JP5444744B2 - Manufacturing equipment for molten metal plated steel strip - Google Patents

Description

  The present invention relates to an apparatus for stably producing a hot-dip metal-plated steel strip by reducing splash scattering in the hot-dip plating process.

  In a continuous hot dipping process or the like, as shown in FIG. 8, after the steel strip 2 is immersed in a plating bath 7 generally filled with molten metal and the direction is changed by the sink roll 6, the steel strip 2 is moved vertically. After the step of pulling upward, the steel strip width provided opposite to the steel strip 2 so that the molten metal adhering to the steel strip surface has a predetermined plating thickness uniformly in the plate width direction and the plate longitudinal direction. There is provided a gas wiping device for jetting pressurized gas from the gas wiping nozzle 3 extending in the direction onto the steel strip, squeezing excess molten metal, and controlling the adhesion amount (plating adhesion amount) of the molten metal. Yes.

  The gas wiping nozzle 3 is usually longer than the width of the steel strip, that is, extends beyond the width end of the steel strip 2 in order to cope with various widths of the steel strip and at the same time shift in the width direction when the steel strip is pulled up. ing. In such a gas wiping apparatus, a so-called splash is generated in which molten metal falling below the steel strip is scattered due to the turbulence of the jet impinging on the steel strip 2, and the surface quality of the steel strip is degraded.

  Moreover, in order to increase the production amount in the continuous process, the steel plate passing speed may be increased. However, in the case of controlling the coating amount by the gas wiping method in the continuous hot dipping process, due to the viscosity of the molten metal, As the line speed increases, the initial adhesion amount immediately after passing through the plating bath of the steel strip increases, so to control the plating adhesion amount within a certain range, the wiping gas pressure must be set to a higher pressure, As a result, the splash is greatly increased and good surface quality cannot be maintained.

  In order to solve the above problem, an apparatus for reducing a certain amount of excess molten metal before reaching the wiping nozzle from the molten metal plating tank is disclosed as follows.

  In Patent Document 1, a molten metal squeeze member is provided between the support roll in the plating solution and the gas wiping nozzle in a non-contact manner on both surfaces of the steel strip, and after removing excess plating, the plating thickness is increased by gas wiping. In the adjusting device, the shape of the molten metal squeezing member is preferably a rectangular shape or a cylindrical body having an introduction portion whose distance from the front and back surfaces of the steel strip becomes wider at the lower end. A molten metal plating apparatus is disclosed in which the position over the liquid level is most desirable.

  Patent Document 2 discloses an apparatus for adjusting a plating thickness by gas wiping after removing surplus plating by providing a blade scraping device that is inclined with respect to the steel strip on both surfaces of the steel strip at the place where it comes out of the plating solution surface. Thus, there is disclosed a molten metal plating apparatus characterized in that the portion of the blade closest to the steel strip has a roundness with a diameter of 30 mm or less.

JP 2004-76082 A JP 2005-15837 A

  However, in the apparatus disclosed in Patent Document 1, when the molten metal drawing member extends above the plating bath surface or above and below the plating solution surface, the molten metal finally removed by gas wiping flows down, and the steel A liquid pool is formed in the gap between the belt and the molten metal squeezing member, and the distance from the height of the liquid reservoir to the gas wiping is short, resulting in a small squeezing effect. There is a problem that the solidified and solidified metal adheres to the steel strip and causes surface defects. On the other hand, even when the molten metal squeezing member is disposed in the plating bath, the flow path gradually narrows by making the distance from the steel strip wider at the lower end of the molten metal squeezing member. The flow velocity increases locally and the throttle effect is reduced.

  Moreover, in the apparatus disclosed in Patent Document 2, even if the blade is tilted to round the steel strip tip, a liquid pool is formed at the upper end as in Patent Document 1, and from there to gas wiping. As a result, the aperture effect is small.

  Therefore, in the apparatus disclosed in Patent Documents 1 and 2, the effect of reducing the initial adhesion amount immediately after passing through the plating bath is not sufficiently exhibited, so the effect of reducing the occurrence of molten metal splash in the gas wiping portion is insufficient. is there.

  In consideration of the above problems, the present invention reduces the amount of initial adhesion immediately after passing through the plating bath, reduces the occurrence of splash even at normal plate feeding speed and at high plate feeding speed, and has excellent surface appearance. It is an object of the present invention to provide a molten metal plated steel strip manufacturing facility capable of stably manufacturing a metal plated steel strip.

  When installing the molten metal throttle member for removing excess molten metal between the sink roll and the gas wiping, the present inventors have a short distance between the liquid pool position and the gas wiping position as described above. As a result, there arises a problem that the surplus plating amount cannot be reduced. Therefore, it is concluded that it is best to install the molten metal drawing member below the plating solution surface. However, if the cross-sectional shape of the molten metal squeezing member is the same as the prior art, the plating squeezing effect is small. Therefore, in order to effectively reduce the amount of molten metal plating accompanying the steel strip coming out of the plating tank, a detailed flow analysis was performed. As a result, it is the so-called accompanying flow that flows in the direction of travel of the steel strip near the surface of the steel strip, which affects the amount of molten metal that is lifted along with the steel strip, and reduces this flow over the entire width of the steel strip. Was found to be effective.

  Based on the above findings, the present inventors have made extensive studies on the shape of the molten metal drawing member for removing excess molten metal accompanying the steel strip, and as a result, completed the invention having the following characteristics. .

[1] Control the thickness of the deposited metal by blowing gas from a wiping nozzle that is disposed opposite to both sides of the steel strip that is pulled up continuously from the molten metal plating bath, with the steel strip sandwiched above the molten metal plating bath. In the manufacturing equipment for hot metal plating steel strip,
On both sides of the steel strip below the bath surface above the support roll in the bath, a roll coating portion formed so as to cover 1/4 or more of the bath surface side of the outer peripheral surface of the support roll in the bath, and the steel strip disposed above it The first rectifying plate formed by connecting the steel strip facing portion to the steel strip side end of the roll coating portion is in non-contact with the steel strip and the in-bath support roll. Further, outside the steel strip edge, surrounding at least 30% of the outer periphery of the support roll in the bath, and at least the center of the support roll in the bath and the end of the first rectifying plate on the steel plate side of the support roll coating portion in the bath A second rectifying plate formed so as to surround the outer periphery of the in-bath support roll above the line extending vertically from the center of the support roll in the bath to the steel plate surface, The plate has a length in the width direction of the steel strip of 10 mm above the bath within the support roll gap and is 1mm or more, and the gap between the strip edges is less than 100mm, molten metal plated steel strip manufacturing apparatus according to claim.

  [2] The apparatus for producing a molten metal plated steel strip according to [1], wherein the second rectifying plate includes a moving mechanism in a steel strip width direction.

  According to the present invention, the first rectifying plate provided with a roll coating portion and a steel strip facing portion formed so as to cover the bath surface side 1/4 or more of the outer peripheral surface of the support roll in the bath, and a steel strip edge By providing the second baffle plate formed so as to surround the outer periphery of the support roll in the bath arranged on the outside, the plating thickness can be adjusted by gas wiping after reducing the excess plating metal over the entire width of the steel strip. Splash generation over the entire width can be greatly reduced, and the sheeting speed at which occurrence can be noticeable can be greatly increased, making it possible to manufacture plated steel strips without surface defects while maintaining high productivity. .

The figure which shows one Embodiment of the manufacturing apparatus of the hot-dip metal plating steel strip of this invention. In the apparatus for producing a molten metal-plated steel strip of the present invention, a steel strip, a first rectifying plate having a roll coating portion and a steel strip facing portion, and a support roll in the bath outside the edge of the steel strip with respect to the support roll in the bath The figure explaining the arrangement | positioning state of the 2nd baffle plate arrange | positioned so that an outer periphery may be enclosed. The figure which shows the cross-sectional shape of a 1st baffle plate, and the flow of the molten metal around this baffle plate. The figure which shows the flow of the molten metal outside a steel strip edge when a 2nd baffle plate is installed. The figure explaining the arrangement | positioning state of a 2nd baffle plate in the manufacturing apparatus of the molten metal plating steel strip of this invention. The front view which shows one Embodiment of the manufacturing apparatus of the molten metal plating steel strip provided with the moving mechanism of the 2nd baffle plate. The figure which shows arrangement | positioning of the drawing member (molten metal drawing member) of a comparative example. The figure which shows a general molten metal plating apparatus.

  Embodiments of the present invention will be described below with reference to the drawings. In the following drawings, the same reference numerals are given to parts having the same functions as the parts shown in the already described drawings, and the description thereof is omitted.

  FIG. 1 shows an embodiment of a manufacturing apparatus for hot-dip metal-plated steel strip according to the present invention. In FIG. 1, 1 is the 1st baffle plate provided with the roll coating | coated part and the steel strip opposing part, 11 is the 2nd baffle plate arrange | positioned so that the outer periphery of a support roll in a bath may be enclosed outside a steel strip edge. .

  FIG. 2 is a view for explaining an arrangement state of the first rectifying plate 1 and the second rectifying plate 11 with respect to the steel strip 2 and the in-bath support roll 5, and (a) is the in-bath support roll 5 in FIG. The enlarged view of the baffle plate 1 and the 2nd baffle plate 11 part, (b) is an AA arrow directional view of (a). In FIG. 2, the 1st rectifying plate 1 and the 2nd rectifying plate 11 which are arrange | positioned in FIG. 1 at the one side (right side of the steel strip 2) of the steel strip 2 are shown.

  FIG. 3 is a diagram showing an embodiment of a cross-sectional shape of the first rectifying plate 1 installed in the apparatus for manufacturing a molten metal-plated steel strip in FIG. 1 and the flow of molten metal around the first rectifying plate 1. 8 is a flow accompanying the in-bath support roll 5, 9 is a flow accompanying the steel strip 2, and 10 is a flow generated by the flow 8.

  The 1st baffle plate 1 is the steel formed so that the roll coating | coated part formed so that the bath surface side 1/4 or more of the outer peripheral surface of a support roll in a bath might be covered, and it may be arrange | positioned above it and may oppose a steel strip The steel strip opposing portion is connected to the steel strip side end portion of the roll coating portion. The length of the first current plate 1 in the steel strip width direction is equal to or greater than the steel strip width. The 1st baffle plate 1 is installed in the non-contact with the steel strip and the support roll in a bath on both sides of the steel strip under the bath surface above the support roll in the bath.

  The 2nd baffle plate 11 is formed in the shape which surrounds the outer periphery of the support roll 5 in a bath outside a steel strip edge, and is non-contacted with the support roll in a bath. When there is a portion surrounding the roll of the first rectifying plate 1 and the roll of the second rectifying plate 11 in the same radial direction of the support roll 5 in the bath, the portion surrounding the roll of the second rectifying plate 11 It is arranged inside the roll coating part of the plate 1.

  When the first rectifying plate 1 is installed above the in-bath support roll below the plating bath surface, a flow 8 away from the steel strip 2 is generated between the in-bath support roll and the rectifying plate. When the flow 8 is generated, a forced flow 10 is generated between the steel strip 2 and the first rectifying plate 1 in the opposite direction to the progress of the steel strip even if the accompanying flow 9 is generated as the steel strip 2 travels. In addition, the accompanying flow 9 can be greatly suppressed. Thereby, the quantity of the excess molten metal plating accompanying a steel strip can be reduced. By using this first rectifying plate 1, it is possible to reduce excess molten metal before reaching the wiping nozzle from the molten metal plating tank. The inventors have applied for a patent for this invention (Japanese Patent Application No. 2007-229781).

  In order to sufficiently generate a flow 10 opposite to the traveling direction of the steel strip 2 between the steel strip 2 and the first rectifying plate 1 by the accompanying flow 9 generated by the rotation of the support roll 5 in the bath, the first rectifying plate The length of the portion covering one in-bath support roll 5 needs to be a length that covers at least 1/4 of the outer peripheral surface of the in-bath support roll 5 on the bath surface side. The effect is improved as the length of the portion covering the in-bath support roll 5 is longer. Here, the length which the 1st baffle plate 1 covers the support roll 5 in a bath is when the 1st baffle plate 1 is projected toward the center of the support roll 5 in a bath in the cross section perpendicular | vertical to the support roll centerline in a bath. The projected arc length of the first rectifying plate 1 on the outer peripheral surface of the support roll 5 in the bath.

  The dimensions and shape of the molten metal squeezing member need to be determined as appropriate in consideration of the equipment to be applied and the sheet feeding speed of the steel strip.

  As an example, one having a steel strip running direction dimension of 10 to 300 mm (however, it must not protrude above the bath surface) can be used.

  The distance between the first rectifying plate 1 and the support roll 5 in the bath is preferably 100 mm or less, and more preferably 50 mm or less. If it is larger than 100 mm, the flow of the accompanying flow 8 becomes weak, so that the flow 10 in the direction opposite to the traveling direction of the steel strip 2 does not occur, and the effect of reducing the amount of excess molten metal accompanying the steel strip is reduced. If it is 50 mm or less, the flow itself for reducing the amount of excess molten metal accompanying the steel sheet can be suppressed, so that the effect of reducing the amount of excess molten metal accompanying the steel strip is further increased. The distance between the first current plate 1 and the in-bath support roll 5 may be small as long as the first current plate 1 does not contact the in-bath support roll 5.

  The distance between the first rectifying plate 1 and the steel strip 2 is preferably 100 mm or less, and more preferably 50 mm or less. When it becomes larger than 100 mm, the flow 10 in the direction opposite to the traveling direction of the steel strip 2 does not affect the accompanying flow 9 accompanying the traveling of the steel strip 2, and the effect of reducing the amount of excess molten metal accompanying the steel strip is reduced. To do. When the thickness is 50 mm or less, the flow itself associated with the steel strip can be suppressed, so that the effect of reducing the amount of excess molten metal associated with the steel strip is further increased. The distance between the first rectifying plate 1 and the steel strip 2 may be reduced if the first rectifying plate 1 does not contact the steel strip 2.

  The first rectifying plate 1 does not need to keep the distance from the in-bath support roll 5 constant, and does not need to keep the distance from the steel strip 2 constant. Therefore, the shape of the portion covering the in-bath support roll 5 of the first rectifying plate 1 is not limited to the arc shape, and the portion facing the steel strip 2 of the first rectifying plate 1 may not be parallel to the steel strip. .

  The upper end of the first rectifying plate 1 is preferably installed so as to be located within 100 mm from the metal plating bath surface. When the distance from the bath surface is larger than 100 mm, the accompanying flow 9 is developed with the progress of the steel strip 2 above the first rectifying plate 1, and the effect of reducing the amount of excess molten metal accompanying the steel strip is reduced. . If the upper end of the first rectifying plate 1 is on the surface of the metal plating bath, there is a problem that excess molten metal that has been wiped adheres to the upper end of the first rectifying plate 1 and damages the steel plate.

  By using the first rectifying plate 1 described above, the amount of excess molten metal associated with the steel strip can be reduced, so that the occurrence of splash can be reduced as compared with the conventional device. By installing the second rectifying plate 11 surrounding the in-bath support roll 5 outside the edge of the steel strip 5, the occurrence of splash can be further reduced.

  The effect | action of the 2nd baffle plate 11 is demonstrated using FIG.

  When the first rectifying plate 1 is installed and the second rectifying plate 11 is not provided, as shown in FIG. 4 (a), it occurs between the two in-bath support rolls 5 and 5 outside the steel strip edge. The flow flows upward along the first current plate 1. This upward flow increases the accompanying flow at the edge of the steel strip, increasing the amount of edge splash generation. If the 2nd baffle plate 11 is installed, as shown in FIG.4 (b), the flow accompanying around the support roll 5 in a bath will flow along the 2nd baffle plate 11 in the circumferential direction. In this case, the upward flow of the first rectifying plate 1 is not generated, and the accompanying flow at the edge of the steel strip is reduced, so that the amount of excess molten metal accompanying the steel strip can be reduced over the entire width of the steel strip. The occurrence of edge splash can be further reduced.

  In FIG.4 (b), although the cross-sectional shape of a 2nd baffle plate is a circle surrounding the perimeter of the support roll 5 in a bath, a notch etc. may enter. When the 2nd baffle plate 11 surrounds the perimeter of the support roll 5 in a bath, the structure which can be divided | segmented into the circumferential direction may be sufficient. The second baffle plate 11 need not surround the entire circumference of the in-bath support roll 5. In order to generate the effect of reducing the edge splash, the second current plate 11 surrounds 30% or more of the outer periphery of the support roll 5 in the bath, and the portion surrounding the outer periphery of the support roll 5 in the bath is as shown in FIG. , At least below the line a connecting the support roll center O in the bath and the steel plate side end of the support roll coating portion in the bath of the first rectifying plate, and extending vertically from the support roll center O in the bath to the steel plate surface What is necessary is just to be formed so that all the outer peripheral parts of the support roll 5 in a bath above b may be enclosed. The ratio (%) of the portion surrounding the outer periphery of the in-bath support roll 5 is determined when the second rectifying plate 11 is projected toward the center of the in-bath support roll 5 in a cross section perpendicular to the in-bath support roll center line. It is a ratio (%) of the projected arc length of the second rectifying plate 1 on the outer peripheral surface of the support roll 5 in the bath to the outer periphery length of the support roll 5 in the bath.

  If the portion surrounding the outer periphery of the in-bath support roll of the second rectifying plate 11 does not satisfy the above condition, the edge splash suppressing effect cannot be obtained.

  The gap between the second current plate 11 and the in-bath support roll 5 is preferably 1 mm or more. If it is smaller than 1 mm, impurities (metal oxide, etc.) in the molten metal are clogged between the support roll 5 in the bath and the second rectifying plate 11, and the rotation of the support roll 5 in the bath is inhibited, the flow 10 is weakened and the effect of reducing splash And the wear and damage of the in-bath support roll 5 and the second rectifying plate 11 become severe.

  The length of the second current plate 11 in the width direction of the steel strip is preferably 100 mm or more. When the distance is less than 100 mm, a flow that occurs between the two support rolls 5 and 5 occurs near the edge of the steel strip without the second rectifying plate 11, and the flow that flows upward along the first rectifying plate 1 becomes stronger and edge splash occurs. The reduction effect is reduced.

  The gap between the steel strip edge and the second rectifying plate 11 is preferably 100 mm or less. When it exceeds 100 mm, the flow generated between the two support rolls 5 between the second rectifying plate 11 and the steel strip becomes large, the flow flowing upward along the first rectifying plate 1 becomes strong, and there is a lot of edge splash. Become.

  In the apparatus for manufacturing a molten metal-plated steel strip, since the width of the steel strip to be passed changes, the second rectifying plate 11 has a moving mechanism 12 that allows movement in the steel strip width direction as shown in FIG. It is preferable to provide. When the steel strip width changes, the moving mechanism 12 moves the steel strip edge corresponding to the changed steel strip width so that the gap D between the second rectifying plate 11 and the steel strip edge becomes a predetermined gap of 100 mm or less. Corresponding to the amount W, the occurrence of splash can be stably reduced by moving the second current plate 11 by W in the steel strip width direction. As the moving mechanism 12, a known moving mechanism can be used. 6, the steel strip 2 and the second rectifying plate 11 indicate the positions of the steel strip before the width change and the second rectifying plate before the steel strip width change, and the steel strip 2 ′ and the second rectifying plate 11 ′ change the width. The position of the 2nd current plate after a steel strip and steel strip width change is shown.

  By installing the second rectifying plate 11 around at least one of the support rolls 5, the occurrence of edge splash can be reduced. It is more effective to reduce the edge splash by installing the second rectifying plate 11 around the support roll 5 on the side farther from the bath surface. This is because the flow accompanying the support roll 5 on the side farther from the bath surface is larger.

  The hot-dip galvanizing apparatus shown in FIG. 1 was installed in a continuous hot-dip galvanizing line, and a manufacturing experiment of hot-dip galvanized steel strip was conducted.

  In the above-described continuous galvanizing line, the distance between the bath surface and the upper end of the in-bath support roll 5 on the side close to the bath surface was 80 mm. The distance between the plate 1 and the steel strip 2 is 20 mm, the distance between the steel strip 2 and the first rectifying plate 1 is 20 mm, and the length of the portion of the first rectifying plate 1 parallel to the steel strip until the distance from the molten zinc liquid surface is 30 mm. I stretched out. The roll coating portion of the first rectifying plate 1 was configured to cover the bath surface side 1/3 of the outer periphery of the in-bath support roll 5. The length of the first current plate 1 in the width direction of the steel strip was set to 2000 mm corresponding to the wiping nozzle. The diameter of the two support rolls was 250 mm, and the height difference between the centers was 150 mm. A second rectifying plate 11 having a thickness of 3 mm surrounding all or part of the outer periphery of the support roll 5 was installed outside the steel strip edge. SUS316L was used for the first rectifying plate 1 and the second rectifying plate 11.

The galvanized steel strip manufacturing conditions were as follows: the wiping nozzle slit gap was 0.8 mm, the distance between the wiping nozzle and the steel strip was 7 mm, the nozzle height from the molten zinc bath was 400 mm, and the molten zinc bath temperature was 460 ° C. The size was 1.2 mm thickness × 1.1 m width, and the amount of plating was 45 g / m ^{2 on} one side.

  Other manufacturing conditions and the length of the second current plate 11 in the width direction of the steel strip, the ratio of covering the outer periphery of the support roll 5 in the bath, the gap with the support roll 5 in the bath, the gap from the edge of the steel strip, and the product quality index Table 1 shows the results of investigating the amount of splash generated. In Example 5 and Comparative Example 3, the second rectifying plate 11 was disposed so that the upper end thereof was on the line a in FIG. In Example 5 in which the ratio of surrounding the outer periphery of the support roll 5 in the bath is 30%, the lower end of the second baffle plate 11 is below the line b, and the ratio of surrounding the outer periphery of the support roll 5 in the bath is 25%. 3, the upper end of the second rectifying plate 11 is above the line a in FIG. 5, and the lower end of the second rectifying plate 11 is below the line b in FIG.

  In Table 1, for comparison, an example in which only the first rectifying plate 1 is arranged, an example in which both the first rectifying plate 1 and the second rectifying plate 11 are not arranged, the first rectifying plate 1 and the second rectifying plate 11 are provided. An example in which the diaphragm member described in the prior art is arranged instead of is also described.

  The splash generation amount is a ratio of the steel strip length determined to have a splash defect in the inspection process to the steel strip length passed under each manufacturing condition, and includes a slight splash defect that does not cause a problem in practice.

  The first embodiment has a smaller gap between the second rectifying plate 11 and the in-bath support roll 5 installed around the in-bath support roll 5 on the outer side of the steel strip edge than the second to fifth embodiments. Although the length was short and the gap between the second current plate 11 and the steel strip edge was wide, a sufficient edge splash preventing effect was obtained.

  In Examples 1 to 5 of the present invention, Comparative Example 5 in which the first rectifying plate and the second rectifying plate defined by the present invention are not arranged, Comparative Example 4 in which only the first rectifying plate is arranged, the first rectifying plate and the first Comparative Example 6 in which the prior art diaphragm member is arranged instead of the two rectifying plates, Comparative Example 1 in which the first rectifying plate and the second rectifying plate are arranged, and the arrangement condition of the second rectifying plate is out of the scope of the present invention. Compared to ˜3, the amount of splash generation is greatly reduced.

  Within the scope of the present invention, the gap between the second rectifying plate 11 and the support roll 5 is widened, the length of the second rectifying plate 11 covering the in-bath support roll 5 is lengthened, the second rectifying plate 11 and steel. A narrower gap with the belt edge is more effective in reducing the occurrence of splash. In addition, the higher the ratio of the second rectifying plate 11 surrounding the outer periphery of the in-bath support roll 5, the better the effect of reducing the occurrence of splash.

  Even when the sheet passing speed is increased to 4.0 m / sec, a better splash reduction effect is exhibited as compared with the comparative example.

  The apparatus of the present invention can be used as a manufacturing facility for a hot-dip metal-plated steel strip that reduces the occurrence of splash and has an excellent surface appearance. Since the apparatus of the present invention can suppress the occurrence of splash even at the time of high-speed plate feeding, it can be used as an apparatus for manufacturing a molten metal plated steel strip excellent in surface appearance while maintaining high productivity.

DESCRIPTION OF SYMBOLS 1 1st baffle 2 Steel strip 3 Wiping nozzle 4 Support roll on bath 5 Support roll in bath 6 Sink roll 7 Molten metal plating bath 8 Flow accompanying support roll in bath 9 Flow accompanying steel strip 10 Support roll in bath Generated by the flow accompanying the flow 11 Second rectifying plate 12 Moving mechanism 13 Drawing member (molten metal drawing member)
W Movement amount of steel strip edge D Gap between steel strip edge and second straightening plate

Claims (2)

Molten metal plating that controls the thickness of the deposited metal by blowing gas from a wiping nozzle that is placed opposite to both sides of the steel strip above the molten metal plating bath against the steel strip that is continuously pulled up from the molten metal plating bath In steel strip production equipment,
On both sides of the steel strip below the bath surface above the support roll in the bath, a roll coating portion formed so as to cover 1/4 or more of the bath surface side of the outer peripheral surface of the support roll in the bath, and the steel strip disposed above it The first rectifying plate formed by connecting the steel strip facing portion to the steel strip side end of the roll coating portion is in non-contact with the steel strip and the in-bath support roll. Further, outside the steel strip edge, surrounds 30% or more of the outer periphery of the support roll in the bath, and at least the center of the support roll in the bath and the end of the first rectifying plate in the bath support roll covering portion on the steel strip side A second baffle plate formed so as to surround the outer periphery of the support roll in the bath below the line connecting the parts and above the line extending in the vertical direction from the center of the support roll in the bath to the steel strip surface, The two rectifying plates have a length in the steel strip width direction of 10 mm above the bath within the support roll gap and is 1mm or more, and the gap between the strip edges is less than 100mm, molten metal plated steel strip manufacturing apparatus according to claim.   The said 2nd baffle plate is provided with the moving mechanism to a steel strip width direction, The manufacturing apparatus of the hot-dip metal plating steel strip of Claim 1 characterized by the above-mentioned.

Images