A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control
The present thesis deals with the development of a new type of dynamic model for metallurgical reactors. It also covers some of the theoretical aspects of steelmaking that is necessary to include in such an application. The thesis consists of modeling work, high temperature experiments and cold mode...
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Format: | Doctoral Thesis |
Language: | English |
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KTH, Mikro-modellering
2012
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Online Access: | http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-101460 http://nbn-resolving.de/urn:isbn:978-91-7501-456-2 |
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ndltd-UPSALLA1-oai-DiVA.org-kth-101460 |
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English |
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Doctoral Thesis |
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BOF process modeling phosphorous capacity penetration depth slag foaming mixing time inclusion removal |
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BOF process modeling phosphorous capacity penetration depth slag foaming mixing time inclusion removal Ek, Mattias A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control |
description |
The present thesis deals with the development of a new type of dynamic model for metallurgical reactors. It also covers some of the theoretical aspects of steelmaking that is necessary to include in such an application. The thesis consists of modeling work, high temperature experiments and cold model experiments. Two different aspects of slags in the oxygen steelmaking were investigated. In the first study, slag samples were equilibrated with copper at 1923K in order to study their capacities in capturing phosphorous. Some of the samples were liquid-solid mixtures. The solid phases in these samples were identified by SEM analysis. The identified phases were found to agree well with Thermocalc calculations while the amount of solid fractions didn’t. The phosphorous distribution between the different phases was examined. The phosphate capacities of the samples were evaluated. The MgO content didn’t show any appreciable impact on the phosphate capacity. Furthermore the activities of FeO in the liquid slag samples were calculated and were found to deviate positively from ideality. In the second study the foaming height of CaO-SiO2-FeO slags by the reaction with hot metal was investigated. It was found that the foaming height increased with increasing FeO content up to 20-25%. The foaming height was seen to decrease with increased viscosity. The present results indicated that simply using foaming index for converter slag might lead to wrong conclusion. Simulation experiments using cold model at room temperature were conducted. Cold model experiments were carried out in order to study the penetration depth due to an impinging gas jet on the surface of a liquid metal. The liquid alloy Ga-In-Sn was used to simulate steel. And an HCl solution was used to simulate the slag. A comparison with predictions of existing models was made and a new model parameter was suggested. The observation of the movement of metal droplets generated by the gas jet was also made. The low velocity of droplets suggested that the turbulent viscosity played important role and the droplets could have long resident time in the slag. Furthermore a study of the effect of gas flow rate on homogenization and inclusion removal in a gas stirred ladle was carried out. Both industrial trials and cold model experiments were conducted. As an auxiliary tool CFD was used to predict the mixing times and was found to agree well with both the model experiments and industrial data. The increase of flow rate of inert gas would not improve the mixing substantially at higher flow rates. The water model study showed also that the gas flow rate had negligible effect on the rate of inclusion removal. Both the experiments and CFD calculation strongly suggested that low gas flow rate should be applied in the ladle treatment. Lastly a new approach to a dynamic process model of 300 ton BOF converter was made. The main feature was to utilize the velocity vectors obtained by CFD simulation. In the standalone model, the steel melt domain was sliced into 1000 cells. Based on the imported velocity vectors from the CFD calculation, the mass transfer of carbon and phosphorus was calculated taking into account the slag metal reactions. The mass exchange between slag and metal was considered to be dominated by the metal droplet formation due to oxygen jet. The convergence of the model calculation and the promising comparison between the model prediction and the industrial data strongly suggested that the proposed approach would be a powerful tool in dynamic process control. However, more precise descriptions of other process aspects need to be included before the model can be practically employed in a dynamic controlling system. === <p>QC 20120829</p> |
author |
Ek, Mattias |
author_facet |
Ek, Mattias |
author_sort |
Ek, Mattias |
title |
A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control |
title_short |
A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control |
title_full |
A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control |
title_fullStr |
A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control |
title_full_unstemmed |
A study of some aspects of gas-slag-metal interactions : Towards dynamic process model and control |
title_sort |
study of some aspects of gas-slag-metal interactions : towards dynamic process model and control |
publisher |
KTH, Mikro-modellering |
publishDate |
2012 |
url |
http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-101460 http://nbn-resolving.de/urn:isbn:978-91-7501-456-2 |
work_keys_str_mv |
AT ekmattias astudyofsomeaspectsofgasslagmetalinteractionstowardsdynamicprocessmodelandcontrol AT ekmattias studyofsomeaspectsofgasslagmetalinteractionstowardsdynamicprocessmodelandcontrol |
_version_ |
1716510203558494208 |
spelling |
ndltd-UPSALLA1-oai-DiVA.org-kth-1014602013-01-08T13:09:32ZA study of some aspects of gas-slag-metal interactions : Towards dynamic process model and controlengEk, MattiasKTH, Mikro-modelleringStockholm2012BOFprocess modelingphosphorous capacitypenetration depthslag foamingmixing timeinclusion removalThe present thesis deals with the development of a new type of dynamic model for metallurgical reactors. It also covers some of the theoretical aspects of steelmaking that is necessary to include in such an application. The thesis consists of modeling work, high temperature experiments and cold model experiments. Two different aspects of slags in the oxygen steelmaking were investigated. In the first study, slag samples were equilibrated with copper at 1923K in order to study their capacities in capturing phosphorous. Some of the samples were liquid-solid mixtures. The solid phases in these samples were identified by SEM analysis. The identified phases were found to agree well with Thermocalc calculations while the amount of solid fractions didn’t. The phosphorous distribution between the different phases was examined. The phosphate capacities of the samples were evaluated. The MgO content didn’t show any appreciable impact on the phosphate capacity. Furthermore the activities of FeO in the liquid slag samples were calculated and were found to deviate positively from ideality. In the second study the foaming height of CaO-SiO2-FeO slags by the reaction with hot metal was investigated. It was found that the foaming height increased with increasing FeO content up to 20-25%. The foaming height was seen to decrease with increased viscosity. The present results indicated that simply using foaming index for converter slag might lead to wrong conclusion. Simulation experiments using cold model at room temperature were conducted. Cold model experiments were carried out in order to study the penetration depth due to an impinging gas jet on the surface of a liquid metal. The liquid alloy Ga-In-Sn was used to simulate steel. And an HCl solution was used to simulate the slag. A comparison with predictions of existing models was made and a new model parameter was suggested. The observation of the movement of metal droplets generated by the gas jet was also made. The low velocity of droplets suggested that the turbulent viscosity played important role and the droplets could have long resident time in the slag. Furthermore a study of the effect of gas flow rate on homogenization and inclusion removal in a gas stirred ladle was carried out. Both industrial trials and cold model experiments were conducted. As an auxiliary tool CFD was used to predict the mixing times and was found to agree well with both the model experiments and industrial data. The increase of flow rate of inert gas would not improve the mixing substantially at higher flow rates. The water model study showed also that the gas flow rate had negligible effect on the rate of inclusion removal. Both the experiments and CFD calculation strongly suggested that low gas flow rate should be applied in the ladle treatment. Lastly a new approach to a dynamic process model of 300 ton BOF converter was made. The main feature was to utilize the velocity vectors obtained by CFD simulation. In the standalone model, the steel melt domain was sliced into 1000 cells. Based on the imported velocity vectors from the CFD calculation, the mass transfer of carbon and phosphorus was calculated taking into account the slag metal reactions. The mass exchange between slag and metal was considered to be dominated by the metal droplet formation due to oxygen jet. The convergence of the model calculation and the promising comparison between the model prediction and the industrial data strongly suggested that the proposed approach would be a powerful tool in dynamic process control. However, more precise descriptions of other process aspects need to be included before the model can be practically employed in a dynamic controlling system. <p>QC 20120829</p>Doctoral thesis, comprehensive summaryinfo:eu-repo/semantics/doctoralThesistexthttp://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-101460urn:isbn:978-91-7501-456-2application/pdfinfo:eu-repo/semantics/openAccess |