JP2005264263A - Immersion tube in rh degassing facility and method for cooling core metal of immersion tube - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an immersion tube in an RH degassing facility and a method for cooling a core metal of the immersion tube, provided with an effective core metal cooling device at a low cost without setting the dedicated additional cooling structure for cooling the core metal. <P>SOLUTION: The immersion tube for RH degassing facility is provided with a refractory set in the inner side part, the core metal set at the outer side of the above refractory, circulated gas piping set on the surface at one side of the core metal, and monolithic refractory covering the core metal and the circulated gas piping. The circulated gas piping is set to the core metal portion at the lower side from at least circulated gas injecting hole, and the cooling of the core metal is performed with the circulated gas flowing in the piping. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a dip tube of a RH degassing facility and a dip tube mandrel cooling method for cooling a mandrel by circulating gas piping.

As a suction type vacuum refining method, there is an RH method in which molten steel in a pan is sucked into a vacuum chamber and brought into contact with a vacuum to perform vacuum refining. In the RH method, Ar gas is blown from one of the two dip tubes, and the molten steel is circulated by the principle of a gas lift pump.
FIG. 7 is a schematic cross-sectional view illustrating a conventional dip tube. As shown in FIG. 7, the dip tube has a brick 101 arranged in the vertical direction on the inner part, and a core iron skin is provided on the back of the brick to fix the brick and prevent air from getting in from outside air. A cored bar 102 is disposed, a pipe 103 for injecting reflux gas to the outside of the cored bar is provided, and an indefinite refractory 104 is provided on the outer side so as to cover the cored bar and the pipe. A flange portion 105 is provided on the top of the dip tube.

When the degassing treatment of the molten steel is performed, the dip tube is immersed in the molten steel, and the molten steel is sucked into the vacuum chamber to perform degassing and component adjustment. Since the dip tube is immersed in high-temperature molten steel, as shown in FIG. 8, the lower portion of the cored bar 102 is deformed by thermal expansion, and the joint portion between the bricks 101 disposed along with it expands, or the brick A crack occurs, and further, the bricks fall off.

Therefore, various methods for cooling the core metal of the dip tube have been proposed in order to prevent the above-described brick cracking / dropping off. For example, Japanese Patent Application Laid-Open No. 10-17920 discloses a method of cooling a metal core with a refrigerant. As shown in FIG. 9, according to this cooling method, a cored bar 111 composed of a double tube of an inner tube 111b and an outer tube 111a is arranged between the brick 101 and the amorphous refractory 104, and a refrigerant is supplied into the cored bar. The pipe 113 is installed, and the refrigerant is sent into the refrigerant supply pipe as indicated by the arrow to cool the cored bar.

That is, a dedicated additional cooling structure for circulating the refrigerant for cooling the cored bar is provided. Furthermore, Japanese Patent Application Laid-Open No. 10-17920 discloses another method for cooling the cored bar with a refrigerant. That is, as shown in FIG. 10, another cooling structure in which a cooling pipe 116 is spirally wound around a solid metal plate 111 (core metal) and cooled by circulating cooling water in the cooling pipe, for example. Is disclosed. Also in this example, an additional cooling structure dedicated for cooling the cored bar is provided.
Japanese Patent Laid-Open No. 10-17920

  As described above, in the conventional dip tube, an additional cooling structure dedicated to cooling the core metal is provided in order to effectively cool the core metal. As described above, in the method using the dedicated additional cooling structure, the cooling structure is specially added, so that there is a problem in that the initial investment is increased and the dip tube price is increased.

  Accordingly, an object of the present invention is to solve the conventional problems and to provide an RH degassing equipped with an effective cored bar cooling device without installing an additional cooling structure dedicated to cooling the cored bar. An object of the present invention is to provide a dip tube for equipment and a method for cooling a dip tube core metal.

  The present inventor has intensively studied to solve the above-mentioned problems of the prior art. As a result, the crack / dropout of the brick arranged vertically inside the dip tube is due to the deformation of the lower part of the core metal (iron skin) arranged on the back of the brick, and It has been found that the deformation of the core metal mainly occurs when the molten steel rises into the vacuum chamber. Furthermore, it has been found that the dip tube damage is due to deformation near the bottom of the cored bar. Therefore, the reflux gas pipe of the dip pipe of the RH degassing equipment is arranged along the surface of the core metal at the lower part of the core metal, that is, the part below the reflux gas inlet, and the reflux gas is arranged in this way. When flowing through the installed reflux gas pipe, the core metal can be cooled effectively without installing a separate dedicated pipe for cooling the core metal, and the dip pipe can be prevented from being damaged. It has been found that the lifetime of

  The present invention has been made on the basis of the above research results. The first aspect of the dip tube of the RH degassing equipment of the present invention includes a refractory disposed on the inner side and an outer side of the refractory. An RH degassing facility comprising: a metal core disposed on the surface of the metal core; a reflux gas pipe disposed on one surface of the metal core; and an amorphous refractory covering the metal core and the reflux gas pipe. It is a dip tube, wherein the reflux gas pipe is disposed at least on the core metal part below the reflux gas blowing port, and the core metal is cooled by the reflux gas flowing in the pipe. It is a dip tube for RH degassing equipment.

  According to a second aspect of the dip pipe of the RH degassing equipment of the present invention, the reflux gas pipe is disposed in a portion within 30% from the bottom in the height direction of the cored bar. It is a dip tube for gas equipment.

  According to a third aspect of the dip pipe of the RH degassing equipment of the present invention, the reflux gas pipe is disposed in a portion within 20% from the bottom in the height direction of the core metal. It is a dip tube for gas equipment.

  According to a fourth aspect of the immersion pipe of the RH degassing facility of the present invention, each of the reflux gas pipes is composed of at least a vertical part and a horizontal part, and a part of the horizontal part is disposed in the cored bar part. It is a dip tube of RH degassing equipment.

  According to a fifth aspect of the immersion pipe of the RH degassing facility of the present invention, each of the reflux gas pipes is composed of at least a vertical part and a horizontal part, and all of the horizontal part is disposed in the cored bar part. It is a dip tube of RH degassing equipment.

  A sixth aspect of the dip tube of the RH degassing equipment according to the present invention is a dip tube of the RH degassing equipment in which each of the reflux gas pipes is composed of a vertical portion and a horizontal portion.

  In the first aspect of the dip tube core metal cooling method of the present invention, a reflux gas pipe is disposed at a predetermined portion of the core metal that holds the refractory of the dip pipe of the RH degassing equipment, and the reflux gas is supplied to the pipe. It is a dip tube mandrel cooling method in which the mandrel is cooled by flowing.

  A second aspect of the dip tube mandrel cooling method according to the present invention is a dip tube mandrel cooling method in which the reflux gas pipe is disposed at least in a mandrel portion below the reflux gas inlet.

  A third aspect of the dip tube core metal cooling method according to the present invention is a dip tube core metal cooling method in which the reflux gas pipe is disposed in a portion within 30% from the bottom in the height direction of the core metal. .

  A fourth aspect of the dip tube mandrel cooling method of the present invention is a dip tube mandrel cooling method in which the reflux gas pipe is disposed within a portion within 20% from the bottom in the height direction of the mandrel. .

  According to a first aspect of the method for cooling a refractory holding hardware according to the present invention, a fluid is circulated on a surface of a predetermined portion of the hardware in a facility for injecting a fluid in a warm environment having a refractory holding hardware inside. This is a cooling method for a refractory-holding hardware, in which a pipe is provided, and the fluid is allowed to flow through the pipe to cool the hardware.

  As described above, according to the present invention, the reflux gas pipe of the dip pipe of the RH degassing equipment is arranged along the surface of the core metal at the lower part of the core metal, that is, the part below the blowing port. Provided is a dip tube capable of suppressing thermal deformation of a cored bar and a cooling method thereof without flowing a dedicated cooling device for cooling the cored bar by flowing the gas through the pipe arranged in this way can do.

The dip tube and the dip tube core metal cooling method of the RH degassing equipment of the present invention will be described with reference to the drawings.
One aspect of the dip tube of the RH degassing equipment of the present invention is a refractory disposed on the inner side, a core disposed outside the refractory, and disposed on one surface of the core. A RH degassing equipment dip pipe comprising a reflux gas pipe and an amorphous refractory covering the core metal and the reflux gas pipe, at least in the portion below the reflux gas inlet And the core metal is cooled by the circulating gas flowing in the pipe.

  1 to 3 are views for explaining a dip tube according to the present invention. 1 to 3 are developed views of the dip tube. That is, it is a view in which the dip tube is cut along a central axis at a predetermined portion, spread in the lateral direction, and developed on a plane. The upper side of the figure shows the upper side of the dip tube, and the lower side of the figure shows the lower side of the dip tube. In order to facilitate the explanation of the cooling of the metal core, the metal core, the circulating gas pipe, and the circulating gas blowing port are shown, and the amorphous refractory covering the metal core is omitted. FIG. 1 is a diagram showing the relative positions of the cored bar and the reflux gas blowing port. As shown in FIG. 1, a flange portion 2 is provided at the upper end portion of the cored bar 1, and a plurality of reflux gas blowing ports 3 are disposed at a substantially central part in the height direction of the cored bar. A plurality of brick support pins 4 are arranged at the lower part of the core bar, and round steel 5 or the like is wound around the lower end part thereof. In the present invention, the brick holding system is not limited to the support pin, and can be applied to a rib type or the like.

  FIG. 4 is a diagram showing a conventional reflux gas pipe. As shown in FIG. 4, conventionally, the reflux gas blowing pipe 26 is arranged through the shortest distance substantially toward each of the plurality of reflux gas blowing ports 23 arranged at substantially the center in the height direction of the cored bar 21. It had been. Accordingly, the circulating gas blowing pipe 26 is not disposed below the plurality of circulating gas blowing ports 23 disposed at the substantially central portion in the height direction of the cored bar 21.

  In the dip tube of the present invention, since the reflux gas pipe is disposed at least along the cored bar portion below the reflux gas blow-in port, it has been deformed by the conventional thermal expansion by the reflux gas flowing in the pipe. The lower part of the mandrel is effectively cooled.

  FIG. 2 is a view showing one piping state of the circulating gas blowing pipe arranged on the surface of the cored bar. As shown in FIG. 2, each of the reflux gas blowing pipes 6 includes a vertical part and a horizontal part, and most of the reflux gas blowing pipes 6 are provided below the reflux gas blowing ports 3, that is, below the core metal in the height direction. Is arranged. In the example shown in FIG. 2, a large number of recirculation blow pipes are arranged in the portion directly above the position of the brick support pin below the core metal.

  In this example, no recirculation blow pipe is disposed below the brick support pins. According to the arrangement of the reflux gas blowing pipe of this aspect, the existing reflux gas blowing pipe is arranged to the lower part of the core metal without newly providing a special additional cooling structure dedicated to the core metal. By simply blowing the reflux gas, incidentally, the vicinity of the lower end portion of the core metal can be effectively cooled, and deformation of the lower end portion of the core metal due to heat can be prevented.

  FIG. 3 is a view showing another piping state of the circulating gas blowing pipe arranged on the surface of the cored bar. As shown in FIG. 3, each of the reflux gas blowing pipes 6 includes a vertical part and a horizontal part, and a number of reflux gas blowing pipes are provided below the reflux gas blowing port 3, that is, below the core metal in the height direction. It is arrange | positioned along the surface of a metal core. In the example shown in FIG. 3, a horizontal portion of a part of the reflux blow pipe is also arranged between the brick support pin 4 and the round steel 5 at the lower part of the core metal. In addition, it is desirable to arrange | position the horizontal part of a perimeter circulation blow-in pipe close to the brick support pin 4, and a cooling effect becomes large.

  According to this aspect, the lower end portion of the core metal can also be effectively cooled. According to the present invention, since the existing reflux gas blowing pipe is disposed up to the lower end of the core metal without newly providing a special additional cooling structure dedicated to the core metal, only the reflux gas is blown into the pipe. In addition, it is possible to effectively cool the vicinity of the lower end portion of the core metal and prevent the lower end portion of the core metal from being deformed by heat.

  In the dip tube mandrel cooling method of the present invention, it is preferable that the reflux gas pipe is disposed in a portion within 30% from the bottom in the height direction of the mandrel. Furthermore, it is more preferable to arrange the reflux gas pipe in a portion within 20% from the bottom in the height direction of the cored bar. Furthermore, it is more preferable to arrange the reflux gas pipe in a portion within 15% from the bottom in the height direction of the cored bar.

The cooling effect of the dip tube of the present invention was first verified by simulation, and then the effect was actually verified. First, in the simulation, assuming the 4CC continuous treatment of ultra-low carbon steel, the temperature change of the core metal was estimated under the following conditions. That is,
Molten steel temperature: 1650 ° C
Ar gas flow rate: 3000 Nl / min immersion pattern: immersion 30 minutes + standby 10 minutes x 4 cycles

  FIG. 5 shows the temperature distribution after 4 cycles. (1) shows a conventional dip tube, and (2) shows a dip tube of the present invention. As shown in FIG. 5, in the conventional dip tube, the high temperature region exceeding 1000 ° C. exists up to the upper part. On the other hand, in the dip tube of the present invention, a high temperature region exceeding 1000 ° C. exists in the lower part. In the present invention, the temperature range below 900 ° C. at which deformation due to thermal expansion of the core metal can be prevented extends to the lower end of the core metal, whereas conventionally, the temperature range below 900 ° C. extends from the lower end of the core metal. It stops at the upper part. That is, in the conventional dip tube, the temperature of the wide portion of the lower end portion of the core metal exceeds 1000 ° C. and deformation due to thermal expansion of the core metal occurs, whereas in the dip tube of the present invention, the lower end portion of the core metal is It can be seen that the temperature is less than 900 ° C. and deformation due to thermal expansion of the cored bar can be prevented. Therefore, according to the simulation, the core metal was effectively cooled also at the lower end portion, and the result that deformation due to thermal expansion did not occur was obtained.

  FIG. 6 shows the calculated temperature and the deformation amount. In the figure, ◯ and Δ indicate the temperature of the core metal, and A and B indicate deformation of the core metal. ○ and A are examples of the present invention, and Δ and B are conventional examples. As is apparent from FIG. 6, in the example of the present invention, the temperature of the cored bar was approximately 800 ° C. or less, and the inner diameter of the cored bar was hardly increased. On the other hand, in the conventional example, the temperature of the cored bar exceeds 1000 ° C., and the inner diameter of the cored bar is greatly expanded at the lower end.

Then, it was actually used and verified. When actually used, the temperature at the lower end of the cored bar was almost the same as in the simulation. That is, the temperatures of the upper, middle, and lowermost portions of the core metal were 368 ° C., 648 ° C., and 1200 ° C. in the conventional method, respectively, whereas in the method of the present invention, they were 383 ° C. and 375 ° C., respectively. And 583 ° C. As a result, in the present invention, the expansion of the inner diameter of the core metal was hardly observed.
Note that the number of reflux gas inlets when the core metal was cooled by the reflux gas piping was examined. Conventionally, the number of reflux gas inlets is 24 to 30, but it has been found that the change in flow rate does not decrease in proportion to the cross-sectional area even if the number of inlets decreases. Therefore, it was found that the desired flow rate was obtained when the reflux gas inlet was 12 to 16. As a result, the cost can be further reduced.

As described above, the metal core can be cooled without providing a special cooling structure by devising the arrangement state of the existing reflux gas piping of the present invention. In addition, according to this invention, it is also possible to cool not only the dip tube but also the refractory holding hardware.
That is, a pipe for circulating a fluid on the surface of a predetermined part of the hardware in a facility for blowing a fluid in a warm environment, provided with a metal for holding a refractory inside, and flowing the fluid through the pipe, It is a cooling method of a refractory-holding hardware for cooling the hardware. By devising the piping for circulating the fluid, the object can be effectively cooled in addition to the original purpose.

  According to the present invention, the reflux gas pipe of the dip pipe of the RH degassing equipment is arranged on the lower surface of the core metal, that is, on the surface of the core metal below the blowing port, and the reflux gas is caused to flow through the pipe Further, it is possible to provide a dip tube capable of suppressing the thermal deformation of the cored bar without attaching a special cooling device and a cooling method therefor, and the industrial utility value is high.

FIG. 1 is a diagram showing the relative positions of the cored bar and the reflux gas blowing port. FIG. 2 is a view showing one piping state of the circulating gas blowing pipe arranged on the surface of the cored bar. FIG. 3 is a view showing another piping state of the circulating gas blowing pipe arranged on the surface of the cored bar. FIG. 4 is a diagram showing a conventional reflux gas pipe. FIG. 5 shows the temperature distribution after 4 cycles. FIG. 6 is a graph showing the calculated temperature and the deformation amount. FIG. 7 is a schematic cross-sectional view illustrating a conventional dip tube. FIG. 8 is a diagram showing a state of damage to the dip tube due to thermal expansion of the cored bar. FIG. 9 is a diagram illustrating a conventional cooling method for a cored bar having a double tube structure. FIG. 10 is a diagram showing a conventional method of cooling by winding a cooling pipe around a cored bar.

Explanation of symbols

1. Core metal 2. 2. Flange 3. Gas inlet 4. Brick support pins Round steel6. Circulating gas blowing pipe 26. Conventional reflux gas blowing tube 101. Brick 102. Core metal 103. Reflux gas blowing tube 104. Indefinite refractory 105. Flange

Claims (11)

A refractory disposed on the inner side; a core disposed outside the refractory; a reflux gas pipe disposed on one surface of the core; and the core and the reflux gas An RH degassing equipment dip pipe provided with an irregular refractory covering the pipe, wherein the reflux gas pipe is disposed at least in a cored bar part below the reflux gas inlet, and the reflux flowing in the pipe The dip tube of the RH degassing equipment, wherein the core metal is cooled by gas. The dip tube of the RH degassing equipment according to claim 1, wherein the reflux gas pipe is disposed in a portion within 30% from the bottom in the height direction of the cored bar. The dip tube of the RH degassing equipment according to claim 1, wherein the reflux gas pipe is disposed in a portion within 20% from the bottom in the height direction of the cored bar. 4. The RH according to claim 1, wherein each of the reflux gas pipes includes at least a vertical part and a horizontal part, and a part of the horizontal part is disposed in the cored bar part. 5. Immersion tube for degassing equipment. 4. The RH removal device according to claim 1, wherein each of the reflux gas pipes includes at least a vertical portion and a horizontal portion, and all of the horizontal portions are disposed in the cored bar portion. 5. Gas equipment dip tube. The dip pipe of the RH degassing equipment according to claim 4 or 5, wherein each of the reflux gas pipes includes a vertical part and a horizontal part. A dip tube mandrel cooling method, wherein a reflux gas pipe is disposed at a predetermined portion of a core metal holding a refractory of a dip pipe of an RH degassing facility, and the core metal is cooled by flowing a reflux gas through the pipe. The dip tube core metal cooling method according to claim 7, wherein the reflux gas pipe is disposed at least in a core metal part below the reflux gas inlet. The dip tube core metal cooling method according to claim 7, wherein the reflux gas pipe is disposed in a portion within 30% from the bottom in the height direction of the core metal. The dip tube core metal cooling method according to claim 7, wherein the reflux gas pipe is disposed in a portion within 20% from the bottom in the height direction of the core metal. A pipe provided with a metal for holding a refractory inside and for circulating a fluid on the surface of a predetermined part of the metal in a facility for injecting a fluid in a warm environment, and flowing the fluid through the pipe, the metal Cooling method for cooling refractory holding hardware.

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