FeO-content of slag promotes sulphur transfer from metal to slag but decreases the thermodynamic equilibrium value of maximum sulphur transfer with carbon unsaturated and pressurised conditions. Metal carbon content has significant influence on sulphur transfer, which was expected also from the thermodynamic point of view. ANNUAL REPORT 2002 25 3.1.5 Coke Coke:The Behaviour and Properties of Coke in a Blast Furnace and in a Cupola Furnace Project Manager: Olli Mattila Researcher: Stanislav Gornostayev Research Assistant: Tommi Kokkonen The project started on 1st of May 2002 and will end on 30th of April 2005.The main target of this project is to increase coke production and improvement of costeffectiveness of coke production and decrease the reducing agent (coke, oil) consumption in BF. Additional targets are to increase knowledge in Finland and in Northern countries in the field of coke structures and the behaviour of coke in BF and to develop methods to analyse coke behaviour straight from the process data. Laboratory of process metallurgy will study the structural changes of coke and the main factors causing those changes as the coke moves downwards in the BF process. An additional task is to study the behaviour of coke in contact with slag and metal e.g. how the mineral particles revealed to the surface of coke will be detached as slag.The project is divided into two parts. In the first part the behaviour of coke is studied in the conditions simulating BF conditions. The second part of this project will focus on coke-slag and coke-metal interaction. Two laboratories and two industrial partners are involved in the project: Laboratory of Process Metallurgy, Laboratory of Heat Engineering and Rautaruukki Oyj, Paroc Group Oyj respectively. Coke research in Sweden is monitored through Jernkontoret’s meetings. 26 ANNUAL REPORT 2002 3.1.6 OPTIDUST II OPTIDUST II - environmentally friendly utilization of dusts, sludge, scraps and skulls of Raahe and Koverhar steel plants in hot metal production Project Manager: Hannu Makkonen Researchers: Hannu Makkonen, Eetu-Pekka Heikkinen and Sirpa Kokko Picture 3. Optidust II logo. The project started on 1st of January 2002 and will be concluded on 31st of December 2004. OPTIDUST was a preliminary project, in which Rautaruukki Group’s and SKJ companies recycling questions and aims were analyzed in order to establish a 3year industrial project. Sufficient results were obtained to continue with the second phase of the project now named as OPTIDUST II. The target is to evaluate and choose the most feasible and ecological recycling and utilization technique for Fundia Koverhar’s and Rautaruukki Steel’s problematic and unexploitable dusts, sludge, skulls, scrap fines and scales. The information obtained will be used as a basis for an industrial designing and selection project to increase Rautaruukki’s hot metal production. ANNUAL REPORT 2002 27 The project will use reduction trials of laboratory scale for the waste materials to assess the efficiency of certain recycling techniques in e.g. Zn removal. The products of the reduction tests will be analyzed chemically, physically and mineralogically in order to evaluate if the products can be utilized in iron production. Thermodynamic calculations complement the evaluation of different recycling methods. The harmful components (Zn, Pb, Na, K, Sn, Cd, As) are emphasized in the calculations. Furthermore, the project will collect data about cupola furnaces and rotary hearth furnaces, which are used for waste recycling. Partners in the project are National Technology Agency of Finland, Rautaruukki Group, SKJ Companies and Technical Research Centre of Finland. 3.2 REFINING METALLURGY 3.2.1 CONVERTO CONVERTO: Computational and Physical Modelling and Development of Control Systems for Converter Process Project Manager: Matti Luomala Research Assistants: Marko Petäjäjärvi, Antti Kaijalainen and Jani Mäenpää CONVERTO was a 3-year project funded by the National Technology Agency and the Finnish Steel Industry. It started on 1st of August 1999 and ended on 31st of July 2002. Participating organisations were the Laboratory of Metallurgy from Helsinki University of Technology and the Laboratory of Process Metallurgy and Control Engineering Laboratory from the University of Oulu. The first goal of this study was to clarify the interaction of the lance jet cavity with the bottom blowing plume and the sidewall blowing jet. Furthermore, the influence of the shape of lance cavity on the direction of splashes was determined. The research was carried out by using a so called simplified physical water model. According to the model tests, there existed three basic axioms in the interaction of the cavity with the bottom plume and sidewall jet. Firstly, when the bottom tuyere was located exactly underneath the lance jet, the shape of the cavity became lower than without bottom blowing. This turned the direction of splashes to lower trajectories. The analogous behaviour was found with sidewall blowing. Secondly, the total amount of splashing was constant and the ‘splashing nose’ was generated on the wall above 28 ANNUAL REPORT 2002 the bottom plume. Thirdly, both the plume and sidewall jet formed the protected zone beyond it. The larger the overlap of cavity and sidewall jet the larger the protected zone until the plume is exactly underneath the cavity.The model experiments showed clearly that the combination of bottom tuyeres and interaction of cavities and plumes have a very important role in splash generation in real converters. It is possible to decrease the wear of refractory lining at the trunnion area by optimizing the bottom and sidewall tuyere combination. Secondly, the effect of lance height, lance nozzle angle, lance position, top gas flow rate, bottom blowing and foamy slag on splashing and spitting behaviour in LD-KGconverter was investigated. A new cold model method for investigating the effects of the above-mentioned parameters on the location and quantity of liquid splashed on the walls of the model was utilised. According to the model tests, reduction of the nozzle angle increased the total amount of splashing and spitting considerably. Consequently, reduced productivity due to an increase in metal losses, skulling of the cone and converter mouth and further increased time for skull removal is expected. Introduction of bottom blowing increased splashing significantly on lower parts of the vessel. Lance position has an effect on total amount of splashing when bottom blowing is used. The presence of even minor foam layer on water surface reduced the amount of total splashing significantly. Thirdly, the effect of bottom nozzle arrangement and lance height on splashing and spitting in a combined blown converter were determined. According to the model tests, total splashing on the converter walls increased with the function of a number of bottom nozzles, both during the initial and final period of blowing. The nozzles arranged at the centre of the vessel increased metal losses and skulling of the converter cone especially at low lance heights. Using high lance gap and several bottom nozzles accelerated wear of the refractory, especially at the knuckle and charge pad areas. Finally, splashing and spitting behaviour, mixing efficiency and bath oscillation was studied with three different bottom nozzle configurations. Due to the different nature of the required measurements, two separate water models were utilised. Both models had the same geometry and dimensions (scaled down to 1:7). ANNUAL REPORT 2002 29 3.2.2 TASK TASK: Effective Blowing Practice for AOD-Converter Project Manager: Timo Fabritius Researchers: Petri Mure, Esa Virtanen and Petri Kurkinen (from the beginning of November) The aim for the project TASK is to develop techniques to achieve as efficient blowing practice as possible for the large scale 150-ton AOD-converter.The project began in the middle of the year 2001 and continued through to the year 2002. The implementation of an efficient blowing practice in the AOD needs that a large amount of gases can be blown into the steel melt in an intense but also controlled way.To achieve this, the facts having an effect on gas blowing and on its behaviour on steel melt has to be carefully scrutinized. Without this knowledge, there may become serious technical or economical problems for the user of an AOD-converter. Of course some basic principles can be applied also to the BOF-process. One important phenomenon for the usability of the vessel is an oscillation of the melt bath. Oscillation does not have a direct effect on the efficiency of process but enough strong oscillations may have a destructive effect on constructions of the AOD. From the economical point of view, the effective mass transfer between gas- and liquid phases is required to achieve both quick and efficient performance of the process. By using adequate gas blowing an efficient mix can be achieved in the meltphase when it is needed. Also the mass transfer from gas to melt can be controlled by proper blowing practice. Picture 4. Modelling of flows in the melt bath by using physical model tests. 30 ANNUAL REPORT 2002 During the year 2002 principles for the mass transfer between phases, theory of the oscillation of the melt bath and mixing properties of the melt were announced.The knowledge of these phenomena was to be deepened by process tests in the beginning of the year 2003. So far, the results have been promising and shown to be in good accordance with hypothesis made in the year 2002. The research was made by using knowledge based on literature, tests made with the watermodel of the AOD and combining all this information with previous results and experiences. 3.2.3 AHA AHA: Controlling of Atmosphere in the AOD-converter Project Manager: Timo Fabritius Researchers: Yong Tang and Esa Virtanen Research Assistants: Virpi Leinonen, Toni Kyllönen, Jani Aho and Topi Ikäheimonen The purposes of the project are to minimise the dissolution of nitrogen into the steel melt in the AOD-converter and to optimise the present “nitrogen model” of AOD to be less argon consumptive. This is possible to achieve by better control of atmosphere during decarburisation and slag reduction periods. The effects of circumstances on dissolution of nitrogen into steel melt and desorption from the melt will be established by thermodynamic equilibrium calculations. Temperature and the composition of steel melt (content of C, Fe, Cr, Mn and Si) and the gas phase change during processing.The effects of vessel geometry (vessel height, vessel diameter, cone diameter and cone angle) and gas flow rate in the upper part of the converter on dissolution of nitrogen from the atmosphere will be studied by CFD-model (Fluent). The financiers of the project are TEKES (National Technology Agency of Finland) and AvestaPolarit Stainless Oy. The duration time of the project is two years and the research started at the beginning of February 2002. ANNUAL REPORT 2002 31 Picture 5. Nitrogen distribution in the upper part of AOD and the hood with low argon flow rate from sidewall tuyeres. 3.2.4 Inclusion Control Inclusion Control: Inclusion Engineering for Better Quality Project Manager: Helena Erkkilä Researcher: Eetu-Pekka Heikkinen Partners: Rautaruukki, Fundia Wire, HUT, VTT, AvestaPolarit Stainless, Imatra Steel. Funding: TEKES, industry Inclusion control started on 1st of January 2002 and it will last until 31st of December 2003. The project is a follow-up to Oxide metallurgy (1998-2001) and TEVITE (1999-2001) projects. The main objective of the project is to develop and to apply thermodynamic equilibrium calculations to predicting and controlling the inclusion composition of steel, during ladle treatment and continuous casting. Multi-component equilibrium thermodynamics are linked with reaction kinetics. 32 ANNUAL REPORT 2002 3.2.5 INGROS INGROS: Inclusion Engineering and Grain Size Control of Steels Project Manager: Helena Erkkilä Partners: Elkem, ASA, Norway; SINTEF Materialteknologi, Norway; NTNU, Norway; Ovako Steel AB, Sweden; AB Sandvik Steel, Sweden; KTH, Sweden; Rautaruukki Oyj, Finland; Fundia Wire Oy Ab, Finland; HUT, Finland. Funding: Nordisk Industrifond The project started on 1st of January 2001 an will end on 31st of December 2003. The main idea behind this project is to establish the required basis for a formal collaboration between the Norwegian Ferroalloy industry and the steel industry in Sweden and Finland.This will be accomplished by initiating an innovation project on inclusion engineering and grain size control of steel along with a network project to promote the education and training of students and researchers with a multidisciplinary background within the field. Both projects build on the existing national programmes on ferroalloy and steel oriented research.Together the three Nordic countries Norway, Sweden and Finland provide a unique cluster of ferroalloy and steel manufacturing industry, end-users, research facilities and educational programmers, and this is also reflected in the project plans. 33 ANNUAL REPORT 2002 3.2.6 TTJV TTJV: Mould Powders for High Casting Speeds Project Manager: Kimmo Kallio Researchers: Marko Petäjäjärvi and Pasi Aspegren TTJV is a 3-year project which started on 1st of March 2001 an will end on 30th of April 2004 and is funded by Rautaruukki Oyj, AvestaPolarit Stainless Oy and TEKES (National Technology Agency of Finland). The aim of the project is to obtain better knowledge about mould powders and to achieve higher casting speeds and flawless surface quality in the steel industry. With higher casting speeds, cleaner and better surface quality steels need to be produced. The steel output can be increased with higher casting speeds, but at the same time the surface quality is reduced. Higher casting speed and better surface quality can be achieved by optimization of the mould powder composition. The most important properties of mould powders are considered with different laboratory scale devices: high temperature viscosimeter, DTA-TGA, optical dilatometer, hot stage microscope, XRD, XRF etc. In addition, plenty of industrial scale mould powder experiments, data collecting and analyses, are included. On the basis of the obtained results a better mould powder composition will be developed, at first for peritectic steel grade. Picture 6. From the top of the mould the mould powder forms a powder layer, then a sintered layer, a mushy layer, a carbon rich layer and eventually a pool of liquid slag. Between the steel shell and the mould the mould powder forms a liquid lubrication film layer and a solid layer, which consists of glassy and crystalline layers. (Sridhar 2000) 34 ANNUAL REPORT 2002 3.2.7 MMX Project Manager: Mikko Angerman Researchers: Markus Harju, Paul Fedory, Jukka Sippola, Samuli Pöyhtäri and Kristian Rantapirkola Project “Iron & Steel MMX” was financed by Finnish steelmaker Rautaruukki Group and National Technology Agency of Finland,TEKES.The project is part of the national technology programme “Frontiers in Metallurgy” conducted during the years 19992003. The MMX-project began in 03/1999 and finished in 02/2003. MMX – project’s objectives were to create a systematic method to compare process route alternatives for integrated iron and steelmaking. The method was to take into account metallurgical, technical, economical and sustainable development factors. For utilizing the method a novel simulation tool, Factory as a working title, was prepared. Software production process proved successful and it resulted in a tool with some distinguishingly flexible features. Even though the MMX-project has ended, the development around Factory software is likely to be continued. For more update information please refer to Factory website at: http://pyomet.oulu.fi/Factory. Picture 7. General view of the Factory simulation tool with production plant on (a) worksheet, (b) status window for viewing results, (c) Process editor window for viewing and editing equations and software’s validation notes in (d) error messages window. ANNUAL REPORT 2002 4 35 RESEARCH DEVICES AND ANALYTIC INSTRUMENTS 4.1 HIGH TEMPERATURE DEVICES The simultaneous DTA - TGA The model of the DTA-TGA device is TA- Instruments SDT 2960. It measures both differential temperature and weight changes in a material as a function of temperature and time in a controlled atmosphere. The furnaces maximum temperature is 1500 ˚C, a maximum sample weight is 200 mg.The sensitivity of TGA is 0,1 mg and DTA sensitivity is 0,001 ˚C. The device was purchased in 1996. 4.1.1 TGA The device measures weight changes in a material as a function of temperature and time in a controlled atmosphere. Flow Control - Brooks mass flow meter 5858S CO2 0 - 2 l /min accuracy ± 0.01 l /min - Brooks mass flow meter 5858S CO 0 - 10 l /min accuracy ± 0.05 l /min Picture 8. TGA 36 ANNUAL REPORT 2002 Balances - Mettler-toledo AG204, sensitivity 0,0001 g, max weight is 210 g. Purchased 1998. - Denver TL 4102D, sensitivity is 0,01 g, max weight is 4100 g. Purchased 1999. Furnaces - The SiC furnace’s maximum working temperature is 1500 ˚C. The inside diameter of the working tube is 30 mm. The other furnace is an Entech ETF 75-125 / 18-V, working tube inside diameter is 105 mm and it’s maximum working temperature is 1800 °C. It was purchased in 2002. 4.1.2 High Temperature Viscosimeter The device measures viscosities of slag and melts as a function of temperature and time in a controlled atmosphere. The model of viscotester is Haake VT 550 and it was purchased in 1996. The furnace is Carbolite PVT 18/75/350 and its maximum temperature is 1750 ˚C. The furnace was purchased in 1999. 4.1.3 Finger Test Device The measurement method is to rotate the refractory material piece “finger” with a constant speed in a slag or metal and then measure the corrosion rate and analyze the infiltration. The IKA eurostar power control visc is the adjustable rotator device which speed can be altered between 15-2000 r/min.The furnace is Lenton CSC 17/ 90/250 and its maximum temperature is 1700 ˚C. The furnace was purchased in 1997. 4.1.4 Optical Dilatometer The device indicates a materials dimension changes as a function of temperature and time in a controlled atmosphere. With the device a sessile drop contact angle and all the parameters for surface tension calculations can be determined.The tailormade programme Dakota calculates automatically the sample area and all the other parameters. Cameras B&W Camera is an AD C660 1/3" ccd 768*494 pixels, the lens is Dyotar DY135. The true maximum resolution is 0.025 mm horizontal and 0.029 mm vertical. The colour Camera is a Canon DM-MV1 digital video camera 1/3" ccd with 420 000 pixels. The cameras resolution is much less than the AD camera because of the digital zoom. ANNUAL REPORT 2002 37 Furnaces The SiC furnace’s maximum working temperature is 1550 ˚C. The inside diameter of the working tube is 30 mm. A sample is made from powder, then pressed into the cylinder, 4mm in diameter and the sample plate is usually sawn into 4 mm thick 10 mm * 10 mm squares. Another optical dilatometer for bigger samples (10 mm in diameter) has a Naber Supertherm HT08/18 furnace with a maximum working temperature of 1750 ˚C. 4.1.5 Gradient Furnace The device is Entech ETF 75/17V. It is a double chamber tube furnace, which tubes are 200 mm in height. The maximum temperature of the furnace is 1750 ˚C. The tubes inside diameter is 200 mm or 75 mm.The purpose of the furnace is to measure material properties in a constantly controlled temperature gradient. It was purchased in 2000. 4.1.6 Pressure Furnace The maximum pressure of the furnace is 10 bar and the temperature 1500 ˚C. The inner pipe diameter is 90 mm. The furnace was purchased in 2000. 4.1.7 Alkali Test The tester measures alkali effects on minerals. The inner diameter of the steel tube is 90 mm and the maximum temperature is 1150 ˚C. It was purchased in 2000. 38 4.2 ANNUAL REPORT 2002 OTHER DEVICES 4.2.1 Watermodels The models visualize phenomenon taking place inside a converter / ladle, like steel / slag flow during a blowing session and wear and tear of refractory materials. The models are scaled down to 1:7. The watermodels were purchased between 19972001. 4.2.2 Coulter Omnisorp 360 cx The gas sorption analyzer measures a surface area of a sample and determinates the pore size distribution. The Omnisorp is a continuous volumetric method, used to determine the adsorption and desorption isotherms.The pore size distribution peaks can be separated in a scale as little as 2 Ångström.The pore size distribution range is from 3 to 2000 Ångströms. The surface area value down to 3m2/gm resolution is better than 2 %. The device was purchased in 1997 in co-operation with the other laboratories. 4.2.3 Computational Fluid Dynamics Software The Phoenics software is for gas and liquid flow modelling.The Femlab software on Matlab is for simple modelling tasks and the Fluent software is for more complicated modelling within a project. 4.2.4 Thermodynamic Calculation Programmes HSC, Chemsage, Fact Sage programmes are for thermodynamic equilibrium calculations. 4.2.5 Gas Chromatograph The device is Agilent 6890 plus a thermal conductivity detector. The carrier gas is helium. The device was purchased in 2001. 4.2.6 Microscopes Olympus polarizing microscope BX51P and Olympus research stereomicroscope SZX9 with DP-12 camera and DP-software. The microscopes were purchased in 2001. ANNUAL REPORT 2002 39 4.2.7 Materialographic Surface Preparation of Solid Materials The device is for preparing materialographic samples for microscopic examination. We use diamond cutting and cold mounting.The Struers Epovac vacuum impregnation equipment is used for mounting and impregnation of porous specimens and for gluing specimens for thin sections to glass slides. Grinding and polishing is done with Struers LaboForce-1 at speed of 8 rpm and LabPol-1 - single speed machine, 250 rpm with MD or SiC consumables.The ready samples go through ultrasonic cleaning before inspection and use. The device was purchased in 2002. Picture 9. Struers LaboForce-1 and LabPol-1 grinding and polishing machine. 40 4.3 ANNUAL REPORT 2002 OTHER AVAILABLE FACILITIES Within the University of Oulu: Institution of Electron Optics (EOL): The EOL facilities are based on the use of seven instruments: Energy Filtered Transmission Electron Microscope EFTEM, Scanning Electron Microscope SEM, Field Emission Scanning Electron Microscope FESEM, Scanning Transmission Electron Microscope STEM, Electron Probe Microanalyzer EPMA, X-Ray Diffractometer XRD and X-Ray Fluorescence Spectrometer XRF. They provide three basic kinds of information: images, chemical analyses and crystal structures. Trace Element Laboratory: Plasma atomic emission spectrometry (DCP-AES, ICP-AES) and plasma mass spectrometry (ICP-MS). This equipment provides chemical analyses of difficult samples. At Rautaruukki Steel in Raahe: There is for example XRF, XRD, OES and SEM. At AvestaPolarit in Tornio Works: There is for example XRF, OES and SEM. ANNUAL REPORT 2002 5 41 PUBLICATIONS 2002 5.1 PAPERS Fabritius,T., Mure, P.,Virtanen, E., Hannula, P., Luomala, M. & Härkki, J.: Splashing mechanism in combined blowing. Ironmaking and Steelmaking 29(2002)1, s. 29-35. Luomala, M.,Virtanen, E., Mure, P., Siivola,T., Fabritius,T., Härkki, J.: A Novel Approach in the Estimation of Splashing in the BOF. Steel Research 73(2002)1, s. 9-14. Luomala, M.J., Fabritius,TM.J.,Virtanen, E.O., Siivola,T.P. & Härkki, J.J.: Splashing and Spitting Behaviour in the Combined Blown Steelmaking Converter. ISIJ International 42(2002)9, s. 944-949. Luomala, M.J., Fabritius,TM.J.,Virtanen, E.O., Siivola,T.P., Fabritius,T.L.J., Tenkku, H. & Härkki, J.J.: Physical Model Study of Selective Slag Splashing in the BOF. ISIJ International 42(2002)11, s. 1219-1224. Makkonen, H., Heino, J., Laitila, L., Hiltunen, A., Pöyliö, E. & Härkki, J.: Optimisation of Steel Plant Recycling in Finland: dusts, scales and sludge. Resources, Conservation and Recycling 35(2002), s. 77-84. Mattila, R.,Vatanen, J. & Härkki, J.: Chemical Wearing Mechanism of Refractory Materials in a Steel Ladle Slag Line. Scandinavian Journal of Metallurgy 31(2002), s, 1-5. Mäki, A., Österman, P. & Luomala, M.: Numerical Study of the Pusher-Type Slab Reheating Furnace. Scandinavian Journal of Metallurgy 31(2002)2, s. 81-87. Tang,Y., Laine, J., Fabritius,T. & Härkki, J.: Simulation of Pusher-Type Steel Slab Reheating Furnace by PHOENICS, Computational Fluid Dynamics and its Applications, 14 (2002) 2. 42 ANNUAL REPORT 2002 Tanskanen, P. A., Huttunen, S. M., Mannila, P. H. & Härkki, J. J.: Experimental Simulations of Primary Slag Formation in Blast Furnace. Ironmaking and Steelmaking 29(2002)4, s. 281-286. Fabritius,T. M. J., Luomala, M. J.,Virtanen, E. O.,Tenkku, H., Fabritius,T. L. J., Siivola,T. P. & Härkki, J.: Effect of Bottom Nozzle Arrangement on Splashing and Spitting in Combined Blowing Converter. ISIJ international 42(2002)8, s. 861-867 5.2 CONFERENCES AND SYMPOSIUMS Heikkinen, E-P., Kokkonen,T., Mattila, R. & Härkki, J.: An experimental study on steel’s reoxidation rate caused by SiO2-, MgO-Cr2O3and MgO-C –refractories. Clean Steel 6, Sixth International Conference on Clean Steel, Balatonfüred, Hungary, 10-12 June 2002, OMBKE, IOM, IISI, ESIC. S. 87-96. Heikkinen, E-P. Mattila, R., Kokkonen,T. & Härkki, J.: The chemical wear of the sen-slagline in the continuous casting of stainless steel. 85th Steelmaking Conference. Nashville,Tennessee, USA, 10-13.3.2002. Iron & Steel Society. S. 419-428. Pöyliö, E., Makkonen, H., Laitila, L., Heino, J., Hiltunen, A. & Härkki, J.: Optimal Recycling of the Iron Ore Based Steelmaking Dusts, Scales and Sludge. In: Björkman, B., Samuelsson, C., Wikström, J.-O. (ed.) Recycling and Waste Treatment in Mineral and Metal Processing: Technical and Economic Aspects. TMS Fall 2002 Extraction and Processing Division Meeting, Luleå, Sweden, 16-20 June 2002. Luleå, Sweden, Luleå University of Technology. Vol. 2, 129-137. Tang,Y.,Wang, J., Cang, D. & Härkki, J.: A New Method of Improving Continuous Casting Structure - The Electric Pulse Treatment. 4th European Continuous Casting Conference, Birmingham, UK, 14-16 October 2002. Angerman, M., Harju, M. & Fedory, P.: A User-friendly Tool for Large-scale Entity Simulation in the Process Industry. SIMS 2002, the 43rd Conference on Simulation and Modelling, Oulu, 26-27 September 2002. 6 s. ANNUAL REPORT 2002 43 5.3 REPORTS Heikkinen, E-P & Fabritius T.: CRK- ja LD-KG –konvertterien loppukuonien jähmettymiskäyttäytyminen – laskennallinen tarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 275. Oulu 2002. 20 s. Hurme, R., Kokkonen,T & Heikkinen, E-P.: MgO-C –tiilen aiheuttama C-pickup Al-tiivistettyyn teräkseen – kokeellinen tarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 276. Oulu 2002. 35 s. Heikkinen, E-P, Kokkonen,T. & Mattila R.: Terässenkan kuonarajan kemiallinen kuluminen – kokeellinen tarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 277. Oulu 2002. 51 s. Erkkilä, H.: Sulkeumat titaanitiivistetyssä teräksessä – laskennallinen tarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 278. Oulu 2002. 49 s. Määttä, H. & Mattila, O.: Masuunin pesän kemiallinen kuluminen: kokeellinen reaktiotarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 279. Oulu 2002. 73 s. Fabritius,T., Heikkinen, E-P., Roininen, J. & Härkki, J.: CRK-konvertterin tulenkestävän suojaus loppukuonaa modifioimalla – kokeellinen tarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 280. Oulu 2002. 47 s. Vähäoja, P.: N-pickup ruostumattomiin teräksiin ja typen liukeneminen terässulaan. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 282. Oulu 2002. 56 s. Petäjäjärvi, M., Kallio, K., Aspergren, P. & Härkki, J.: Valupulverien viskositeetin mittaus. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 283. Oulu 2002. 51 s. 44 ANNUAL REPORT 2002 Erkkilä, H.: Sulkeumat kalsiumkäsitellyssä ruostumattomassa teräksessä – kokeellinen tarkastelu. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 284. Oulu 2002. 57 s. Heikkinen, E-P.: Valuputken tukkeutuminen terästen jatkuvavalussa: syitä ja seurauksia. Kirjallisuusselvitys. Oulun yliopisto, prosessi- ja ympäristötekniikan osasto. Report 285. Oulu 2002. 82 s. 5.4 ANNUALS AND FINAL REPORTS Heikkinen, Kaisa (ed.): University of Oulu. Laboratory of Process Metallurgy, Department of Process and Environmental Engineering. Annual report 2001. Oulu 2002, University of Oulu. 58 s. Hämäläinen, M., Erkkilä, H., Liukkonen, M., Lind, M., Härkki, J. & Holappa, J.: Oksidimetallurgia-projekti. Espoo 2002, Teknillisen korkeakoulun materiaalitekniikan ja metallurgian julkaisuja, TKK-MK-131. ANNUAL REPORT 2002 6 45 THESIS 6.1 LICENCIATE IN TECHNOLOGY THESES Heikkinen, Eetu-Pekka Phenomena at refractory-steel-interfaces in the steel-ladles Luomala, Matti Development and application of physical models for investigating three different ironmaking and steelmaking unit operations 6.2 DIPLOMA ENGINEER THESES (MASTER OF SCIENCE IN TECHNOLOGY) Franssila, Laura The reduction behaviour of Lapland chromite Siivola,Tero The formation of scale in the slab reheating furnaces Karekivi, Pasi Chromium losses in slag in ferrochrome process Karhulahti,Timo Chemical, mineralogical and metallurgical properties of Rautaruukki sinter for different size fractions Hurme, Rauno Start-up of converters slag splashing equipment Olenius, Elina The production and characterization of oxide layers as catalyst for the oxygen evolution reaction Halmeenpää, Riina H2 –reduction of CuCl-solutions and Cu2O – suspensions in the autoclave Sola, Petri Slag handling in electric arc furnace Mure, Petri The effect of sidewall blowing on melt flows, mixing and oscillation of melt bath in a 150 ton AOD-converter 46 7 ANNUAL REPORT 2002 CONFERENCE VISITS Jouko Härkki: - Sixth International Conference Clean Steel, Balatonfüred, Unkari. 1012.6.2002 - Recycling and Waste Treatment in Mineral Processing: Technical and Economic Aspects, Luleå, Ruotsi. 16-20.6.2002 - Mills Symposium, Metals, Slags, Glasses: High Temperature Properties & Phenomena, London UK. 22-23.8.2002 - Nordic-Chinese Ironmaking Symposium, Luleå, Ruotsi. 3-4.9.2002 Eetu-Pekka Heikkinen: - 85th Steelmaking and 61st Ironmaking Conference. Nashville, Tennessee, USA. 10-13.3.2002 - 6th International Conference on Clean Steel. Balatonfüred, Hungary. 1012.6.2002. Matti Luomala: - 85th Steelmaking and 61st Ironmaking Conferences, Nashville, USA. 8.315.3.2002 Yong Tang: - Ninth International Phoenics User Conference, Moscow, Russia. 2329.9.2002 - 4th European Continuous Casting Conference, Birmingham, UK. 1416.10.2002 Pekka Tanskanen: - Nordic-Chinese Ironmaking Symposium, Luleå, Ruotsi. 3-4.9.2002 ANNUAL REPORT 2002 8 47 LABORATORY FREE-TIME ACTIVITIES It has become a tradition for the laboratory to participate in the annual Oulu Tar Skiing Race. The year 2002 was the third time that the laboratory had their own team.The team included seven men and one brave woman. Skiing distances were 40 and 70 kilometers with traditional and freestyle skiing styles. Team members: Hanski Määttä Sauli Kallio Kimmo Kallio Esa Virtanen Petri Mure Pasi Aspegren Pasi Karekivi Rita Hiltunen 48 ANNUAL REPORT 2002 Another major event during the year was the annual Terästurnaus that was arranged for the first time. Terästurnaus is a floorball tournament between Rautatuukki Steel Oy, AvestaPolarit Oyj and our laboratory. The winner of the first tournament was Rautaruukki and the laboratory came second after tight battle with both teams. Rautaruukki won the challenge trophy for a year but the laboratory plans to win it back next year. The players of our team were: Sauli Kallio, Marko Petäjäjärvi, Kimmo Kallio,Tero Siivola, Pasi Aspegren, Pasi Suikkanen, Jani Mäenpää,Timo Paananen, Antti Kaijalainen and Jani Isokääntä. Esa Virtanen was the referee and Rita Hiltunen acted as the tournament manager. Picture 11. The Terästurnaus challenge trophy. ANNUAL REPORT 2002 9 CONTACT INFORMATION Address: UNIVERSITY OF OULU Department of Process and Environmental Engineering Laboratory of Process Metallurgy P.O. Box 4300 FIN-90014 UNIVERSITY OF OULU FINLAND Fax: +358 8 553 2339 Email: [email protected] e.g. [email protected] Internet: http://pyomet.oulu.fi Contact Persons: Professor Mr. Jouko Härkki [email protected] tel +358 8 553 2424 Research Manager Mr. Timo Farbritius [email protected] tel +358 8 553 2421 Laboratory Manager Mr. Riku Mattila [email protected] tel +358 8 553 2425 Project Secretary Ms. Berith Zinovjev [email protected] tel +358 8 553 2553 49 50 ANNUAL REPORT 2002 Map of the University of Oulu ANNUAL REPORT 2002 NOTES 51
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