TY - JOUR
T1 - Numerical Analysis of Blast Furnace Hearth Drainage Based on a Simulated Hele–Shaw Model
AU - Liu, Weiqiang
AU - Shao, Lei
AU - Saxén, Henrik
N1 - Funding Information:
This work was carried out with support from the European Union's Research Fund for Coal and Steel (RFCS) research program under grant agreement no. 847332 and from the Åbo Akademi Foundation. This funding is gratefully acknowledged. L.S. thanks the National Natural Science Foundation of China (grant 51604068) for providing financial support for this work.
Publisher Copyright:
© 2022 Wiley-VCH GmbH
PY - 2022/6
Y1 - 2022/6
N2 - For a modern blast furnace (BF), a smooth tapping is a key prerequisite to keep the furnace running efficiently. An understanding of the hearth drainage and the influence of associated operational factors is therefore vitally important. To investigate the hearth tapping, a 2D computational fluid dynamics (CFD) model is developed and verified based on results from an experimental Hele–Shaw model. A series of simulation cases are conducted with the CFD model, studying the effect of the blast pressure, packed bed permeability, coke-free zone, and initial accumulated amounts of liquids on the tapping behavior, using water and oil as liquids as in the experimental model. To quantify the simulation findings, the effect of the above process conditions on the evolution of some drainage parameters, i.e., the liquid levels and volumes, flow rates, ratio of oil and water in the outflow, as well as the angle of the interfaces, are analyzed. The results reveal interesting findings of the hearth drainage and also show similarities with the outflow patterns of the hearth liquids in operating BFs.
AB - For a modern blast furnace (BF), a smooth tapping is a key prerequisite to keep the furnace running efficiently. An understanding of the hearth drainage and the influence of associated operational factors is therefore vitally important. To investigate the hearth tapping, a 2D computational fluid dynamics (CFD) model is developed and verified based on results from an experimental Hele–Shaw model. A series of simulation cases are conducted with the CFD model, studying the effect of the blast pressure, packed bed permeability, coke-free zone, and initial accumulated amounts of liquids on the tapping behavior, using water and oil as liquids as in the experimental model. To quantify the simulation findings, the effect of the above process conditions on the evolution of some drainage parameters, i.e., the liquid levels and volumes, flow rates, ratio of oil and water in the outflow, as well as the angle of the interfaces, are analyzed. The results reveal interesting findings of the hearth drainage and also show similarities with the outflow patterns of the hearth liquids in operating BFs.
UR - http://www.scopus.com/inward/record.url?scp=85122759888&partnerID=8YFLogxK
U2 - 10.1002/srin.202100629
DO - 10.1002/srin.202100629
M3 - Article
AN - SCOPUS:85122759888
SN - 1611-3683
VL - 93
JO - Steel Research International
JF - Steel Research International
IS - 6
M1 - 2100629
ER -