2014
DOI: 10.2355/isijinternational.54.504
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Analysis and Application of Soft Reduction Amount for Bloom Continuous Casting Process

Abstract: Based on the principle of solidification shrinkage compensation, a soft reduction amount calculation method was derived for bloom continuous casting process, and the bearing steel GCr15 was chosen as specific research steel to describe calculation process in detail. A two-dimensional heat transfer model was built to predict the solidification process of bloom, and the material properties of GCr15 were derived by weighted averaging of the phase fractions. The predicted temperature and shell thickness were verif… Show more

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Cited by 71 publications
(51 citation statements)
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“…The synchrotron experimental procedure has been described in previous publications [8,14,16] and is schematized in Figure 1. It consisted of the specimen being held in a square, hollowed out, 200 µm thick Al2O3 mould sandwiched in between two 100 µm thick sapphire plates and held in between two boron nitride plates.…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…The synchrotron experimental procedure has been described in previous publications [8,14,16] and is schematized in Figure 1. It consisted of the specimen being held in a square, hollowed out, 200 µm thick Al2O3 mould sandwiched in between two 100 µm thick sapphire plates and held in between two boron nitride plates.…”
Section: Methodsmentioning
confidence: 99%
“…On the other hand, external deformation can be beneficial such as the application of a 'soft reduction', a small rolling reduction (e.g. a few % strain) near to the end of the sump to compensate for solidification shrinkage and reduce centreline segregation and porosity [6][7][8]. Despite this importance, there remains only limited understanding of the mechanical behaviour of the mushy-zone in steels and, in particular, of their microstructural response to load and how this leads to defects.…”
Section: Introductionmentioning
confidence: 99%
“…In the secondary cooling zones, the heat of the strand is taken away by the cooling water, roll contact, and radiation. Therefore, the heat flux in secondary cooling was calculated as follows: qseci=hseci(TsurfTamb) centerhseci=αiWi0.55false(10.0075Twfalse)+hciNRiRliZLicenter+σϵfalse(Tsurf+Tambfalse)false(Tsurf2+Tamb2false) where, i denotes the i th cooling zone; qseci is the heat flux, MW m −2 , hseci is the effective heat transfer coefficient, w/(m 2 · °C); α i is the modified parameter; W i is the cooling water flux density, L/(m 2 · min); NRi is the number of roll; hci and Rli are, respectively, represent the heat transfer coefficient and the contact length between the strand and roll in W/(m 2 · °C) and m; T w , T surf , and T amb are, respectively, the cooling water temperature, the surface temperature and the ambient temperature, °C.…”
Section: Model Descriptionmentioning
confidence: 99%
“…17 The boundary condition of heat transfer has been described in the present authors' previous work. 1 In the mold, the heat flux decreases from the surface center to the corner due to the shrinkage of the shell. In the secondary cooling zone, the equivalent convection coefficients of each of the cooling zones were calculated according to the measured water flux distribution of the nozzles.…”
Section: Heat Transfer Modelmentioning
confidence: 99%