1981
DOI: 10.2355/isijinternational1966.21.270
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Analysis of Slab Temperature Change and Rolling Mill dine Length in Quasi Continuous Hot Strip Mill Equipped with Two Roughing Mills and Six Finishing Mills

Abstract: SynopsisThe length of the rolling mill line and the slab temperature change are theoretically compared between the quasi continuous type equipped with 3 rougher mills, of which the first one is reversible, and 6 finisher mills and the quasi continuous 4 passes type equipped with 2 rougher mills, of which the first is reversible, and 6 finisher mills for a mathematical model that a slab is rolled from the initial thickness 230 mm to the final thickness 2.5 mm.In the quasi continuous 4 passes type, the total len… Show more

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Cited by 7 publications
(8 citation statements)
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“…Devadas and Samarasekera [9] used this relation and obtained a value 21 kW/m 2 K. They observed that this value matched with data published [20] for high-pressure water sprays whereas Sasaki's relation was based on low pressure water sprays. HTC values used by various investigators [9,15,21,22] lie in the range 1.16-25 kW/m 2 K. Sasaki's relation could not be used in the present study because of insufficient mill data. However a heat transfer coefficient value of 2 kW/m 2 K was found appropriate in simulating plant data.…”
Section: Descaler Boxmentioning
confidence: 88%
“…Devadas and Samarasekera [9] used this relation and obtained a value 21 kW/m 2 K. They observed that this value matched with data published [20] for high-pressure water sprays whereas Sasaki's relation was based on low pressure water sprays. HTC values used by various investigators [9,15,21,22] lie in the range 1.16-25 kW/m 2 K. Sasaki's relation could not be used in the present study because of insufficient mill data. However a heat transfer coefficient value of 2 kW/m 2 K was found appropriate in simulating plant data.…”
Section: Descaler Boxmentioning
confidence: 88%
“…As the experimental conditions differ significantly, the results are also very different, e.g., constant heat transfer coefficients in the range from 1162 W/(m 2 K) to 20,920 W/(m 2 K) are reported in [7] and [23], respectively. A dependence of the heat transfer coefficient on the impact pressure is suggested in [24], where different constant values from 2000 W/(m 2 K) to 8000 W/(m 2 K) are used for different levels of spray pressure.…”
Section: State Of the Artmentioning
confidence: 91%
“…In some cases, e.g., [4,7,23], the contact problem is solved analytically. However, the analytical solution can only be derived, if some assumptions are made, including that the plate and the work roll are two semi-infinite solids in perfect contact with homogeneous initial temperature profiles.…”
Section: State Of the Artmentioning
confidence: 99%
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