WO2015198689A1 - Water-granulated-slag manufacturing device and water-granulated-slag manufacturing method - Google Patents

Water-granulated-slag manufacturing device and water-granulated-slag manufacturing method Download PDF

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Publication number
WO2015198689A1
WO2015198689A1 PCT/JP2015/061341 JP2015061341W WO2015198689A1 WO 2015198689 A1 WO2015198689 A1 WO 2015198689A1 JP 2015061341 W JP2015061341 W JP 2015061341W WO 2015198689 A1 WO2015198689 A1 WO 2015198689A1
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Prior art keywords
granulated
granulated slag
slurry
slag
unit
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Application number
PCT/JP2015/061341
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French (fr)
Japanese (ja)
Inventor
昌男 藤田
徹志 宮田
ボブ グライベルディンガー
真司 枝村
Original Assignee
株式会社Ihi
株式会社Ihiポールワース
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Application filed by 株式会社Ihi, 株式会社Ihiポールワース filed Critical 株式会社Ihi
Priority to CN201580032127.4A priority Critical patent/CN106458747B/en
Priority to KR1020167032634A priority patent/KR101780409B1/en
Publication of WO2015198689A1 publication Critical patent/WO2015198689A1/en

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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • C21B3/08Cooling slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2200/00Recycling of non-gaseous waste material
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/032Separating slag from liquid, e.g. from water, after quenching

Definitions

  • the present invention relates to a granulated slag production apparatus and a granulated slag production method for producing granulated slag from molten slag discharged from a blast furnace.
  • This application claims priority based on Japanese Patent Application No. 2014-128325 for which it applied to Japan on June 23, 2014, and uses the content here.
  • the molten iron and molten slag generated in the blast furnace are discharged from the outlet.
  • the hot metal is poured into a torpedo car through the output and sent to the downstream equipment such as a converter.
  • the molten slag is diverted to the soot branched from the tuna and sent to a dry pit or a granulated slag production apparatus.
  • the molten slag is gradually cooled to produce ballast (gravel).
  • the granulated slag production device produces pressurized granulated slag by injecting pressurized water into the molten slag and rapidly crushing it.
  • molten slag since granulated slag has much demand compared with a ballast, molten slag is processed more by a granulated slag manufacturing apparatus than a dry pit.
  • the dewatering apparatus for dewatering the granulated slurry is provided in the granulated slag manufacturing apparatus.
  • a dewatering device for example, an invar filter that includes a cylindrical screen installed so that its axis is in the horizontal direction and a drive unit that rotates the screen, and dewaters the granulated slurry on the inner wall surface of the screen. (INBA filter) is used (for example, see Patent Document 1).
  • Patent Document 2 discloses a facility for producing granulated slag
  • Patent Document 3 discloses a power generation device that generates power using exhaust heat discharged from the facility for producing granulated slag.
  • the production capacity of the granulated slag in the granulated slag production apparatus provided with the invar filter of Patent Document 1 depends on the area of the screen of the invar filter. In general, the area (size) of the screen is determined based on the amount of molten slag delivered from one outlet. Therefore, when the spout expands at the end of the tap and the amount of molten slag to be sent increases, or when the molten slag is sent from the two taps simultaneously to one invar filter, The supply amount of the slurry may exceed the dewatering capacity of the invar filter. In this case, the delivery destination of the molten slag must be switched from the granulated slag production apparatus to the dry pit, which may reduce the production efficiency of the granulated slag.
  • the granulated slag production apparatus includes first and second granulated slag production units, and the first and second granulated slag production units include: Each includes a granulated slurry generating section that generates water granulated slurry by injecting water onto the molten slag discharged from the blast furnace body, and an invar filter that dehydrates the granulated slurry to produce the granulated slag.
  • the said granulated slag manufacturing apparatus sends out the granulated slurry produced
  • a device is further provided.
  • each of the said 1st and 2nd granulated slag manufacturing unit is the granulated which the said granulated slurry production
  • a granulation tank is further provided for storing the slurry and separating water vapor from the granulated slurry.
  • the said delivery apparatus is comprised so that the granulated slurry in the said granulation tank of the said 1st granulated slag manufacturing unit may be sent to the said 2nd granulated slag manufacturing unit.
  • the delivery device in the granulated slag production apparatus according to the second aspect, includes the granulation tank and the second granulated slag production of the first granulated slag production unit.
  • the unit is connected to the above-mentioned granulating tank.
  • the delivery device in the granulated slag production apparatus according to any one of the first to third aspects, the delivery device generates the granulated slurry in the first granulated slag production unit.
  • a delivery pipe extending from the downstream side of the section, and a pump for circulating the granulated slurry through the delivery pipe.
  • the pump is provided in the delivery pipe, and the delivery apparatus is located upstream of the pump in the delivery pipe. Further provided is a shut-off valve.
  • the delivery device in the granulated slag manufacturing apparatus according to the fifth aspect, includes a buffer tank for storing the granulated slurry between the shutoff valve and the pump. Further prepare.
  • the delivery device in the seventh aspect of the present invention, includes first and second delivery units.
  • the first delivery unit is configured to send the granulated slurry generated by the first granulated slag production unit to the invar filter of the second granulated slag production unit.
  • the said 2nd sending part is comprised so that the granulated slurry produced
  • the granulated slag manufacturing method is the granulated slag manufacturing method using the 1st, 2nd granulated slag manufacturing unit which manufactures granulated slag from the molten slag discharged
  • the first production process of dewatering and producing the granulated slag, and the above-mentioned generated in the first granulated slag production unit when a predetermined condition is satisfied Sending the granulated slurry to the second granulated slag production unit, and sending the granulated slurry from the first granulated slag production unit to the second granulated slag production unit in the delivery step
  • the water-granulated slurry, and a second process of manufacturing a water granulated slag is dehydrated in the second granulated slag production unit.
  • FIG. 1 is a diagram for explaining the blast furnace 100.
  • a blast furnace 100 having a two-face cast floor will be described as an example.
  • a blast furnace 100 includes a blast furnace body 110 that generates pig iron by reducing and melting iron ore that is a metal raw material.
  • molten slag is generated together with pig iron (molten iron), and a spout 112 (indicated by reference numerals 112A to 112D in FIG. 1) for discharging the generated pig iron and molten slag is provided.
  • a spout 112 indicated by reference numerals 112A to 112D in FIG. 1 for discharging the generated pig iron and molten slag is provided. 110 is provided below.
  • a skinmer 130 is provided on the tread 120, and the pig iron and the molten slag are separated by the skinmer 130, and the pig iron passes through the tread 120 and the tilting rod 140 to a torpedo car 142 arranged under the casting floor.
  • the molten slag separated from the pig iron by the skinmer 130 is guided to the pole 150 branched from the tread 120 and passed through the pole 150 and the rotary pole 152 through the dry pit 160 (reference numerals 160A and 160B in FIG. 1).
  • a granulated slag production unit 200 (indicated by reference numerals 200A and 200B in FIG. 1) constituting the granulated slag production apparatus 170.
  • the granulated slag production apparatus 170 of the present embodiment includes a granulated slag production unit 200A (first granulated slag production unit) and a granulated slag production unit 200B (second granulated slag production unit).
  • At least two of the granulated slag production units may be the granulated slag production units 200A and 200B of the present embodiment. .
  • a plurality of outlets 112 are provided in the blast furnace main body 110, and a plurality of The spout 112 is opened alternately and continuously spouted.
  • the blast furnace 100 having a double-faced cast floor has four tap holes 112.
  • the dry pit 160A and the granulated slag are alternately formed by alternately changing the period for opening the tap opening 112A or the tap opening 112B and the period for opening the tap opening 112C or the tap opening 112D.
  • the production unit 200A, the dry pit 160B and the granulated slag production unit 200B are alternately used.
  • the spout 112B, 112C, 112D is closed.
  • the output through 112A is carried out in a predetermined period and the output port 112A expands to a predetermined size (becomes the end of output)
  • the output port 112C or the output port 112D is opened, and then the spout 112A is closed.
  • the spout 112A is opened, and then the spout 112C or The sealing port 112D is closed.
  • it is called a wrap tapping to perform the tapping with both the tapping holes 112 opened.
  • the spout 112B is opened, the spouts 112A, 112C, and 112D are closed, and the spout through the spout 112B is performed during a predetermined period.
  • the spout 112C or the spout 112D is opened, and then the spout 112B is closed.
  • the spout 112B is opened, and then the spout 112C or The sealing port 112D is closed.
  • the molten slag extracted from the tap outlet 112A or the tap outlet 112B is introduced into the dry pit 160A or the granulated slag manufacturing unit 200A, and the dry pit 160B or water
  • the crushed slag production unit 200 ⁇ / b> B is introduced with molten slag discharged from the tap outlet 112 ⁇ / b> C or the tap outlet 112 ⁇ / b> D.
  • outlets 112 Of the four outlets 112 described above, two outlets 112 are alternately used (one of the outlets 112A and 112B, and the outlets 112C and 112D. In the configuration in which one of the outlets 112 is alternately opened (so-called two-turning), one of the two outlets 112 that is not in use is repaired with respect to one outlet 112. Repair of the ridge 120), the other outlet 112 is dried and is on standby.
  • both the molten slag discharged from the outlet 112A and the molten slag discharged from the outlet 112B Is introduced into the dry pit 160A or the granulated slag production unit 200A.
  • the dry pit 160 gradually cools the molten slag to produce ballast (gravel).
  • the granulated slag production unit 200 produces a granulated slag by quenching and crushing the molten slag.
  • FIG. 2 is a diagram for explaining one granulated slag production unit 200.
  • the molten slag (shown in black in FIG. 2) falls from the ridge 150 into the granulated tub 210 and flows in.
  • a large amount of pressurized water is sprayed from the granulated slurry generation unit (blowing box) 220 together with the inflow of molten slag into the granulated jar 210.
  • the granulated slag 210 the molten slag (about 1500 ° C.) is rapidly cooled to less than 100 ° C. and crushed by injecting pressurized water into the molten slag, and a granulated slurry (FIG. 5) is a mixture of the granulated slag and water. 2 are indicated by hatching).
  • the granulated slurry thus produced is sent to the granulation tank 230.
  • the granulation tank 230 temporarily stores the granulated slurry and separates water vapor from the granulated slurry.
  • the granulated slurry from which water vapor has been separated by the granulation tank 230 is introduced into the invar filter 250 by the distributor 240.
  • FIG. 3 is a view for explaining the invar filter 250, and is a cross-sectional view taken along line III-III in FIG.
  • the invar filter 250 is installed so that its axis is in the horizontal direction, and has a cylindrical screen 252 in which a plurality of holes are formed, and a screen 252 that rotates the screen 252 around the axis.
  • a drive unit a plurality of holes 242 are provided in the lower surface of a portion of the distributor 240 that is disposed inside the screen 252, and the granulated slurry (shown by hatching in FIG. 3) is substantially contained in the screen 252 by the distributor 240.
  • the slurry is uniformly dispersed and introduced by dropping, and the granulated slurry is dehydrated by the screen 252.
  • the screen 252 is provided with a plurality of scraping plates 254 erected from the inner wall of the screen 252 toward the center.
  • the scraping plates 254 are rotated in accordance with the rotation of the screen 252 (counterclockwise in FIG. 3).
  • the granulated slag (indicated by cross hatching in FIG. 3) is scraped and dropped onto the discharge conveyor 260.
  • the granulated slag is separated from the water of the granulated slurry and dehydrated. That is, granulated slag is produced.
  • the granulated slag dehydrated by the inva filter 250 is discharged out of the inva filter 250 by the discharge conveyor 260 and falls from the inva filter 250 (water separated from the granulated slurry, shown in white in FIG. 3). Is stored in a water collection tank 290 provided below the inva filter 250.
  • the granulated slag (denoted by cross hatching in FIG. 2) dehydrated by the inva filter 250 and conveyed by the discharge conveyor 260 is supplied to the product tank 280 via the transport conveyor 270.
  • the water separated from the granulated slurry by the Inba filter 250 and stored in the water collecting tank 290 is introduced into the hot water tank 300 by overflow.
  • Water (about 90 ° C.) introduced into the hot water tank 300 is sent to the cooling tower 320 by the hot water pump 310 and is cooled to about 50 ° C. to 60 ° C. in the cooling tower 320.
  • the water thus cooled is circulated through the granulated slag manufacturing unit 200 by being returned to the granulated slurry generation unit 220 by the cold water pump 330.
  • the granulated slag production unit 200 granulated slag is produced, and in the dry pit 160, ballast is produced. Since granulated slag is more demanding than ballast, there is a desire to introduce the entire amount of molten slag discharged from the blast furnace into the granulated slag production unit 200. However, at the end of the brewing process or during the lapping process, there are cases where the entire amount of the molten slag cannot be processed by only one granulated slag production unit 200. In this case, the delivery destination of the molten slag must be switched from the granulated slag production unit 200 to the dry pit 160, and the production efficiency of the granulated slag decreases.
  • molten slag processing manufacture of granulated slag
  • sending using a granulated slag production unit 200 that is in the initial stage of brewing and has a sufficient amount of granulation processing.
  • FIG. 4 is a diagram for explaining a delivery device 400 that constitutes the granulated slag production apparatus 170.
  • the delivery device 400 includes a delivery pipe 410, a pump 420, a shut-off valve 430, and a slag control unit 440.
  • the delivery pipe 410 (indicated by reference numerals 410A and 410B in FIG. 4) is a pipe that connects the granulated tank 230 of the granulated slag production unit 200A and the granulated tank 230 of the granulated slag production unit 200B.
  • a pump 420 (indicated by reference numerals 420 ⁇ / b> A and 420 ⁇ / b> B in FIG. 4) causes the granulated slurry to flow through the delivery pipe 410.
  • the shut-off valve 430 (indicated by reference numerals 430A and 430B in FIG. 4) is provided on the upstream side of the pump 420 in the delivery pipe 410.
  • the delivery pipe 410A of the present embodiment is configured to send the granulated slurry generated by the granulated slag production unit 200A to the inva filter 250 of the granulated slag production unit 200B. Therefore, at least the delivery pipe 410A corresponds to the first delivery unit of the present invention. Further, the delivery pipe 410B of the present embodiment is configured to send the granulated slurry generated by the granulated slag production unit 200B to the inva filter 250 of the granulated slag production unit 200A. Therefore, at least the delivery pipe 410B corresponds to the second delivery unit of the present invention.
  • the slag control unit 440 is composed of, for example, a semiconductor integrated circuit including a CPU (Central Processing Unit), reads a program, parameters, and the like for operating the CPU itself from the ROM, and serves as a RAM and other electronic circuits as a work area.
  • the entire delivery device 400 is managed and controlled in cooperation.
  • the slag control unit 440 controls the pump 420 and the shutoff valve 430. Specific control processing of the pump 420 and the shutoff valve 430 by the slag control unit 440 will be described in detail later.
  • the slag control unit 440 opens the shutoff valve 430A and the pump 420A. Is driven to feed the granulated slurry from the granulated tank 230 of the granulated slag production unit 200A to the granulated tank 230 of the granulated slag production unit 200B.
  • the molten slag that cannot be processed in the granulated slag production unit 200A can be treated in the granulated slag production unit 200B, and the granulated slag production apparatus can be used without increasing the area of the screen 252 constituting the invar filter 250.
  • the production efficiency of the granulated slag at 170 can be improved.
  • the slag control unit 440 opens the shut-off valve 430B and the pump 420B. Is driven to feed the granulated slurry from the granulated tank 230 of the granulated slag production unit 200B to the granulated tank 230 of the granulated slag production unit 200A.
  • the molten slag that cannot be processed in the granulated slag production unit 200B can be treated in the granulated slag production unit 200A, and the production efficiency of the granulated slag in the granulated slag production apparatus 170 can be improved.
  • FIG. 5 is a flowchart for explaining the flow of processing of the granulated slag manufacturing method.
  • a case where a lap is carried out at the spout 112A and the spout 112B will be described as an example.
  • the shutoff valve 430 is closed and the pump 420 is stopped.
  • the granulated slurry production unit 220 of the granulated slag production unit 200A injects pressurized water into the molten slag to produce a granulated slurry (granulated slurry production step S110, production step).
  • the invar filter 250 of the granulated slag production unit 200A dehydrates the granulated slurry produced in the granulated slurry production step S110 to produce granulated slag (granulated slag production step S120, first production step). ).
  • the slag control unit 440 determines whether or not a predetermined switching condition is satisfied (determination step S130).
  • the switching condition may be that the weight of the granulated slag transported by the transport conveyor 270 is equal to or greater than a predetermined weight set value, or the torque of the screen 252 is equal to or greater than a predetermined torque set value. Can be mentioned.
  • the slag control unit 440 maintains the introduction of the granulated slurry from the granulation tank 230 to the inva filter 250 in the granulated slag production unit 200A, and the granulated slag production method Terminate the process.
  • the flowchart shown in FIG. 5 shows the process of determining whether or not the sending apparatus 400 of this embodiment is necessary, and therefore, for example, the process shown in FIG. Determine no.
  • the slag control unit 440 opens the shut-off valve 430A (valve opening step S140), drives the pump 420A (pump driving step S150), and produces granulated slag.
  • the granulated slurry generated in the unit 200A is sent to the granulated slag manufacturing unit 200B (feeding step).
  • the granulated slag production unit 200B dehydrates the granulated slurry sent from the granulated slag production unit 200A to produce a granulated slag (a granulated slag production process S160, a second production process).
  • the granulated slag manufacturing unit 200B is the granulated slurry sent from the granulated slag manufacturing unit 200A and the granulated slag manufacturing unit 200B.
  • the produced granulated slurry is dehydrated together to produce granulated slag (second production step).
  • FIG. 5 shows the process of determining whether or not the delivery device 400 is necessary, FIG. 5 always shows that the granulated slag manufacturing process S160 is performed after the granulated slag manufacturing process S120. It does not indicate that it is carried out, and in fact, these manufacturing steps may be performed simultaneously.
  • the molten slag that cannot be treated in the granulated slag production unit 200A can be treated in the granulated slag production unit 200B, and the production efficiency of the granulated slag Can be improved.
  • the delivery pipe 410B of the delivery device 400 is configured to send the granulated slurry generated by the granulated slag production unit 200B to the invar filter 250 of the granulated slag production unit 200A. .
  • the molten slag which cannot be processed in the granulated slag production unit 200B can be sent to the granulated slag production unit 200A for processing, and the production efficiency of the granulated slag can be improved.
  • Whether or not the delivery pipe 410B is to be used may be determined in the same process as the flowchart shown in FIG.
  • the delivery apparatus 400 is provided with delivery piping 410A, 410B, the delivery direction of the granulated slurry is not limited to one direction, and the delivery apparatus 400 includes a plurality of granulated slag production units (invar filters). ) Can be changed as appropriate according to the processing status of the slurry.
  • the processing capacity (dewatering capacity) of one granulated slag production unit 200 is insufficient among the plurality of granulated slag production units 200
  • the delivery device 400 is the one granulated slag production unit 200. It is comprised so that the produced
  • FIG. 6 is a diagram for explaining a sending device 500 according to a modification of the present invention.
  • the delivery device 500 of the modified example includes a buffer tank 510, an air discharge pipe 520, and a cleaning mechanism 530 in addition to the delivery pipe 410, the pump 420, the shutoff valve 430, and the slag control unit 440.
  • the buffer tank 510, the air discharge pipe 520, and the cleaning mechanism 530 disposed in the delivery pipe 410A will be described
  • the buffer tank 510, the air discharge pipe 520, and the washing mechanism 530 disposed in the delivery pipe 410B will be described. Since the function is substantially the same as the said structure distribute
  • the buffer tank 510 is provided between the shut-off valve 430A and the pump 420A, and stores the granulated slurry.
  • the delivery pipe 410A extending from the shutoff valve 430A is connected to the upper part of the buffer tank 510, and the delivery pipe 410A extending from the pump 420A is connected to the lower part of the buffer tank 510.
  • the air mixed in the granulated tank 230 can be separated from the granulated slurry.
  • an air discharge pipe 520 is provided on the upper surface of the buffer tank 510, and the air separated in the buffer tank 510 is discharged to the water granulation tank 230.
  • the pump 420A With the configuration including the buffer tank 510, it is possible to prevent the introduction of air that could not be separated in the water granulating tank 230 into the pump 420A. Further, it is possible to prevent the introduction of air into the pump 420A due to a decrease in the level of the granulated slurry in the granulating tank 230. As a result, the pump 420A can be stably operated.
  • the cleaning mechanism 530 includes a cleaning pipe 532 connected to the delivery pipe 410A between the shutoff valve 430A and the buffer tank 510, and a washing water pump 534 that supplies washing water to the delivery pipe 410A through the washing pipe 532. Composed.
  • the granulated slurry is not always introduced into the delivery pipe 410A, but is introduced only when the switching condition is satisfied. Therefore, there is a possibility that the granulated slurry is fixed in the delivery pipe 410A during the period when the granulated slurry is not introduced.
  • the configuration including the cleaning mechanism 530 allows the water supply slurry 410A, the pump 420A, the shutoff valve 430A, and the buffer tank 510 to be cleaned with the cleaning water after the introduction of the granulated slurry into the supply piping 410A is stopped. .
  • the configuration including the cleaning mechanism 530 allows the water supply slurry 410A, the pump 420A, the shutoff valve 430A, and the buffer tank 510 to be cleaned with the cleaning water after the introduction of the granulated slurry into the supply piping 410A is stopped. .
  • the delivery device 400 includes the delivery pipe 410, the pump 420, the shutoff valve 430, and the slag control unit 440 has been described.
  • the delivery device has a configuration as long as the granulated slurry generated by the granulated slurry production unit 220 of one granulated slag production unit 200 can be delivered to the invar filter 250 of another granulated slag production unit 200.
  • the delivery device has a configuration as long as the granulated slurry generated by the granulated slurry production unit 220 of one granulated slag production unit 200 can be delivered to the invar filter 250 of another granulated slag production unit 200.
  • the delivery piping 410 demonstrated and demonstrated the structure which connects the granulation tanks 230 as an example.
  • the delivery pipe may be connected to any part (for example, the water granule 210 and the distributor 240) on the downstream side of the granulated slurry generation unit 220 and on the upstream side of the invar filter 250.
  • the delivery pipe includes any one of the granulated slag 210, the granulated tank 230, and the distributor 240 in one granulated slag production unit 200, and the granulated slag 210 and the granulated water in another granulated slag production unit 200.
  • Any one of the tank 230 and the distributor 240 may be connected to each other.
  • the delivery device 400 includes the cutoff valve 430 .
  • the delivery device may not include the cutoff valve. In this case, for example, whether or not the granulated slurry is delivered is determined by driving the pump 420.
  • the blast furnace 100 having a two-face cast floor has been described.
  • the delivery device 400 uses the granulated slurry produced by the granulated slurry production unit 220 of one granulated slag production unit 200 as the other. This can be sent to the INVA filter 250 of the granulated slag production unit 200, and the production efficiency of the granulated slag can be improved.
  • the granulated slag manufacturing apparatus 170 demonstrated the structure provided with the two granulated slag manufacturing units 200 in the said embodiment, the number of the granulated slag manufacturing units 200 may be three or more.
  • the configuration in which the molten slag is guided to the granulated slag manufacturing unit 200 or the dry pit 160 has been described as an example.
  • a ladle-type receiving device that receives a hot pot may be adopted.
  • the rotary rod 152 has been described as an example of the switching device that switches the introduction destination of the molten slag flowing through the rod 150 to the dry pit 160 or the granulated slag production unit 200.
  • the switching device is not limited, and for example, a stopper for blocking the flow of the molten slag is provided on each of the dredger 150 communicating only with the dry pit 160 and the dredger 150 communicating only with the granulated slag production unit 200.
  • the introduction destination of the molten slag may be switched to the dry pit 160 or the granulated slag production unit 200 by moving the stopper up and down.
  • the slag control unit 440 is configured by a semiconductor integrated circuit including a CPU has been described as an example, it may be a DSC, a PLC (Programmable Logic Controller), a relay board, or the like. Moreover, the granulated slag manufacturing apparatus 170 may not include the slag control unit 440. For example, an alarm may be generated when the screen torque (torque of the drive unit) exceeds a set value, and the operator may switch the operation of the delivery device based on the occurrence of the alarm.
  • the delivery device 400 includes delivery pipes 410A and 410B, but the present invention is not limited to this configuration.
  • the delivery device is provided with one delivery pipe that connects two granulated slag production units, a pump that can change the flow direction of the granulated slurry is provided in the delivery pipe, and water between the two granulated slag production units is provided. You may comprise so that the delivery direction of crushed slurry can be changed.
  • this one delivery pipe corresponds to both the first and second delivery parts of the present invention.
  • the processing capacity (dewatering capacity) of only a specific granulated slag production unit among a plurality of granulated slag production units is insufficient, two granulated slag production units are connected by one delivery pipe,
  • the sending direction may be fixed in one direction.
  • the processing capacity of only the granulated slag manufacturing unit 200A is insufficient, only the delivery pipe 410A is provided, and the delivery pipe 410B may not be provided.
  • the delivery piping should just be a flow path
  • the present invention can be used in a granulated slag production apparatus and a granulated slag production method for producing granulated slag from molten slag discharged from a blast furnace.
  • Granulated slag production apparatus 200 Granulated slag production unit 200A Granulated slag production unit (first granulated slag production unit) 200B Granulated slag production unit (2nd granulated slag production unit) 220 Granulated slurry generator 230 Granulated tank 250 Inver filter 400 Sending device 410 Sending pipe 410A Sending pipe (first sending part) 410B Delivery pipe (second delivery part) 420 Pump 430 Shut-off valve 500 Delivery device 510 Buffer tank

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Manufacture Of Iron (AREA)
  • Furnace Details (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

 This water-granulated-slag manufacturing device (170) is provided with first and second water-granulated-slag manufacturing units (200A, 200B), and each of the first and second water-granulated-slag manufacturing units is provided with a water-granulated slurry generating unit (220) for injecting water into molten slag and generating a water-granulated slurry, and an Invar filter (250) for dehydrating the water-granulated slurry and manufacturing a water-granulated slag. The water-granulated-slag manufacturing device is further provided with a delivery device (400) for delivering the water-granulated slurry generated by the first water-granulated slag manufacturing unit to the Invar filter of the second water-granulated-slag manufacturing unit.

Description

水砕スラグ製造装置および水砕スラグ製造方法Granulated slag production apparatus and granulated slag production method
 本発明は、高炉から排出された溶融スラグから水砕スラグを製造する水砕スラグ製造装置、および、水砕スラグ製造方法に関する。
 本願は、2014年6月23日に日本に出願された特願2014-128325号に基づき優先権を主張し、その内容をここに援用する。
The present invention relates to a granulated slag production apparatus and a granulated slag production method for producing granulated slag from molten slag discharged from a blast furnace.
This application claims priority based on Japanese Patent Application No. 2014-128325 for which it applied to Japan on June 23, 2014, and uses the content here.
 高炉において生成された溶銑および溶融スラグは、出銑口から出銑樋に出銑滓される。溶銑は、出銑樋を通じてトーピードカーに流し込まれ、転炉等の後段の設備に送られる。一方、溶融スラグは、出銑樋から分岐された滓樋に分流され、ドライピットもしくは水砕スラグ製造装置に送出される。ドライピットは、溶融スラグを徐冷してバラス(砂利)を製造する。水砕スラグ製造装置は、溶融スラグに加圧水を噴射して急冷破砕し、水砕スラグを製造する。なお、水砕スラグは、バラスと比較して需要が多いため、溶融スラグは、ドライピットよりも水砕スラグ製造装置で多く処理される。 The molten iron and molten slag generated in the blast furnace are discharged from the outlet. The hot metal is poured into a torpedo car through the output and sent to the downstream equipment such as a converter. On the other hand, the molten slag is diverted to the soot branched from the tuna and sent to a dry pit or a granulated slag production apparatus. In the dry pit, the molten slag is gradually cooled to produce ballast (gravel). The granulated slag production device produces pressurized granulated slag by injecting pressurized water into the molten slag and rapidly crushing it. In addition, since granulated slag has much demand compared with a ballast, molten slag is processed more by a granulated slag manufacturing apparatus than a dry pit.
 上述したように水砕スラグ製造装置では、溶融スラグに加圧水を噴射するため、水砕スラグと水との混合物である水砕スラリーが生成される。したがって、水砕スラグ製造装置には、水砕スラリーを脱水するための脱水装置が設けられている。このような脱水装置として、例えば、軸心が水平方向となるように設置された円筒型のスクリーンと、スクリーンを回転させる駆動部とを備え、スクリーンの内壁面において水砕スラリーを脱水するインバフィルタ(INBAフィルタ)が利用されている(例えば、特許文献1参照)。 As described above, in the granulated slag production apparatus, since pressurized water is injected into the molten slag, a granulated slurry that is a mixture of the granulated slag and water is generated. Therefore, the dewatering apparatus for dewatering the granulated slurry is provided in the granulated slag manufacturing apparatus. As such a dewatering device, for example, an invar filter that includes a cylindrical screen installed so that its axis is in the horizontal direction and a drive unit that rotates the screen, and dewaters the granulated slurry on the inner wall surface of the screen. (INBA filter) is used (for example, see Patent Document 1).
 また、特許文献2には、水砕スラグの製造設備が開示され、特許文献3には、水砕スラグの製造設備から排出される排熱を利用して発電する発電装置が開示されている。 Further, Patent Document 2 discloses a facility for producing granulated slag, and Patent Document 3 discloses a power generation device that generates power using exhaust heat discharged from the facility for producing granulated slag.
日本国特開平8-157241号公報Japanese Laid-Open Patent Publication No. 8-157241 日本国特開2001-180989号公報Japanese Laid-Open Patent Publication No. 2001-180989 日本国特開昭60-195309号公報Japanese Unexamined Patent Publication No. 60-195309
 上記特許文献1のインバフィルタが設けられた水砕スラグ製造装置における水砕スラグの製造能力は、インバフィルタのスクリーンの面積に依存する。一般的にスクリーンの面積(大きさ)は、1つの出銑口から送出される溶融スラグの量に基づいて決定される。したがって、出銑末期において出銑口が拡大し、送出される溶融スラグの量が増加した場合や、2つの出銑口から溶融スラグが同時に1つのインバフィルタへ送出される期間においては、水砕スラリーの供給量がインバフィルタの脱水能力を超えてしまう場合がある。この場合、溶融スラグの送出先を水砕スラグ製造装置からドライピットへ切り換えなければならず、水砕スラグの製造効率が低下する可能性がある。 The production capacity of the granulated slag in the granulated slag production apparatus provided with the invar filter of Patent Document 1 depends on the area of the screen of the invar filter. In general, the area (size) of the screen is determined based on the amount of molten slag delivered from one outlet. Therefore, when the spout expands at the end of the tap and the amount of molten slag to be sent increases, or when the molten slag is sent from the two taps simultaneously to one invar filter, The supply amount of the slurry may exceed the dewatering capacity of the invar filter. In this case, the delivery destination of the molten slag must be switched from the granulated slag production apparatus to the dry pit, which may reduce the production efficiency of the granulated slag.
 なお、インバフィルタを構成するスクリーンの面積を大きくして脱水効率を向上することも考えられるが、インバフィルタに要するコストが増大する可能性がある。 Although it is conceivable to improve the dewatering efficiency by increasing the area of the screen constituting the invar filter, the cost required for the invar filter may increase.
 本発明は、インバフィルタを構成するスクリーンの面積を増大させることなく、水砕スラグの製造効率を向上することができる水砕スラグ製造装置、および、水砕スラグ製造方法を提供することを目的とする。 It is an object of the present invention to provide a granulated slag production apparatus and a granulated slag production method capable of improving the production efficiency of granulated slag without increasing the area of the screen constituting the invar filter. To do.
 上記課題を解決するために、本発明の第1の態様では、水砕スラグ製造装置は、第1、第2水砕スラグ製造ユニットを備え、これら第1、第2水砕スラグ製造ユニットは、それぞれ、高炉本体から排出された溶融スラグに水を噴射して水砕スラリーを生成する水砕スラリー生成部と、上記水砕スラリーを脱水して水砕スラグを製造するインバフィルタと、を備える。また、上記水砕スラグ製造装置は、上記第1水砕スラグ製造ユニットの上記水砕スラリー生成部によって生成された水砕スラリーを、上記第2水砕スラグ製造ユニットの上記インバフィルタに送出する送出装置をさらに備える。 In order to solve the above-described problem, in the first aspect of the present invention, the granulated slag production apparatus includes first and second granulated slag production units, and the first and second granulated slag production units include: Each includes a granulated slurry generating section that generates water granulated slurry by injecting water onto the molten slag discharged from the blast furnace body, and an invar filter that dehydrates the granulated slurry to produce the granulated slag. Moreover, the said granulated slag manufacturing apparatus sends out the granulated slurry produced | generated by the said granulated slurry production | generation part of the said 1st granulated slag production unit to the said invar filter of the said 2nd granulated slag production unit. A device is further provided.
 また、本発明の第2の態様では、上記第1の態様の水砕スラグ製造装置において、上記第1、第2水砕スラグ製造ユニットは、それぞれ、上記水砕スラリー生成部が生成した水砕スラリーを貯留してこの水砕スラリーから水蒸気を分離する水砕槽をさらに備える。また、上記送出装置は、上記第1水砕スラグ製造ユニットの上記水砕槽内の水砕スラリーを上記第2水砕スラグ製造ユニットに送出するように構成されている。 Moreover, in the 2nd aspect of this invention, in the granulated slag manufacturing apparatus of the said 1st aspect, each of the said 1st and 2nd granulated slag manufacturing unit is the granulated which the said granulated slurry production | generation part produced | generated, respectively. A granulation tank is further provided for storing the slurry and separating water vapor from the granulated slurry. Moreover, the said delivery apparatus is comprised so that the granulated slurry in the said granulation tank of the said 1st granulated slag manufacturing unit may be sent to the said 2nd granulated slag manufacturing unit.
 また、本発明の第3の態様では、上記第2の態様の水砕スラグ製造装置において、上記送出装置は、上記第1水砕スラグ製造ユニットの上記水砕槽と上記第2水砕スラグ製造ユニットの上記水砕槽とを接続している。 In the third aspect of the present invention, in the granulated slag production apparatus according to the second aspect, the delivery device includes the granulation tank and the second granulated slag production of the first granulated slag production unit. The unit is connected to the above-mentioned granulating tank.
 また、本発明の第4の態様では、上記第1から第3のいずれか1つの態様の水砕スラグ製造装置において、上記送出装置は、上記第1水砕スラグ製造ユニットにおける上記水砕スラリー生成部の下流側から延在した送出配管と、上記送出配管に上記水砕スラリーを流通させるポンプと、を備える。 In the fourth aspect of the present invention, in the granulated slag production apparatus according to any one of the first to third aspects, the delivery device generates the granulated slurry in the first granulated slag production unit. A delivery pipe extending from the downstream side of the section, and a pump for circulating the granulated slurry through the delivery pipe.
 また、本発明の第5の態様では、上記第4の態様の水砕スラグ製造装置において、上記ポンプは、上記送出配管に設けられ、上記送出装置は、上記送出配管における上記ポンプの上流側に設けられた遮断弁をさらに備える。 According to a fifth aspect of the present invention, in the granulated slag manufacturing apparatus according to the fourth aspect, the pump is provided in the delivery pipe, and the delivery apparatus is located upstream of the pump in the delivery pipe. Further provided is a shut-off valve.
 また、本発明の第6の態様では、上記第5の態様の水砕スラグ製造装置において、上記送出装置は、上記遮断弁と上記ポンプとの間に、上記水砕スラリーを貯留するバッファタンクをさらに備える。 In the sixth aspect of the present invention, in the granulated slag manufacturing apparatus according to the fifth aspect, the delivery device includes a buffer tank for storing the granulated slurry between the shutoff valve and the pump. Further prepare.
 また、本発明の第7の態様では、上記第1の態様の水砕スラグ製造装置において、上記送出装置は、第1、第2送出部を備える。上記第1送出部は、上記第1水砕スラグ製造ユニットで生成された水砕スラリーを上記第2水砕スラグ製造ユニットの上記インバフィルタに送出するように構成されている。また、上記第2送出部は、上記第2水砕スラグ製造ユニットで生成された水砕スラリーを上記第1水砕スラグ製造ユニットの上記インバフィルタに送出するように構成されている。 Moreover, in the seventh aspect of the present invention, in the granulated slag manufacturing apparatus of the first aspect, the delivery device includes first and second delivery units. The first delivery unit is configured to send the granulated slurry generated by the first granulated slag production unit to the invar filter of the second granulated slag production unit. Moreover, the said 2nd sending part is comprised so that the granulated slurry produced | generated by the said 2nd granulated slag manufacturing unit may be sent to the said invar filter of the said 1st granulated slag manufacturing unit.
 また、本発明の第8の態様では、水砕スラグ製造方法は、高炉から排出された溶融スラグから水砕スラグを製造する第1、第2水砕スラグ製造ユニットを用いた水砕スラグ製造方法であって、上記第1水砕スラグ製造ユニットにおいて、上記溶融スラグに水を噴射して水砕スラリーを生成する生成工程と、上記第1水砕スラグ製造ユニットにおいて生成された上記水砕スラリーを、この第1水砕スラグ製造ユニットにおいて脱水して水砕スラグを製造する第1製造工程と、予め定められた条件が満たされたときに、上記第1水砕スラグ製造ユニットにおいて生成された上記水砕スラリーを上記第2水砕スラグ製造ユニットに送出する送出工程と、上記送出工程で上記第1水砕スラグ製造ユニットから上記第2水砕スラグ製造ユニットに送出された上記水砕スラリーを、この第2水砕スラグ製造ユニットにおいて脱水して水砕スラグを製造する第2製造工程と、を含む。 Moreover, in the 8th aspect of this invention, the granulated slag manufacturing method is the granulated slag manufacturing method using the 1st, 2nd granulated slag manufacturing unit which manufactures granulated slag from the molten slag discharged | emitted from the blast furnace. In the first granulated slag production unit, a production step of injecting water into the molten slag to produce a granulated slurry, and the granulated slurry produced in the first granulated slag production unit. In the first granulated slag production unit, the first production process of dewatering and producing the granulated slag, and the above-mentioned generated in the first granulated slag production unit when a predetermined condition is satisfied Sending the granulated slurry to the second granulated slag production unit, and sending the granulated slurry from the first granulated slag production unit to the second granulated slag production unit in the delivery step The water-granulated slurry, and a second process of manufacturing a water granulated slag is dehydrated in the second granulated slag production unit.
 本発明によれば、インバフィルタを構成するスクリーンの面積を増大させることなく、水砕スラグの製造効率を向上することができる。 According to the present invention, it is possible to improve the production efficiency of granulated slag without increasing the area of the screen constituting the invar filter.
高炉を説明するための図である。It is a figure for demonstrating a blast furnace. 水砕スラグ製造ユニットを説明するための図である。It is a figure for demonstrating a granulated slag manufacturing unit. インバフィルタを説明するための図である。It is a figure for demonstrating an inba filter. 本発明の一実施形態にかかる水砕スラグ製造装置を構成する送出装置を説明するための図である。It is a figure for demonstrating the delivery apparatus which comprises the granulated slag manufacturing apparatus concerning one Embodiment of this invention. 本発明の一実施形態にかかる水砕スラグ製造方法の処理の流れを説明するためのフローチャートである。It is a flowchart for demonstrating the flow of a process of the granulated slag manufacturing method concerning one Embodiment of this invention. 本発明の変形例にかかる送出装置を説明するための図である。It is a figure for demonstrating the sending apparatus concerning the modification of this invention.
 以下に添付図面を参照しながら、本発明の好適な実施形態について詳細に説明する。かかる実施形態に示す寸法、材料、その他具体的な数値等は、発明の理解を容易とするための例示にすぎず、特に断る場合を除き、本発明を限定するものではない。なお、本明細書および図面において、実質的に同一の機能、構成を有する要素については、同一の符号を付することにより重複説明を省略し、また本発明に直接関係のない要素は図示を省略する。 Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. The dimensions, materials, and other specific numerical values shown in the embodiments are merely examples for facilitating the understanding of the invention, and do not limit the present invention unless otherwise specified. In the present specification and drawings, elements having substantially the same function and configuration are denoted by the same reference numerals, and redundant description is omitted, and elements not directly related to the present invention are not illustrated. To do.
 図1は、高炉100を説明するための図である。なお、本実施形態では、2面鋳床の高炉100を例に挙げて説明する。図1に示すように高炉100は、金属原料である鉄鉱石を還元溶融して銑鉄を生成する高炉本体110を備えている。高炉本体110においては、銑鉄(溶銑)とともに溶融スラグが生成され、生成された銑鉄および溶融スラグを出銑滓するための出銑口112(図1中、符号112A~112Dで示す)が高炉本体110の下部に設けられている。 FIG. 1 is a diagram for explaining the blast furnace 100. In the present embodiment, a blast furnace 100 having a two-face cast floor will be described as an example. As shown in FIG. 1, a blast furnace 100 includes a blast furnace body 110 that generates pig iron by reducing and melting iron ore that is a metal raw material. In the blast furnace body 110, molten slag is generated together with pig iron (molten iron), and a spout 112 (indicated by reference numerals 112A to 112D in FIG. 1) for discharging the generated pig iron and molten slag is provided. 110 is provided below.
 高炉本体110の外部には、出銑口112から出銑滓された銑鉄および溶融スラグが流れる出銑樋120が出銑口112ごとに設けられている。また、出銑樋120には、スキンマー130が設けられており、スキンマー130によって銑鉄と溶融スラグとが分離され、銑鉄は出銑樋120、傾注樋140を通じて、鋳床下に配されたトーピードカー142に導かれる。一方、スキンマー130によって銑鉄から分離された溶融スラグは、出銑樋120から分岐された滓樋150に導かれ、滓樋150、回転樋152を通じて、ドライピット160(図1中、符号160A、160Bで示す)もしくは水砕スラグ製造装置170を構成する水砕スラグ製造ユニット200(図1中、符号200A、200Bで示す)に導かれる。なお、本実施形態において、ドライピット160および水砕スラグ製造ユニット200は、それぞれ2基ずつ設けられているが、3基以上の複数基ずつ設けられていてもよい。すなわち、本実施形態の水砕スラグ製造装置170は、水砕スラグ製造ユニット200A(第1水砕スラグ製造ユニット)および水砕スラグ製造ユニット200B(第2水砕スラグ製造ユニット)を備えているが、3基以上の水砕スラグ製造ユニットが水砕スラグ製造装置に設けられる場合は、そのうち少なくとも2基の水砕スラグ製造ユニットが、本実施形態の水砕スラグ製造ユニット200A、200Bであればよい。 Outside the blast furnace body 110, a tapping iron 120 and a tapping iron 120 through which molten slag flowed out from the tapping port 112 are provided for each tapping port 112. In addition, a skinmer 130 is provided on the tread 120, and the pig iron and the molten slag are separated by the skinmer 130, and the pig iron passes through the tread 120 and the tilting rod 140 to a torpedo car 142 arranged under the casting floor. Led. On the other hand, the molten slag separated from the pig iron by the skinmer 130 is guided to the pole 150 branched from the tread 120 and passed through the pole 150 and the rotary pole 152 through the dry pit 160 ( reference numerals 160A and 160B in FIG. 1). Or a granulated slag production unit 200 (indicated by reference numerals 200A and 200B in FIG. 1) constituting the granulated slag production apparatus 170. In the present embodiment, two each of the dry pit 160 and the granulated slag production unit 200 are provided, but a plurality of three or more units may be provided. That is, the granulated slag production apparatus 170 of the present embodiment includes a granulated slag production unit 200A (first granulated slag production unit) and a granulated slag production unit 200B (second granulated slag production unit). When three or more granulated slag production units are provided in the granulated slag production apparatus, at least two of the granulated slag production units may be the granulated slag production units 200A and 200B of the present embodiment. .
 一般的に高炉本体110では、高炉本体110内の銑鉄および溶融スラグの液位を一定に維持しながら出銑を行うために、複数の出銑口112を高炉本体110に設けておき、複数の出銑口112を交互に開孔して連続的に出銑する。 In general, in the blast furnace main body 110, in order to perform the dredging while maintaining the liquid level of the pig iron and the molten slag in the blast furnace main body 110, a plurality of outlets 112 are provided in the blast furnace main body 110, and a plurality of The spout 112 is opened alternately and continuously spouted.
 具体的に説明すると、図1に示すように、2面鋳床の高炉100では、出銑口112が4つ設けられている。この場合、出銑口112A、または、出銑口112Bを開孔する期間と、出銑口112C、または、出銑口112Dを開孔する期間とを交互にして、ドライピット160Aおよび水砕スラグ製造ユニット200Aと、ドライピット160Bおよび水砕スラグ製造ユニット200Bとを交互に利用する。 More specifically, as shown in FIG. 1, the blast furnace 100 having a double-faced cast floor has four tap holes 112. In this case, the dry pit 160A and the granulated slag are alternately formed by alternately changing the period for opening the tap opening 112A or the tap opening 112B and the period for opening the tap opening 112C or the tap opening 112D. The production unit 200A, the dry pit 160B and the granulated slag production unit 200B are alternately used.
 出銑口112A、または、出銑口112Bを開孔する期間において、一例として出銑口112Aを開孔している間は、出銑口112B、112C、112Dを閉塞しておき、出銑口112Aを通じた出銑が予め定められた期間で実施され、出銑口112Aが拡大して予め定められた大きさになる(出銑末期になる)と、出銑口112C、または、出銑口112Dを開孔し、その後、出銑口112Aを閉塞する。また、出銑口112C、または、出銑口112Dを通じた出銑が予め定められた期間で実施されて出銑末期になると、出銑口112Aを開孔し、その後、出銑口112C、または、出銑口112Dを閉塞する。なお、2つの出銑口112を両方とも開孔させて出銑を行うことをラップ出銑という。同様に、出銑口112Bを開孔している間は、出銑口112A、112C、112Dを閉塞しておき、出銑口112Bを通じた出銑が予め定められた期間で実施されて出銑末期になると、出銑口112C、または、出銑口112Dを開孔し、その後、出銑口112Bを閉塞する。また、出銑口112C、または、出銑口112Dを通じた出銑が予め定められた期間で実施されて出銑末期になると、出銑口112Bを開孔し、その後、出銑口112C、または、出銑口112Dを閉塞する。したがって、ドライピット160A、または、水砕スラグ製造ユニット200Aには、出銑口112A、または、出銑口112Bから出銑(出滓)された溶融スラグが導入され、ドライピット160B、または、水砕スラグ製造ユニット200Bには、出銑口112C、または、出銑口112Dから出銑された溶融スラグが導入される。 As an example, during the period of opening the spout 112A or the spout 112B, while the spout 112A is opened, the spout 112B, 112C, 112D is closed, When the output through 112A is carried out in a predetermined period and the output port 112A expands to a predetermined size (becomes the end of output), the output port 112C or the output port 112D is opened, and then the spout 112A is closed. In addition, when the tapping through the spout 112C or the spout 112D is carried out in a predetermined period and reaches the end of the spout, the spout 112A is opened, and then the spout 112C or The sealing port 112D is closed. In addition, it is called a wrap tapping to perform the tapping with both the tapping holes 112 opened. Similarly, while the spout 112B is opened, the spouts 112A, 112C, and 112D are closed, and the spout through the spout 112B is performed during a predetermined period. At the end stage, the spout 112C or the spout 112D is opened, and then the spout 112B is closed. In addition, when the tapping through the spout 112C or the spout 112D is performed in a predetermined period and reaches the end of the spout, the spout 112B is opened, and then the spout 112C or The sealing port 112D is closed. Therefore, the molten slag extracted from the tap outlet 112A or the tap outlet 112B is introduced into the dry pit 160A or the granulated slag manufacturing unit 200A, and the dry pit 160B or water The crushed slag production unit 200 </ b> B is introduced with molten slag discharged from the tap outlet 112 </ b> C or the tap outlet 112 </ b> D.
 上述した、4つの出銑口112のうち、2つの出銑口112を交互に使用する構成(出銑口112A、112Bのうちいずれか一方の出銑口112と、出銑口112C、112Dのうちいずれか一方の出銑口112を交互に開孔する構成、いわゆる2本廻し)では、使用していない2つの出銑口112のうち一方の出銑口112に対して樋修理(出銑樋120の修理)を施し、他方の出銑口112を乾燥させて待機中としている。 Of the four outlets 112 described above, two outlets 112 are alternately used (one of the outlets 112A and 112B, and the outlets 112C and 112D. In the configuration in which one of the outlets 112 is alternately opened (so-called two-turning), one of the two outlets 112 that is not in use is repaired with respect to one outlet 112. Repair of the ridge 120), the other outlet 112 is dried and is on standby.
 しかし、出銑量を多くする場合等では、4つの出銑口112のうち、3つの出銑口112を順番に使用する構成(3本廻し)を採る(残りの1つの出銑口112に対して樋修理を施す)場合もある。例えば、出銑口112A、112B、112Cを順番に使用する構成を採る場合、出銑口112Aの出銑末期と、出銑口112Bの出銑初期とがラップする期間(出銑口112Aと出銑口112Bとでラップ出銑する期間)があり、このラップ出滓する期間においては、出銑口112Aから出銑滓された溶融スラグおよび出銑口112Bから出銑滓された溶融スラグの両方が、ドライピット160Aまたは水砕スラグ製造ユニット200Aに導入される。 However, in the case of increasing the output amount, etc., a configuration (three rotations) in which the three output ports 112 of the four output ports 112 are used in order (the remaining one output port 112 is used). In some cases, repairs are performed on the heel. For example, when adopting a configuration in which the tap outlets 112A, 112B, and 112C are used in order, a period during which the tap end of the tap outlet 112A and the initial tap output of the tap outlet 112B are wrapped (the tap outlet 112A and the tap out). There is a period during which the lap is taken out at the inlet 112B), and during this lap outlet period, both the molten slag discharged from the outlet 112A and the molten slag discharged from the outlet 112B Is introduced into the dry pit 160A or the granulated slag production unit 200A.
 ドライピット160は、溶融スラグを徐冷してバラス(砂利)を製造する。水砕スラグ製造ユニット200は、溶融スラグを急冷破砕して水砕スラグを製造する。 The dry pit 160 gradually cools the molten slag to produce ballast (gravel). The granulated slag production unit 200 produces a granulated slag by quenching and crushing the molten slag.
 図2は、1つの水砕スラグ製造ユニット200を説明するための図である。図2に示すように、溶融スラグ(図2中、黒い塗りつぶしで示す)は、滓樋150から水砕樋210に落下して流入する。また、水砕樋210には、溶融スラグの流入とともに、水砕スラリー生成部(吹製函)220から多量の加圧水が噴射される。水砕樋210において、溶融スラグに加圧水が噴射されることにより、溶融スラグ(1500℃程度)が100℃未満に急冷されて破砕され、水砕スラグと水との混合物である水砕スラリー(図2中、ハッチングで示す)が生成される。こうして生成された水砕スラリーは、水砕槽230に送出される。 FIG. 2 is a diagram for explaining one granulated slag production unit 200. As shown in FIG. 2, the molten slag (shown in black in FIG. 2) falls from the ridge 150 into the granulated tub 210 and flows in. In addition, a large amount of pressurized water is sprayed from the granulated slurry generation unit (blowing box) 220 together with the inflow of molten slag into the granulated jar 210. In the granulated slag 210, the molten slag (about 1500 ° C.) is rapidly cooled to less than 100 ° C. and crushed by injecting pressurized water into the molten slag, and a granulated slurry (FIG. 5) is a mixture of the granulated slag and water. 2 are indicated by hatching). The granulated slurry thus produced is sent to the granulation tank 230.
 水砕槽230は、水砕スラリーを一時的に貯留し、水砕スラリーから水蒸気を分離する。水砕槽230によって水蒸気が分離された水砕スラリーは、ディストリビュータ240によってインバフィルタ250に導入される。 The granulation tank 230 temporarily stores the granulated slurry and separates water vapor from the granulated slurry. The granulated slurry from which water vapor has been separated by the granulation tank 230 is introduced into the invar filter 250 by the distributor 240.
 図3は、インバフィルタ250を説明するための図であり、図2のIII-III線断面図である。図3に示すように、インバフィルタ250は、軸心が水平方向となるように設置され、複数の孔が形成された円筒型のスクリーン252と、スクリーン252を軸心周りで回転させる不図示の駆動部とを含んで構成される。ディストリビュータ240におけるスクリーン252の内側に配される箇所の下面には、複数の孔242が設けられており、スクリーン252内には、ディストリビュータ240によって水砕スラリー(図3中、ハッチングで示す)が実質的に均一に分散されて落下導入され、スクリーン252によって水砕スラリーが脱水される。 FIG. 3 is a view for explaining the invar filter 250, and is a cross-sectional view taken along line III-III in FIG. As shown in FIG. 3, the invar filter 250 is installed so that its axis is in the horizontal direction, and has a cylindrical screen 252 in which a plurality of holes are formed, and a screen 252 that rotates the screen 252 around the axis. And a drive unit. A plurality of holes 242 are provided in the lower surface of a portion of the distributor 240 that is disposed inside the screen 252, and the granulated slurry (shown by hatching in FIG. 3) is substantially contained in the screen 252 by the distributor 240. The slurry is uniformly dispersed and introduced by dropping, and the granulated slurry is dehydrated by the screen 252.
 また、スクリーン252には、スクリーン252の内壁から中心に向かって立設した掻き板254が複数設けられており、掻き板254はスクリーン252の回転に伴って(図3中、反時計回り)、水砕スラグ(図3中、クロスハッチングで示す)を掻き上げて、排出コンベア260上に落下させる。このようにして水砕スラリーの水から水砕スラグが分離されて脱水される。すなわち、水砕スラグが製造される。インバフィルタ250によって脱水された水砕スラグは、排出コンベア260によってインバフィルタ250外に排出され、インバフィルタ250から落下した水(水砕スラリーから分離された水、図3中、白い塗りつぶしで示す)は、インバフィルタ250の下方に設けられた集水槽290に貯留される。 Further, the screen 252 is provided with a plurality of scraping plates 254 erected from the inner wall of the screen 252 toward the center. The scraping plates 254 are rotated in accordance with the rotation of the screen 252 (counterclockwise in FIG. 3). The granulated slag (indicated by cross hatching in FIG. 3) is scraped and dropped onto the discharge conveyor 260. Thus, the granulated slag is separated from the water of the granulated slurry and dehydrated. That is, granulated slag is produced. The granulated slag dehydrated by the inva filter 250 is discharged out of the inva filter 250 by the discharge conveyor 260 and falls from the inva filter 250 (water separated from the granulated slurry, shown in white in FIG. 3). Is stored in a water collection tank 290 provided below the inva filter 250.
 図2に戻って説明すると、インバフィルタ250によって脱水され、排出コンベア260によって搬送された水砕スラグ(図2中、クロスハッチングで示す)は、輸送コンベア270を介して、製品槽280に供給される。 Returning to FIG. 2, the granulated slag (denoted by cross hatching in FIG. 2) dehydrated by the inva filter 250 and conveyed by the discharge conveyor 260 is supplied to the product tank 280 via the transport conveyor 270. The
 一方、インバフィルタ250によって水砕スラリーから分離され、集水槽290に貯留された水は、オーバーフローによって、温水槽300に導入される。温水槽300に導入された水(90℃程度)は、温水ポンプ310によって冷却塔320に送出され、冷却塔320において50℃~60℃程度に冷却される。こうして冷却された水は、冷水ポンプ330によって水砕スラリー生成部220に返送されることで、水砕スラグ製造ユニット200を循環する。 On the other hand, the water separated from the granulated slurry by the Inba filter 250 and stored in the water collecting tank 290 is introduced into the hot water tank 300 by overflow. Water (about 90 ° C.) introduced into the hot water tank 300 is sent to the cooling tower 320 by the hot water pump 310 and is cooled to about 50 ° C. to 60 ° C. in the cooling tower 320. The water thus cooled is circulated through the granulated slag manufacturing unit 200 by being returned to the granulated slurry generation unit 220 by the cold water pump 330.
 以上説明したように、水砕スラグ製造ユニット200においては、水砕スラグが製造され、ドライピット160においては、バラスが製造される。水砕スラグは、バラスと比較して需要が多いため、高炉から排出される溶融スラグ全量を水砕スラグ製造ユニット200に導入したいという要望がある。しかし、出銑末期や、ラップ出銑を行っている際には、1つの水砕スラグ製造ユニット200のみでは溶融スラグ全量を処理できない場合がある。この場合、溶融スラグの送出先を水砕スラグ製造ユニット200からドライピット160へ切り換えなければならず、水砕スラグの製造効率が低下する。そこで、本実施形態では、溶融スラグの処理(水砕スラグの製造)を行っていない、または、出銑初期等であって水砕処理量に余裕のある水砕スラグ製造ユニット200を活用する送出装置400を水砕スラグ製造装置170に設けることで、水砕スラグの製造効率の向上を図る。以下、送出装置400の構成について説明する。 As described above, in the granulated slag production unit 200, granulated slag is produced, and in the dry pit 160, ballast is produced. Since granulated slag is more demanding than ballast, there is a desire to introduce the entire amount of molten slag discharged from the blast furnace into the granulated slag production unit 200. However, at the end of the brewing process or during the lapping process, there are cases where the entire amount of the molten slag cannot be processed by only one granulated slag production unit 200. In this case, the delivery destination of the molten slag must be switched from the granulated slag production unit 200 to the dry pit 160, and the production efficiency of the granulated slag decreases. Therefore, in this embodiment, molten slag processing (manufacture of granulated slag) is not performed, or sending using a granulated slag production unit 200 that is in the initial stage of brewing and has a sufficient amount of granulation processing. By providing the apparatus 400 in the granulated slag production apparatus 170, the production efficiency of the granulated slag is improved. Hereinafter, the configuration of the sending device 400 will be described.
(送出装置400)
 図4は、水砕スラグ製造装置170を構成する送出装置400を説明するための図である。図4に示すように、送出装置400は、送出配管410と、ポンプ420と、遮断弁430と、スラグ制御部440とを含んで構成される。
(Sending device 400)
FIG. 4 is a diagram for explaining a delivery device 400 that constitutes the granulated slag production apparatus 170. As shown in FIG. 4, the delivery device 400 includes a delivery pipe 410, a pump 420, a shut-off valve 430, and a slag control unit 440.
 送出配管410(図4中、符号410A、410Bで示す)は、水砕スラグ製造ユニット200Aの水砕槽230と、水砕スラグ製造ユニット200Bの水砕槽230とを接続する配管である。ポンプ420(図4中、符号420A、420Bで示す)は、送出配管410に水砕スラリーを流通させる。遮断弁430(図4中、符号430A、430Bで示す)は、送出配管410におけるポンプ420の上流側に設けられる。 The delivery pipe 410 (indicated by reference numerals 410A and 410B in FIG. 4) is a pipe that connects the granulated tank 230 of the granulated slag production unit 200A and the granulated tank 230 of the granulated slag production unit 200B. A pump 420 (indicated by reference numerals 420 </ b> A and 420 </ b> B in FIG. 4) causes the granulated slurry to flow through the delivery pipe 410. The shut-off valve 430 (indicated by reference numerals 430A and 430B in FIG. 4) is provided on the upstream side of the pump 420 in the delivery pipe 410.
 本実施形態の送出配管410Aは、水砕スラグ製造ユニット200Aで生成された水砕スラリーを、水砕スラグ製造ユニット200Bのインバフィルタ250に送出するように構成されている。そのため、少なくとも送出配管410Aが、本発明の第1送出部に相当する。また、本実施形態の送出配管410Bは、水砕スラグ製造ユニット200Bで生成された水砕スラリーを、水砕スラグ製造ユニット200Aのインバフィルタ250に送出するように構成されている。そのため、少なくとも送出配管410Bが、本発明の第2送出部に相当する。 The delivery pipe 410A of the present embodiment is configured to send the granulated slurry generated by the granulated slag production unit 200A to the inva filter 250 of the granulated slag production unit 200B. Therefore, at least the delivery pipe 410A corresponds to the first delivery unit of the present invention. Further, the delivery pipe 410B of the present embodiment is configured to send the granulated slurry generated by the granulated slag production unit 200B to the inva filter 250 of the granulated slag production unit 200A. Therefore, at least the delivery pipe 410B corresponds to the second delivery unit of the present invention.
 スラグ制御部440は、例えば、CPU(中央処理装置)を含む半導体集積回路で構成され、ROMからCPU自体を動作させるためのプログラムやパラメータ等を読み出し、ワークエリアとしてのRAMや他の電子回路と協働して送出装置400全体を管理および制御する。本実施形態において、スラグ制御部440は、ポンプ420、遮断弁430を制御する。スラグ制御部440によるポンプ420、遮断弁430の具体的な制御処理については、後に詳述する。 The slag control unit 440 is composed of, for example, a semiconductor integrated circuit including a CPU (Central Processing Unit), reads a program, parameters, and the like for operating the CPU itself from the ROM, and serves as a RAM and other electronic circuits as a work area. The entire delivery device 400 is managed and controlled in cooperation. In the present embodiment, the slag control unit 440 controls the pump 420 and the shutoff valve 430. Specific control processing of the pump 420 and the shutoff valve 430 by the slag control unit 440 will be described in detail later.
 送出装置400では、例えば、水砕スラグ製造ユニット200Aにおいて、出銑口112A、112Bから出滓された溶融スラグの全てを処理できない場合、スラグ制御部440が遮断弁430Aを開弁し、ポンプ420Aを駆動して、水砕スラグ製造ユニット200Aの水砕槽230から水砕スラグ製造ユニット200Bの水砕槽230へ水砕スラリーを送出する。 In the delivery device 400, for example, in the granulated slag manufacturing unit 200A, when all of the molten slag discharged from the outlets 112A and 112B cannot be processed, the slag control unit 440 opens the shutoff valve 430A and the pump 420A. Is driven to feed the granulated slurry from the granulated tank 230 of the granulated slag production unit 200A to the granulated tank 230 of the granulated slag production unit 200B.
 これにより、水砕スラグ製造ユニット200Aにおいて処理できない溶融スラグを、水砕スラグ製造ユニット200Bで処理することができ、インバフィルタ250を構成するスクリーン252の面積を増大させずとも、水砕スラグ製造装置170における水砕スラグの製造効率を向上することが可能となる。 As a result, the molten slag that cannot be processed in the granulated slag production unit 200A can be treated in the granulated slag production unit 200B, and the granulated slag production apparatus can be used without increasing the area of the screen 252 constituting the invar filter 250. The production efficiency of the granulated slag at 170 can be improved.
 また、送出装置400では、水砕スラグ製造ユニット200Bが、出銑口112C、112Dから出滓された溶融スラグの全てを処理できない場合、スラグ制御部440が遮断弁430Bを開弁し、ポンプ420Bを駆動して、水砕スラグ製造ユニット200Bの水砕槽230から水砕スラグ製造ユニット200Aの水砕槽230へ水砕スラリーを送出する。この場合にも、水砕スラグ製造ユニット200Bにおいて処理できない溶融スラグを、水砕スラグ製造ユニット200Aで処理することができ、水砕スラグ製造装置170における水砕スラグの製造効率を向上できる。 Moreover, in the delivery apparatus 400, when the granulated slag manufacturing unit 200B cannot process all of the molten slag discharged from the outlets 112C and 112D, the slag control unit 440 opens the shut-off valve 430B and the pump 420B. Is driven to feed the granulated slurry from the granulated tank 230 of the granulated slag production unit 200B to the granulated tank 230 of the granulated slag production unit 200A. Also in this case, the molten slag that cannot be processed in the granulated slag production unit 200B can be treated in the granulated slag production unit 200A, and the production efficiency of the granulated slag in the granulated slag production apparatus 170 can be improved.
(水砕スラグ製造方法)
 続いて、上記水砕スラグ製造装置170を用いた水砕スラグ製造方法について説明する。図5は、水砕スラグ製造方法の処理の流れを説明するためのフローチャートである。本実施形態では、出銑口112A、および、出銑口112Bでラップ出滓する場合を例に挙げて説明する。また、水砕スラグ製造の開始時には、遮断弁430は閉弁され、ポンプ420は停止されている。
(Granulated slag manufacturing method)
Then, the granulated slag manufacturing method using the said granulated slag manufacturing apparatus 170 is demonstrated. FIG. 5 is a flowchart for explaining the flow of processing of the granulated slag manufacturing method. In the present embodiment, a case where a lap is carried out at the spout 112A and the spout 112B will be described as an example. At the start of granulated slag production, the shutoff valve 430 is closed and the pump 420 is stopped.
 まず、水砕スラグ製造ユニット200Aの水砕スラリー生成部220は、溶融スラグに加圧水を噴射して、水砕スラリーを生成する(水砕スラリー生成工程S110、生成工程)。続いて、水砕スラグ製造ユニット200Aのインバフィルタ250は、水砕スラリー生成工程S110で生成された水砕スラリーを脱水して水砕スラグを製造する(水砕スラグ製造工程S120、第1製造工程)。 First, the granulated slurry production unit 220 of the granulated slag production unit 200A injects pressurized water into the molten slag to produce a granulated slurry (granulated slurry production step S110, production step). Subsequently, the invar filter 250 of the granulated slag production unit 200A dehydrates the granulated slurry produced in the granulated slurry production step S110 to produce granulated slag (granulated slag production step S120, first production step). ).
 続いて、スラグ制御部440は、予め定められた切換条件を満たすか否かを判定する(判定工程S130)。 Subsequently, the slag control unit 440 determines whether or not a predetermined switching condition is satisfied (determination step S130).
 この切換条件は、例えば、輸送コンベア270で輸送される水砕スラグの重量が予め定められた重量設定値以上となることや、スクリーン252のトルクが予め定められたトルク設定値以上となることが挙げられる。 For example, the switching condition may be that the weight of the granulated slag transported by the transport conveyor 270 is equal to or greater than a predetermined weight set value, or the torque of the screen 252 is equal to or greater than a predetermined torque set value. Can be mentioned.
 スラグ制御部440は、切換条件を満たさなければ(S130におけるNO)、水砕スラグ製造ユニット200Aにおいて水砕槽230からインバフィルタ250への水砕スラリーの導入を維持して、水砕スラグ製造方法の処理を終了する。なお、図5に示すフローチャートは、本実施形態の送出装置400の使用の要否を判断する工程を示しているため、例えば一定期間毎に図5に示す工程を実施し、送出装置400の要否を判断する。 If the switching condition is not satisfied (NO in S130), the slag control unit 440 maintains the introduction of the granulated slurry from the granulation tank 230 to the inva filter 250 in the granulated slag production unit 200A, and the granulated slag production method Terminate the process. Note that the flowchart shown in FIG. 5 shows the process of determining whether or not the sending apparatus 400 of this embodiment is necessary, and therefore, for example, the process shown in FIG. Determine no.
 一方、スラグ制御部440は、切換条件を満たすと(S130におけるYES)、遮断弁430Aを開弁し(開弁工程S140)、ポンプ420Aを駆動して(ポンプ駆動工程S150)、水砕スラグ製造ユニット200Aにおいて生成された水砕スラリーを水砕スラグ製造ユニット200Bに送出する(送出工程)。続いて、水砕スラグ製造ユニット200Bは、水砕スラグ製造ユニット200Aから送出された水砕スラリーを脱水して水砕スラグを製造する(水砕スラグ製造工程S160、第2製造工程)。なお、水砕スラグ製造ユニット200Bにおいても水砕スラリーが生成されている場合は、水砕スラグ製造ユニット200Bは、水砕スラグ製造ユニット200Aから送出された水砕スラリーと水砕スラグ製造ユニット200Bで生成された水砕スラリーとを共に脱水して水砕スラグを製造する(第2製造工程)。また、上述したように、図5に示すフローチャートは送出装置400の使用の要否を判断する工程を示しているため、図5は必ず水砕スラグ製造工程S120の後に水砕スラグ製造工程S160が実施されることを示すものではなく、実際にはこれらの製造工程は同時に行われてもよい。 On the other hand, when the switching condition is satisfied (YES in S130), the slag control unit 440 opens the shut-off valve 430A (valve opening step S140), drives the pump 420A (pump driving step S150), and produces granulated slag. The granulated slurry generated in the unit 200A is sent to the granulated slag manufacturing unit 200B (feeding step). Subsequently, the granulated slag production unit 200B dehydrates the granulated slurry sent from the granulated slag production unit 200A to produce a granulated slag (a granulated slag production process S160, a second production process). In addition, when the granulated slurry is produced | generated also in the granulated slag manufacturing unit 200B, the granulated slag manufacturing unit 200B is the granulated slurry sent from the granulated slag manufacturing unit 200A and the granulated slag manufacturing unit 200B. The produced granulated slurry is dehydrated together to produce granulated slag (second production step). Further, as described above, since the flowchart shown in FIG. 5 shows the process of determining whether or not the delivery device 400 is necessary, FIG. 5 always shows that the granulated slag manufacturing process S160 is performed after the granulated slag manufacturing process S120. It does not indicate that it is carried out, and in fact, these manufacturing steps may be performed simultaneously.
 以上説明したように、本実施形態にかかる水砕スラグ製造方法により、水砕スラグ製造ユニット200Aにおいて処理できない溶融スラグを、水砕スラグ製造ユニット200Bで処理することができ、水砕スラグの製造効率を向上することが可能となる。 As explained above, by the granulated slag production method according to the present embodiment, the molten slag that cannot be treated in the granulated slag production unit 200A can be treated in the granulated slag production unit 200B, and the production efficiency of the granulated slag Can be improved.
 また、上述したように、送出装置400の送出配管410Bは、水砕スラグ製造ユニット200Bで生成された水砕スラリーを、水砕スラグ製造ユニット200Aのインバフィルタ250に送出するように構成されている。このため、水砕スラグ製造ユニット200Bにおいて処理できない溶融スラグを、水砕スラグ製造ユニット200Aに送出して処理することができ、水砕スラグの製造効率を向上させることができる。なお、送出配管410Bを使用するか否かの判断は、図5に示すフローチャートと同様の工程で判断すればよい。 Further, as described above, the delivery pipe 410B of the delivery device 400 is configured to send the granulated slurry generated by the granulated slag production unit 200B to the invar filter 250 of the granulated slag production unit 200A. . For this reason, the molten slag which cannot be processed in the granulated slag production unit 200B can be sent to the granulated slag production unit 200A for processing, and the production efficiency of the granulated slag can be improved. Whether or not the delivery pipe 410B is to be used may be determined in the same process as the flowchart shown in FIG.
 このように、送出装置400は送出配管410A、410Bを備えているため、水砕スラリーの送出方向は一方向に限定されておらず、送出装置400は、複数の水砕スラグ製造ユニット(インバフィルタ)の処理状況に応じて、水砕スラリーの送出方向を適宜変更することができる。言い換えれば、送出装置400は、複数の水砕スラグ製造ユニット200のうち、1の水砕スラグ製造ユニット200の処理能力(脱水能力)が不足するときに、当該1の水砕スラグ製造ユニット200で生成された水砕スラリーを、他の水砕スラグ製造ユニットに送出するように構成されている。よって、複数の水砕スラグ製造ユニット(インバフィルタ)の処理状況に応じて、水砕スラグの製造を柔軟に行うことができる。 Thus, since the delivery apparatus 400 is provided with delivery piping 410A, 410B, the delivery direction of the granulated slurry is not limited to one direction, and the delivery apparatus 400 includes a plurality of granulated slag production units (invar filters). ) Can be changed as appropriate according to the processing status of the slurry. In other words, when the processing capacity (dewatering capacity) of one granulated slag production unit 200 is insufficient among the plurality of granulated slag production units 200, the delivery device 400 is the one granulated slag production unit 200. It is comprised so that the produced | generated granulated slurry may be sent to another granulated slag manufacturing unit. Therefore, according to the processing condition of a plurality of granulated slag production units (inva filters), granulated slag can be flexibly produced.
(変形例)
 図6は、本発明の変形例にかかる送出装置500を説明するための図である。変形例の送出装置500は、上記送出配管410、ポンプ420、遮断弁430、スラグ制御部440に加えて、バッファタンク510と、空気排出管520と、洗浄機構530とを含んで構成される。なお、本変形例では、送出配管410Aに配されるバッファタンク510、空気排出管520、洗浄機構530について説明し、送出配管410Bに配されるバッファタンク510、空気排出管520、洗浄機構530については、送出配管410Aに配される上記構成と実質的に機能が等しいため、説明を省略する。
(Modification)
FIG. 6 is a diagram for explaining a sending device 500 according to a modification of the present invention. The delivery device 500 of the modified example includes a buffer tank 510, an air discharge pipe 520, and a cleaning mechanism 530 in addition to the delivery pipe 410, the pump 420, the shutoff valve 430, and the slag control unit 440. In this modification, the buffer tank 510, the air discharge pipe 520, and the cleaning mechanism 530 disposed in the delivery pipe 410A will be described, and the buffer tank 510, the air discharge pipe 520, and the washing mechanism 530 disposed in the delivery pipe 410B will be described. Since the function is substantially the same as the said structure distribute | arranged to the delivery piping 410A, description is abbreviate | omitted.
 バッファタンク510は、遮断弁430Aとポンプ420Aとの間に設けられ、水砕スラリーを貯留する。なお、遮断弁430Aから延在した送出配管410Aは、バッファタンク510の上部に接続され、ポンプ420Aから延在した送出配管410Aは、バッファタンク510の下部に接続される。バッファタンク510に水砕スラリーを貯留することにより、水砕槽230において混入された空気を、水砕スラリーから分離することができる。また、バッファタンク510の上面には、空気排出管520が設けられており、バッファタンク510において分離された空気を水砕槽230に排出する。 The buffer tank 510 is provided between the shut-off valve 430A and the pump 420A, and stores the granulated slurry. The delivery pipe 410A extending from the shutoff valve 430A is connected to the upper part of the buffer tank 510, and the delivery pipe 410A extending from the pump 420A is connected to the lower part of the buffer tank 510. By storing the granulated slurry in the buffer tank 510, the air mixed in the granulated tank 230 can be separated from the granulated slurry. Further, an air discharge pipe 520 is provided on the upper surface of the buffer tank 510, and the air separated in the buffer tank 510 is discharged to the water granulation tank 230.
 バッファタンク510を備える構成により、水砕槽230において分離できなかった空気のポンプ420Aへの導入を防止することができる。また、水砕槽230における水砕スラリーの液面が低下することによるポンプ420Aへの空気の導入を防止することができる。これにより、ポンプ420Aを安定して運転することが可能となる。 With the configuration including the buffer tank 510, it is possible to prevent the introduction of air that could not be separated in the water granulating tank 230 into the pump 420A. Further, it is possible to prevent the introduction of air into the pump 420A due to a decrease in the level of the granulated slurry in the granulating tank 230. As a result, the pump 420A can be stably operated.
 洗浄機構530は、遮断弁430Aとバッファタンク510との間の送出配管410Aに接続される洗浄配管532と、洗浄配管532を通じて、送出配管410Aに洗浄水を供給する洗浄水ポンプ534とを含んで構成される。 The cleaning mechanism 530 includes a cleaning pipe 532 connected to the delivery pipe 410A between the shutoff valve 430A and the buffer tank 510, and a washing water pump 534 that supplies washing water to the delivery pipe 410A through the washing pipe 532. Composed.
 送出配管410Aには、常時水砕スラリーが導入されるわけではなく、切換条件を満たした場合にのみ水砕スラリーが導入される。したがって、水砕スラリーが導入されない期間において、送出配管410A内で水砕スラリーが固着してしまう可能性がある。 The granulated slurry is not always introduced into the delivery pipe 410A, but is introduced only when the switching condition is satisfied. Therefore, there is a possibility that the granulated slurry is fixed in the delivery pipe 410A during the period when the granulated slurry is not introduced.
 そこで、洗浄機構530を備える構成により、水砕スラリーの送出配管410A内への導入が停止した後、送出配管410A内、ポンプ420A、遮断弁430A、バッファタンク510を洗浄水で洗浄することができる。これにより、送出配管410A内、ポンプ420A、遮断弁430A、バッファタンク510における水砕スラリーの固着を防止することが可能となる。 Therefore, the configuration including the cleaning mechanism 530 allows the water supply slurry 410A, the pump 420A, the shutoff valve 430A, and the buffer tank 510 to be cleaned with the cleaning water after the introduction of the granulated slurry into the supply piping 410A is stopped. . As a result, it is possible to prevent adhesion of the granulated slurry in the delivery pipe 410A, the pump 420A, the shutoff valve 430A, and the buffer tank 510.
 以上、添付図面を参照しながら本発明の好適な実施形態について説明したが、本発明はかかる実施形態に限定されない。当業者であれば、請求の範囲に記載された範囲において、各種の変更例または修正例を想到でき、それらについても当然に本発明の技術的範囲に属する。 The preferred embodiments of the present invention have been described above with reference to the accompanying drawings, but the present invention is not limited to such embodiments. A person skilled in the art can conceive various changes or modifications within the scope of the claims, and these naturally belong to the technical scope of the present invention.
 例えば、上記実施形態において、送出装置400が、送出配管410、ポンプ420、遮断弁430、スラグ制御部440を含んで構成される例について説明した。しかし、送出装置は、1の水砕スラグ製造ユニット200の水砕スラリー生成部220によって生成された水砕スラリーを、他の水砕スラグ製造ユニット200のインバフィルタ250に送出することができれば構成に限定はない。 For example, in the above embodiment, the example in which the delivery device 400 includes the delivery pipe 410, the pump 420, the shutoff valve 430, and the slag control unit 440 has been described. However, the delivery device has a configuration as long as the granulated slurry generated by the granulated slurry production unit 220 of one granulated slag production unit 200 can be delivered to the invar filter 250 of another granulated slag production unit 200. There is no limitation.
 また、上記実施形態において、送出配管410が、水砕槽230同士を接続する構成を例に挙げて説明した。しかし、送出配管は、水砕スラリー生成部220の下流側であってインバフィルタ250の上流側のいずれかの箇所(例えば、水砕樋210、ディストリビュータ240)を互いに接続していてもよい。例えば、送出配管は、1の水砕スラグ製造ユニット200における水砕樋210と水砕槽230とディストリビュータ240とのいずれか1つと、他の水砕スラグ製造ユニット200における水砕樋210と水砕槽230とディストリビュータ240とのいずれか1つを互いに接続していてもよい。 Moreover, in the said embodiment, the delivery piping 410 demonstrated and demonstrated the structure which connects the granulation tanks 230 as an example. However, the delivery pipe may be connected to any part (for example, the water granule 210 and the distributor 240) on the downstream side of the granulated slurry generation unit 220 and on the upstream side of the invar filter 250. For example, the delivery pipe includes any one of the granulated slag 210, the granulated tank 230, and the distributor 240 in one granulated slag production unit 200, and the granulated slag 210 and the granulated water in another granulated slag production unit 200. Any one of the tank 230 and the distributor 240 may be connected to each other.
 また上記実施形態において、送出装置400が遮断弁430を備える構成について説明したが、送出装置は、遮断弁を備えずともよい。この場合、例えばポンプ420の駆動によって、水砕スラリーの送出の有無が決定される。 In the above embodiment, the configuration in which the delivery device 400 includes the cutoff valve 430 has been described. However, the delivery device may not include the cutoff valve. In this case, for example, whether or not the granulated slurry is delivered is determined by driving the pump 420.
 また、上記実施形態においては、2面鋳床の高炉100について説明したが、例えば、3面鋳床の高炉であってもよい。いずれにしても、複数基の水砕スラグ製造ユニット200を備えていれば、送出装置400が、1の水砕スラグ製造ユニット200の水砕スラリー生成部220によって生成された水砕スラリーを、他の水砕スラグ製造ユニット200のインバフィルタ250に送出することができ、水砕スラグの製造効率を向上することが可能となる。 In the above-described embodiment, the blast furnace 100 having a two-face cast floor has been described. In any case, as long as a plurality of granulated slag production units 200 are provided, the delivery device 400 uses the granulated slurry produced by the granulated slurry production unit 220 of one granulated slag production unit 200 as the other. This can be sent to the INVA filter 250 of the granulated slag production unit 200, and the production efficiency of the granulated slag can be improved.
 また、上記実施形態では、水砕スラグ製造装置170が水砕スラグ製造ユニット200を2基備える構成について説明したが、水砕スラグ製造ユニット200は、3基以上であってもよい。 Moreover, although the granulated slag manufacturing apparatus 170 demonstrated the structure provided with the two granulated slag manufacturing units 200 in the said embodiment, the number of the granulated slag manufacturing units 200 may be three or more.
 また、上記実施形態において、溶融スラグが、水砕スラグ製造ユニット200、または、ドライピット160に導かれる構成を例に挙げて説明した。しかし、ドライピット160に代えて、滓鍋で受滓する滓鍋方式による受滓装置を採用してもよい。 In the above-described embodiment, the configuration in which the molten slag is guided to the granulated slag manufacturing unit 200 or the dry pit 160 has been described as an example. However, instead of the dry pit 160, a ladle-type receiving device that receives a hot pot may be adopted.
 また、上記実施形態において、滓樋150を流れる溶融スラグの導入先を、ドライピット160または水砕スラグ製造ユニット200に切り換える切換装置として、回転樋152を例に挙げて説明した。しかし、切換装置に限定はなく、例えば、ドライピット160のみに連通する滓樋150および水砕スラグ製造ユニット200のみに連通する滓樋150のそれぞれに、溶融スラグの流れを堰き止めるストッパを設けておき、ストッパを上下させることで、溶融スラグの導入先を、ドライピット160または水砕スラグ製造ユニット200に切り換えてもよい。 In the above-described embodiment, the rotary rod 152 has been described as an example of the switching device that switches the introduction destination of the molten slag flowing through the rod 150 to the dry pit 160 or the granulated slag production unit 200. However, the switching device is not limited, and for example, a stopper for blocking the flow of the molten slag is provided on each of the dredger 150 communicating only with the dry pit 160 and the dredger 150 communicating only with the granulated slag production unit 200. Alternatively, the introduction destination of the molten slag may be switched to the dry pit 160 or the granulated slag production unit 200 by moving the stopper up and down.
 スラグ制御部440が、CPUを含む半導体集積回路で構成される場合を例に挙げて説明したが、DSC、PLC(Programmable Logic Controller)、リレー盤等であってもよい。また、水砕スラグ製造装置170は、スラグ制御部440を備えずともよい。例えば、スクリーンのトルク(駆動部のトルク)が設定値を超えた場合にアラームを発生するように構成し、アラームの発生に基づいて、作業者が送出装置の動作を切り替えてもよい。 Although the case where the slag control unit 440 is configured by a semiconductor integrated circuit including a CPU has been described as an example, it may be a DSC, a PLC (Programmable Logic Controller), a relay board, or the like. Moreover, the granulated slag manufacturing apparatus 170 may not include the slag control unit 440. For example, an alarm may be generated when the screen torque (torque of the drive unit) exceeds a set value, and the operator may switch the operation of the delivery device based on the occurrence of the alarm.
 上記実施形態では、送出装置400は、送出配管410A、410Bを備えているが、本発明はこの構成に限定されない。送出装置が2つの水砕スラグ製造ユニットを接続する1つの送出配管を備え、この送出配管に水砕スラリーの流動方向を変更可能なポンプ等を設けて、2つの水砕スラグ製造ユニット間の水砕スラリーの送出方向を変更できるように構成してもよい。この場合、この1つの送出配管が本発明の第1、第2送出部のいずれにも相当する。 In the above embodiment, the delivery device 400 includes delivery pipes 410A and 410B, but the present invention is not limited to this configuration. The delivery device is provided with one delivery pipe that connects two granulated slag production units, a pump that can change the flow direction of the granulated slurry is provided in the delivery pipe, and water between the two granulated slag production units is provided. You may comprise so that the delivery direction of crushed slurry can be changed. In this case, this one delivery pipe corresponds to both the first and second delivery parts of the present invention.
 また、複数の水砕スラグ製造ユニットのうち、特定の水砕スラグ製造ユニットのみの処理能力(脱水能力)が不足する場合には、2つの水砕スラグ製造ユニットを1つの送出配管で接続し、その送出方向を一方向に固定してもよい。例えば、上記実施形態において、水砕スラグ製造ユニット200Aのみの処理能力が不足する場合は、送出配管410Aのみが設けられ、送出配管410Bが設けられなくともよい。なお、送出配管は、水砕スラリーを流動させることのできる流動経路であればよく、例えば樋でもよい。 Moreover, when the processing capacity (dewatering capacity) of only a specific granulated slag production unit among a plurality of granulated slag production units is insufficient, two granulated slag production units are connected by one delivery pipe, The sending direction may be fixed in one direction. For example, in the above embodiment, when the processing capacity of only the granulated slag manufacturing unit 200A is insufficient, only the delivery pipe 410A is provided, and the delivery pipe 410B may not be provided. In addition, the delivery piping should just be a flow path | route which can make a granulated slurry flow, for example, a soot may be sufficient.
 本発明は、高炉から排出された溶融スラグから水砕スラグを製造する水砕スラグ製造装置、および、水砕スラグ製造方法に利用することができる。 The present invention can be used in a granulated slag production apparatus and a granulated slag production method for producing granulated slag from molten slag discharged from a blast furnace.
170  水砕スラグ製造装置
200  水砕スラグ製造ユニット
200A 水砕スラグ製造ユニット(第1水砕スラグ製造ユニット)
200B 水砕スラグ製造ユニット(第2水砕スラグ製造ユニット)
220  水砕スラリー生成部
230  水砕槽
250  インバフィルタ
400  送出装置
410  送出配管
410A 送出配管(第1送出部)
410B 送出配管(第2送出部)
420  ポンプ
430  遮断弁
500  送出装置
510  バッファタンク
170 Granulated slag production apparatus 200 Granulated slag production unit 200A Granulated slag production unit (first granulated slag production unit)
200B Granulated slag production unit (2nd granulated slag production unit)
220 Granulated slurry generator 230 Granulated tank 250 Inver filter 400 Sending device 410 Sending pipe 410A Sending pipe (first sending part)
410B Delivery pipe (second delivery part)
420 Pump 430 Shut-off valve 500 Delivery device 510 Buffer tank

Claims (8)

  1.  第1、第2水砕スラグ製造ユニットを備える水砕スラグ製造装置であって、
     前記第1、第2水砕スラグ製造ユニットは、それぞれ、高炉本体から排出された溶融スラグに水を噴射して水砕スラリーを生成する水砕スラリー生成部と、前記水砕スラリーを脱水して水砕スラグを製造するインバフィルタと、を備え、
     前記第1水砕スラグ製造ユニットの前記水砕スラリー生成部によって生成された水砕スラリーを、前記第2水砕スラグ製造ユニットの前記インバフィルタに送出する送出装置をさらに備える水砕スラグ製造装置。
    A granulated slag production apparatus comprising first and second granulated slag production units,
    Each of the first and second granulated slag production units dehydrates the granulated slurry and a granulated slurry generator that injects water into the molten slag discharged from the blast furnace body to generate a granulated slurry. An inba filter for producing granulated slag,
    The granulated slag production apparatus further comprising a delivery device that sends the granulated slurry produced by the granulated slurry production unit of the first granulated slag production unit to the invar filter of the second granulated slag production unit.
  2.  前記第1、第2水砕スラグ製造ユニットは、それぞれ、前記水砕スラリー生成部が生成した水砕スラリーを貯留して該水砕スラリーから水蒸気を分離する水砕槽をさらに備え、
     前記送出装置は、前記第1水砕スラグ製造ユニットの前記水砕槽内の水砕スラリーを前記第2水砕スラグ製造ユニットに送出するように構成されている請求項1に記載の水砕スラグ製造装置。
    Each of the first and second granulated slag production units further includes a granulation tank that stores the granulated slurry generated by the granulated slurry generation unit and separates water vapor from the granulated slurry.
    The granulated slag according to claim 1, wherein the delivery device is configured to deliver the granulated slurry in the granulated tank of the first granulated slag production unit to the second granulated slag production unit. Manufacturing equipment.
  3.  前記送出装置は、前記第1水砕スラグ製造ユニットの前記水砕槽と前記第2水砕スラグ製造ユニットの前記水砕槽とを接続している請求項2に記載の水砕スラグ製造装置。 The granulated slag production apparatus according to claim 2, wherein the delivery device connects the granulation tank of the first granulated slag production unit and the granulation tank of the second granulated slag production unit.
  4.  前記送出装置は、前記第1水砕スラグ製造ユニットにおける前記水砕スラリー生成部の下流側から延在した送出配管と、前記送出配管に前記水砕スラリーを流通させるポンプと、を備える請求項1から3のいずれか1項に記載の水砕スラグ製造装置。 The said delivery apparatus is equipped with the delivery piping extended from the downstream of the said granulated slurry production | generation part in the said 1st granulated slag manufacturing unit, and the pump which distribute | circulates the said granulated slurry to the said delivery piping. 4. The granulated slag production apparatus according to any one of items 1 to 3.
  5.  前記ポンプは、前記送出配管に設けられ、
     前記送出装置は、前記送出配管における前記ポンプの上流側に設けられた遮断弁をさらに備える請求項4に記載の水砕スラグ製造装置。
    The pump is provided in the delivery pipe,
    The said delivery apparatus is a granulated slag manufacturing apparatus of Claim 4 further provided with the cutoff valve provided in the upstream of the said pump in the said delivery piping.
  6.  前記送出装置は、前記遮断弁と前記ポンプとの間に、前記水砕スラリーを貯留するバッファタンクをさらに備える請求項5に記載の水砕スラグ製造装置。 The granulated slag manufacturing apparatus according to claim 5, wherein the delivery device further includes a buffer tank that stores the granulated slurry between the shut-off valve and the pump.
  7.  前記送出装置は、第1、第2送出部を備え、
     前記第1送出部は、前記第1水砕スラグ製造ユニットで生成された水砕スラリーを前記第2水砕スラグ製造ユニットの前記インバフィルタに送出するように構成され、
     前記第2送出部は、前記第2水砕スラグ製造ユニットで生成された水砕スラリーを前記第1水砕スラグ製造ユニットの前記インバフィルタに送出するように構成されている請求項1に記載の水砕スラグ製造装置。
    The delivery device includes first and second delivery units,
    The first delivery unit is configured to send the granulated slurry generated in the first granulated slag production unit to the invar filter of the second granulated slag production unit,
    The said 2nd sending part is comprised so that the granulated slurry produced | generated by the said 2nd granulated slag manufacturing unit may be sent to the said invar filter of the said 1st granulated slag manufacturing unit. Granulated slag production equipment.
  8.  高炉から排出された溶融スラグから水砕スラグを製造する第1、第2水砕スラグ製造ユニットを用いた水砕スラグ製造方法であって、
     前記第1水砕スラグ製造ユニットにおいて、前記溶融スラグに水を噴射して水砕スラリーを生成する生成工程と、
     前記第1水砕スラグ製造ユニットにおいて生成された前記水砕スラリーを、該第1水砕スラグ製造ユニットにおいて脱水して水砕スラグを製造する第1製造工程と、
     予め定められた条件が満たされたときに、前記第1水砕スラグ製造ユニットにおいて生成された前記水砕スラリーを、前記第2水砕スラグ製造ユニットに送出する送出工程と、
     前記送出工程で前記第1水砕スラグ製造ユニットから前記第2水砕スラグ製造ユニットに送出された前記水砕スラリーを、該第2水砕スラグ製造ユニットにおいて脱水して水砕スラグを製造する第2製造工程と、を含む水砕スラグ製造方法。
    A granulated slag production method using first and second granulated slag production units for producing granulated slag from molten slag discharged from a blast furnace,
    In the first granulated slag production unit, a production step of generating water granulated slurry by injecting water into the molten slag;
    A first production process for producing the granulated slag by dehydrating the granulated slurry generated in the first granulated slag production unit, in the first granulated slag production unit;
    A delivery step of sending the granulated slurry generated in the first granulated slag production unit to the second granulated slag production unit when a predetermined condition is satisfied;
    The granulated slurry sent from the first granulated slag production unit to the second granulated slag production unit in the delivery step is dehydrated in the second granulated slag production unit to produce granulated slag. A granulated slag manufacturing method including two manufacturing steps.
PCT/JP2015/061341 2014-06-23 2015-04-13 Water-granulated-slag manufacturing device and water-granulated-slag manufacturing method WO2015198689A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5443932A (en) * 1977-09-14 1979-04-06 Rasa Corp Water crushing treatment of blast furnace slag
JPS60235749A (en) * 1984-05-04 1985-11-22 日本鋼管株式会社 Facilities for manufacturing water-granulated slag
JPS6230645A (en) * 1985-08-02 1987-02-09 川崎製鉄株式会社 Assumption device for blast furnace slag outgoing speed
JPS62502611A (en) * 1985-04-02 1987-10-08 ア−ヨ・シユタ−ルバウ ゲゼルシヤフト ミツト ベシユレンクテル ハフツング ウント コンパニ− コマンデイ−トゲゼルシヤフト Method and apparatus for producing slag sand (granules) from blast furnace slag

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60195309A (en) 1984-03-16 1985-10-03 Nippon Steel Corp Granulated slag waste heat recovery generating set
JPH08157241A (en) 1994-12-06 1996-06-18 Kawasaki Steel Corp Water-granulated slag dehydrator
JP3630051B2 (en) * 1999-12-20 2005-03-16 Jfeスチール株式会社 Method and equipment for producing granulated slag
JP2002226239A (en) * 2001-01-30 2002-08-14 Kawasaki Steel Corp Method for producing hard granulated slag and apparatus therefor
WO2009069794A1 (en) * 2007-11-26 2009-06-04 Nippon Steel Corporation Method and apparatus for treating high-temperature slag
JP5484850B2 (en) * 2009-09-30 2014-05-07 三菱重工業株式会社 Slag discharge system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5443932A (en) * 1977-09-14 1979-04-06 Rasa Corp Water crushing treatment of blast furnace slag
JPS60235749A (en) * 1984-05-04 1985-11-22 日本鋼管株式会社 Facilities for manufacturing water-granulated slag
JPS62502611A (en) * 1985-04-02 1987-10-08 ア−ヨ・シユタ−ルバウ ゲゼルシヤフト ミツト ベシユレンクテル ハフツング ウント コンパニ− コマンデイ−トゲゼルシヤフト Method and apparatus for producing slag sand (granules) from blast furnace slag
JPS6230645A (en) * 1985-08-02 1987-02-09 川崎製鉄株式会社 Assumption device for blast furnace slag outgoing speed

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