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WO2017061664A1 - Sintered ore manufacturing apparatus and manufacturing method - Google Patents

Sintered ore manufacturing apparatus and manufacturing method Download PDF

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Publication number
WO2017061664A1
WO2017061664A1 PCT/KR2015/014119 KR2015014119W WO2017061664A1 WO 2017061664 A1 WO2017061664 A1 WO 2017061664A1 KR 2015014119 W KR2015014119 W KR 2015014119W WO 2017061664 A1 WO2017061664 A1 WO 2017061664A1
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WO
WIPO (PCT)
Prior art keywords
sintered
raw material
sintering
sintered ore
blended
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Ceased
Application number
PCT/KR2015/014119
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French (fr)
Korean (ko)
Inventor
박종력
양영철
곽성대
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Posco Holdings Inc
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Posco Co Ltd
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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Publication date
Application filed by Posco Co Ltd filed Critical Posco Co Ltd
Priority to DE112015005874.5T priority Critical patent/DE112015005874T5/en
Priority to CN201580074900.3A priority patent/CN107208977A/en
Priority to ATA9484/2015A priority patent/AT518585A2/en
Priority to JP2017536837A priority patent/JP2018505965A/en
Publication of WO2017061664A1 publication Critical patent/WO2017061664A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B21/00Open or uncovered sintering apparatus; Other heat-treatment apparatus of like construction
    • F27B21/06Endless-strand sintering machines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D11/00Arrangement of elements for electric heating in or on furnaces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D15/00Handling or treating discharged material; Supports or receiving chambers therefor
    • F27D15/02Cooling
    • F27D15/0206Cooling with means to convey the charge
    • F27D15/0273Cooling with means to convey the charge on a rotary hearth

Definitions

  • the present invention relates to a sintered ore manufacturing apparatus and a manufacturing method, and more particularly, by minimizing the half-light generation of the upper layer of the sintered trolley by irradiating microwaves on the top of the sintered bogie, to improve the particle size of the sintered ore and increase the sintered ore recovery productivity It relates to a sintered ore manufacturing apparatus and a manufacturing method that can be improved.
  • the sintered ore used as a raw material in the blast furnace accounts for about 80% of the main raw material, the sintered ore is prepared by charging the raw material and the top light in the sintering apparatus and firing at high temperature.
  • FIG. 1 is a schematic view showing a sintering process using a general down suction sintering apparatus
  • FIG. 2 is a view showing a recovery rate by sintering cart position of a conventional general down suction sintering apparatus.
  • the sintering process using a downward suction sintering apparatus is stored in the ore bin (ORE BIN) 10, and the iron ore, secondary raw materials, coke (Coke), and then cut out a certain amount of the drum mixer ( Water is added and mixed in the DRUM MIXER; 11) and stored in the SURGE HOPPER 12.
  • a compounding raw material is prepared by adding, and the compounding raw material prepared as described above is charged to the upper portion of the sintering cart 15 along the inclined plate (Deflector Plate) 16 to induce a classification phenomenon.
  • bogie 15 in which the compounding material loading was completed ignites the compounding material superficial layer part with the flame
  • the suction force is transmitted to the windbox 20 through the chamber 19, and the suction force transmitted to the windbox 20 strongly sucks the lower portion of the sintering cart 15 so that air in the air is charged into the sintering cart 15. Passing from the upper part to the lower part of the blended raw material, the iron ore is agglomerated by high temperature firing to produce a sintered ore.
  • the sintered ore manufacturing process adopts a method of maximizing the quality of the sintered ore and maximizing recovery and productivity while minimizing fuel consumption.
  • the downward suction type sintering apparatus continuously burns the combustion gas under the sintering cart 15. As the air is sucked, the cool air rapidly cools the upper layer formed from the plane of the blended material to one third depth with respect to the entire depth of the sintered bogie 15, so that the upper tier of the sintered bogie 15 occupies about one third of the manufactured sintered ore.
  • the sintered ore does not receive enough heat for sintering, a large amount of semi-glossy particles having a diameter of less than 5 mm is generated, which has a problem in that the recovery rate of the sintered ore is lowered.
  • the present invention has been made to solve the above problems, it is charged into the sinter bogie and passed through the ignition furnace while irradiating microwaves to the plane of the compounding material complexed with the surface layer is supplied by supplying a heat source insufficient in the upper sinter bogie sintered condensation
  • a sintered ore manufacturing apparatus and a manufacturing method that can improve the quality and recovery of the sintered ore by minimizing the generation of semi-glow.
  • the sintered ore manufacturing apparatus in the sintered ore manufacturing apparatus that proceeds the sintering process by connecting a plurality of sintered trolley in an endless track, an upper light hopper for supplying the upper light and the blended raw materials to the sintered trolley respectively Raw material supply including a surge hopper; An ignition furnace disposed at a rear end of the raw material supply part in the advancing direction of the sintered bogie to complex the surface layer portion of the blended raw material charged into the sintered bogie; And a microwave heating furnace disposed at a rear end of the ignition furnace and irradiating microwaves to the surface layer portion of the blended raw material charged into the sintering cart.
  • the microwave heating furnace may be characterized in that for irradiating the microwave with a frequency of 800MHz ⁇ 3kHz.
  • the microwave heating furnace is preferably formed in a tunnel shape in which both ends are opened in the advancing direction of the sintering bogie so that the microwaves can be irradiated onto the surface of the blended material accommodated therein while the sintering bogie passes.
  • the microwave is preferably irradiated with a frequency of 800MHz ⁇ 3kHz.
  • the heating step may be characterized in that for irradiating the microwave for 10 seconds to 3 minutes.
  • the sintered ore quality and recovery rate can be improved It works.
  • FIG. 1 is a schematic view showing a sintering process using a conventional double-low suction sintering apparatus
  • Figure 2 is a view showing the recovery rate for each position of the sintered cart of the conventional general down suction sintering apparatus
  • FIG. 3 is a schematic view showing a sintered ore manufacturing apparatus according to an embodiment of the present invention.
  • FIG. 4 is a view for explaining a microwave heating furnace, according to an embodiment of the present invention.
  • FIG. 5 is a flowchart showing a sintered ore manufacturing method according to an embodiment of the present invention
  • FIG. 6 is a view showing a temperature distribution of a conventional general down suction sintering apparatus and a sintered ore manufacturing apparatus according to an embodiment of the present invention.
  • FIG 3 is a schematic view showing a sintered ore manufacturing apparatus according to an embodiment of the present invention
  • Figure 4 is a view for explaining a microwave heating furnace, according to an embodiment of the present invention.
  • the sintered ore manufacturing apparatus is a raw material supply unit for supplying the raw material into the sintered trolley 15 is connected to a plurality of tracks in the orbit and each of the sintered trolley 15 And an ignition furnace 17 for igniting the surface layer portion of the raw material charged in the) and a microwave heating furnace 30 for irradiating the microwaves to the surface of the raw material charged in the sintering cart 15.
  • the raw material supplied into each of the sintered trolleys 15 is composed of a compound raw material stacked on top of the upper light and the upper light, and the raw material supply part is an upper portion of one side of the path along which the sintered trolley 15 moves along the running rail formed in an endless track.
  • positioned at the rear end of the upper light hopper 14 are comprised.
  • the upper light hopper 14 charges the upper light having a particle size range of 10 to 15 mm in the sintering cart 15 to the sintering cart 15 with a thickness of about 50 mm, and the surge hopper 12 installed at the rear end has a predetermined amount of moisture.
  • the added blending raw material is supplied to the sintering cart 15.
  • the surge hopper 12 is rotated the drum feeder 13 installed in the lower portion of the blended raw material contained in the surge hopper 12 is discharged into the sintering cart 15 and blended according to the rotational speed of the drum feeder 13
  • the discharge amount of the raw material is controlled, and a lower plate (Deflector Plate, 16) is installed at the lower part to induce the classification phenomenon of the mixed raw material is discharged from the surge hopper 12 along the inclined plate (16) It is charged into the sinter cart 15.
  • the ignition furnace 17 is provided with a plurality of burners spaced apart at regular intervals in the width direction of the sintering bogie 15 so as to ignite the surface layer portion of the blended material charged into the sinter bogie 15, and continuously The surface layer portions of the blended raw materials charged into the sintered trolleys 15 to be passed are sequentially fired.
  • the microwave heating furnace 30 is formed in a tunnel shape in which its bottom and both ends are open so that a plurality of sintering trolleys 15 can be continuously passed, and the raw material charged in the sintering trolley 15 passed below.
  • Microwave oscillation means is installed on the ceiling to irradiate the microwaves to the surface layer.
  • microwaves are a form of energy with a low frequency of electromagnetic energy and have a frequency range of 800 to 300,000 MHz, causing only the rotation of molecules within the electromagnetic field range and do not affect the molecular structure.
  • the microwave is composed of an electric field and a magnetic field, of which the electric field serves to heat the material, propagates at the speed of light and the photon energy (0.037kcal / mole) is the energy (80 ⁇ 120kcal / It is lower than mole, so it only heats the material and does not affect the molecular structure.
  • the microwave heating furnace 30 replaces the conventional inefficient conventional heating method by using energy conduction heat, which is slow in energy transfer rate and takes a long time until thermal equilibrium of materials, thereby uniformizing internal and external temperatures. Investigate microwaves that can be heated quickly.
  • the frequency of the microwave used is preferably 800MHz ⁇ 3kHz, the reason is that when the frequency of the microwave exceeds 3kHz the cost is increased and the sintering temperature is excessively raised to improve the quality of the sintered ore produced If it is less than 800MHz, the depth penetrated into the blending material is increased, and the energy density decreases, so that the upper part of the blending material having semi-gloss with a particle size of less than 5 mm is not sufficiently heated, and heating takes a long time. to be.
  • Table 1 is a table showing the temperature measured after 1 minute irradiation of microwave of 2 kW capacity, 2.4 kW for 1 minute with respect to the main components of the blended raw materials charged in the sintering cart.
  • the microwave heating furnace 30 is preferably formed to a length that each sintering cart 15 can pass for 1 to 2 minutes.
  • the length of the microwave heating furnace 30 is preferably formed such that the sintering cart 15 has a passage time of 1 to 2 minutes.
  • Table 2 is a table showing the rate of semi-glow generation according to the microwave irradiation conditions, in the present invention, after the surface of the 120kg blended material is ignited using a flame and irradiated with microwaves (2kW, 2.4GHz) to heat the upper layer, The combustion gas was aspirated at a pressure of 1,600 mmHq from below, and after combustion was completed, the sample was crushed to 50 mm or less, and the drum strength was measured.
  • Microwave (5kW, 2.4GHz) irradiation time Half light generation rate - 33.2% 10 sec 30.7% 30 seconds 24.4% 60 seconds 18.5%
  • Table 3 is a table showing the half light generation ratio according to the irradiation time when the microwave power is increased to 5 kW, it can be seen that the half light generation ratio decreases rapidly in a short time compared to 2 kW of Table 2.
  • FIG. 5 is a flowchart showing a sintered ore manufacturing method according to an embodiment of the present invention.
  • the sintered ore manufacturing method includes a raw material supplying step, an ignition step of complexing the surface of the blended raw material, and a heating step of irradiating microwaves to the surface layer of the blended raw material.
  • the upper light hopper 14 and the surge hopper 12 are sequentially supplied to the inside of the sintered trolley 15 which is moved on the track.
  • the sintered trolley 15 loaded with the raw materials passes through the ignition furnace 17 to ignite the surface layer portion of the blended raw material contained therein.
  • FIG. 6 is a view showing the temperature distribution (a) of the conventional general down suction sintering apparatus and the temperature distribution (b) of the sintered ore manufacturing apparatus according to an embodiment of the present invention.
  • the microwave is 800MHz ⁇ 3 kHz at the surface layer portion of the blended raw material charged in the sintered cart 15 in the heating step Irradiate for 1 to 2 minutes to heat the upper layer of the blended raw material.
  • the cooling temperature can be compensated by continuously inhaling the combustion gas from below to compensate for the cooling temperature of the upper part of the blended raw material, thereby supplying the heat energy necessary for the upper part of the blended raw material charged in the sintered bogie 15, thereby improving the sintered ore quality and recovery rate. There is an effect to improve.
  • heating by using a microwave does not affect the flow of the combustion gas has the effect of making the quality of the sintered ore produced uniformly, improving the productivity.
  • the main blower 18 is operated to generate a suction force under the sinter truck 15 to produce a sintered ore while sucking the combustion gas.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Furnace Details (AREA)

Abstract

A sintered ore manufacturing apparatus according to one embodiment of the present invention performs a sintering process by connecting a plurality of sintering trolleys in a caterpillar form and comprises: a material feeding part including an upper ore hopper and a surge hopper, which respectively feed upper ores and mixed materials into the sintering trolleys; an ignition furnace disposed at the rear end of the material feeding part in the progressing direction of the sintering trolleys so as to ignite a surface layer part of the mixed materials charged in the sintering trolley; and a microwave heating furnace disposed at the rear end of the ignition furnace so as to emit microwaves at the surface layer part of the mixed materials charged in the sintering trolley.

Description

소결광 제조장치 및 제조방법Sintered Ore Manufacturing Equipment

본 발명은 소결광 제조장치 및 제조방법에 관한 것으로서, 보다 상세하게는 소결대차의 상부에 마이크로웨이브를 조사하여 소결대차 상층부의 반광생성을 최소화함으로써, 소결광의 입도를 개선하고 소결광 회수율을 증가시켜 생산성을 향상시킬 수 있는 소결광 제조장치 및 제조방법에 관한 것이다.The present invention relates to a sintered ore manufacturing apparatus and a manufacturing method, and more particularly, by minimizing the half-light generation of the upper layer of the sintered trolley by irradiating microwaves on the top of the sintered bogie, to improve the particle size of the sintered ore and increase the sintered ore recovery productivity It relates to a sintered ore manufacturing apparatus and a manufacturing method that can be improved.

일반적으로 고로에서 원료로 사용되는 소결광은 주 원료의 약 80%를 차지하며, 소결광은 소결장치에 배합원료와 상부광을 장입하고 고온으로 소성시켜 제조한다.Generally, the sintered ore used as a raw material in the blast furnace accounts for about 80% of the main raw material, the sintered ore is prepared by charging the raw material and the top light in the sintering apparatus and firing at high temperature.

도 1은 일반적인 하방 흡입식(Dwight Loyd) 소결장치를 이용한 소결공정을 보여주는 개략도이고, 도 2는 종래 일반적인 하방 흡입식 소결장치의 소결대차 위치별 회수율을 보여주는 도면이다.FIG. 1 is a schematic view showing a sintering process using a general down suction sintering apparatus, and FIG. 2 is a view showing a recovery rate by sintering cart position of a conventional general down suction sintering apparatus.

도 1 및 도 2에 도시된 바와 같이, 하방 흡입식 소결장치를 이용한 소결공정은 분 철광석과 부원료, 코크스(Coke)를 광석 빈(ORE BIN; 10)에 저장한 후, 일정량을 절출하여 드럼 믹서(DRUM MIXER; 11)에서 수분을 첨가 및 혼합하여 써지 호퍼(SURGE HOPPER; 12)에 저장한다.As shown in Figure 1 and 2, the sintering process using a downward suction sintering apparatus is stored in the ore bin (ORE BIN) 10, and the iron ore, secondary raw materials, coke (Coke), and then cut out a certain amount of the drum mixer ( Water is added and mixed in the DRUM MIXER; 11) and stored in the SURGE HOPPER 12.

이후, 상부광 호퍼(14)를 통하여 상부광이 장입된 소결대차(15)가 이동되면 상부광 호퍼(14) 후단에서 드럼피더(13)가 써지 호퍼(12)를 통해 배출되는 원료에 수분을 첨가하여 배합원료를 마련되며, 상기와 같이 마련된 배합원료는 분급 현상을 유도하기 위한 경사 플레이트(Deflector Plate, 16)을 따라 소결대차(15) 상부에 장입된다.Subsequently, when the sintered trolley 15 into which the upper light is charged is moved through the upper light hopper 14, the drum feeder 13 absorbs moisture to the raw material discharged through the surge hopper 12 at the rear end of the upper light hopper 14. A compounding raw material is prepared by adding, and the compounding raw material prepared as described above is charged to the upper portion of the sintering cart 15 along the inclined plate (Deflector Plate) 16 to induce a classification phenomenon.

이와 같이, 배합원료 장입이 완료된 소결대차(15)는 점화로(17)에서 고온(약 1200℃)의 불꽃으로 배합원료 표층부를 착화시키고, 메인 블로워(18)를 작동시켜 흡입력을 발생시킨다.Thus, the sintered trolley | bogie 15 in which the compounding material loading was completed ignites the compounding material superficial layer part with the flame | hot flame of high temperature (about 1200 degreeC) in the ignition furnace 17, and operates the main blower 18, and generates a suction force.

흡입력은 챔버(19)를 통하여 윈드박스(20)로 전달되는 것으로, 윈드박스(20)로 전달된 흡입력은 소결대차(15)의 하부를 강하게 흡입하여 대기 중의 공기가 소결대차(15)에 장입된 배합원료의 상부에서 하부로 통과하면서 고온소성에 의해 분 철광석을 괴성화시켜 소결광을 제조한다.The suction force is transmitted to the windbox 20 through the chamber 19, and the suction force transmitted to the windbox 20 strongly sucks the lower portion of the sintering cart 15 so that air in the air is charged into the sintering cart 15. Passing from the upper part to the lower part of the blended raw material, the iron ore is agglomerated by high temperature firing to produce a sintered ore.

한편, 소결광 제조공정은 소결광의 품질은 우수하고 연료소비를 최소화하면서도 회수율 및 생산성을 극대화하는 방법을 채택하게 되는데, 상기와 같은 하방 흡입식 소결장치는 소결대차(15)의 하방에서 지속적으로 연소가스를 흡입함에 따라 차가운 공기가 소결대차(15)의 전체 깊이에 대하여 배합원료의 평면으로부터 1/3 깊이까지 형성되는 상층부를 빠르게 냉각시키기 때문에 제조된 소결광의 약 1/3을 차지하는 소결대차(15) 상층부 소결광이 소결에 필요한 열을 충분히 공급받지 못함에 따라 입자의 직경이 5㎜ 미만인 반광이 다량 발생되어 소결광의 회수율이 저하되는 문제점을 가지고 있었다.Meanwhile, the sintered ore manufacturing process adopts a method of maximizing the quality of the sintered ore and maximizing recovery and productivity while minimizing fuel consumption. The downward suction type sintering apparatus continuously burns the combustion gas under the sintering cart 15. As the air is sucked, the cool air rapidly cools the upper layer formed from the plane of the blended material to one third depth with respect to the entire depth of the sintered bogie 15, so that the upper tier of the sintered bogie 15 occupies about one third of the manufactured sintered ore. As the sintered ore does not receive enough heat for sintering, a large amount of semi-glossy particles having a diameter of less than 5 mm is generated, which has a problem in that the recovery rate of the sintered ore is lowered.

종래 이러한 문제점을 해결하기 위해 마이크로웨이브를 이용한 기술에 대해서는 "소결광의 제조방법(한국공개특허 제10-1995-0018555호)", "소결광 제조 방법(일본공개특허 제1996-014763호)", "소결광 배합원료 수분 제거장치 및 방법(한국공개특허 제10-2010-0026457호)" 등이 있다.In order to solve such problems in the related art, for the technique using microwave, "a method of manufacturing sintered ore (Korean Patent Publication No. 10-1995-0018555)", "a method of manufacturing a sintered ore (Japanese Patent Publication No. 1996-014763)", " Sintered ore blending material moisture removal device and method (Korea Patent Publication No. 10-2010-0026457).

그러나, 선행문헌들은 모두 소결대차에 원료를 장입한 후 표층부를 점화시키기 전에 마이크로웨이브를 이용하여 원료를 가열하여 수분을 건조시켜 의사입자의 강도를 증진시키거나, 예열시킴으로써 소결시 에너지 소모를 감소시키는 방법으로 소결대차의 상층부가 빠르게 냉각됨에 따라 상층부의 소결광 입자의 크기가 감소된 반광이 다량 생성되어 소결광 회수율이 저하되는 문제점을 해결하지 못하였다.However, all of the prior literatures use a microwave to heat the raw material to dry the moisture before charging the surface layer after loading the raw material into the sintering bogie to enhance the strength of the pseudoparticles, or to reduce the energy consumption during sintering by preheating. As the upper portion of the sintered trolley is rapidly cooled by the method, a large amount of semi-reflected light having a reduced size of the sintered ore particles in the upper portion is generated, and thus, the problem that the recovery rate of the sintered ore is reduced is not solved.

본 발명은 상기와 같은 문제점을 해결하기 위해 안출된 것으로, 소결대차에 장입되어 점화로를 통과하면서 표층부가 착화된 배합원료의 평면에 마이크로웨이브를 조사하여 소결대차 상층부에 부족한 열원을 공급하여 미소결로 인한 반광 발생을 최소화함으로써, 소결광의 품질 및 회수율을 향상시킬 수 있는 소결광 제조장치 및 제조방법을 제공한다.The present invention has been made to solve the above problems, it is charged into the sinter bogie and passed through the ignition furnace while irradiating microwaves to the plane of the compounding material complexed with the surface layer is supplied by supplying a heat source insufficient in the upper sinter bogie sintered condensation Provided is a sintered ore manufacturing apparatus and a manufacturing method that can improve the quality and recovery of the sintered ore by minimizing the generation of semi-glow.

본 발명의 일 실시예에 따른 소결광 제조장치는 무한궤도상으로 다수의 소결대차를 연결하여 소결공정을 진행하는 소결광 제조장치에 있어서, 상기 소결대차에 상부광 및 배합원료를 각각 공급하는 상부광 호퍼와 써지 호퍼를 포함하는 원료 공급부; 상기 소결대차의 진행방향으로 상기 원료 공급부 후단에 배치되어 상기 소결대차에 장입된 배합원료의 표층부를 착화시키는 점화로; 및 상기 점화로의 후단에 배치되어 상기 소결대차에 장입된 배합원료의 표층부에 마이크로웨이브를 조사하는 마이크로웨이브 가열로;를 포함한다.In the sintered ore manufacturing apparatus according to an embodiment of the present invention in the sintered ore manufacturing apparatus that proceeds the sintering process by connecting a plurality of sintered trolley in an endless track, an upper light hopper for supplying the upper light and the blended raw materials to the sintered trolley respectively Raw material supply including a surge hopper; An ignition furnace disposed at a rear end of the raw material supply part in the advancing direction of the sintered bogie to complex the surface layer portion of the blended raw material charged into the sintered bogie; And a microwave heating furnace disposed at a rear end of the ignition furnace and irradiating microwaves to the surface layer portion of the blended raw material charged into the sintering cart.

상기 마이크로웨이브 가열로는, 주파수가 800㎒ ~ 3㎓인 마이크로웨이브를 조사하는 것을 특징으로 할 수 있다.The microwave heating furnace may be characterized in that for irradiating the microwave with a frequency of 800MHz ~ 3kHz.

상기 마이크로웨이브 가열로는, 상기 소결대차가 통과되면서 그 내부에 수용된 배합원료의 표면에 마이크로웨이브를 조사할 수 있도록, 상기 소결대차의 진행방향으로 양단이 개구된 터널형상으로 형성된 것이 바람직하다.The microwave heating furnace is preferably formed in a tunnel shape in which both ends are opened in the advancing direction of the sintering bogie so that the microwaves can be irradiated onto the surface of the blended material accommodated therein while the sintering bogie passes.

본 발명의 일 실시예에 따른 소결광 제조방법은 하방 흡입식(Dwight Loyd) 소결장치를 이용한 소결광 제조방법에 있어서, 무한궤도상에서 이동되는 소결대차에 상부광 및 배합원료를 공급하는 원료공급 단계; 상기 소결대차에 장입된 배합원료의 표층부를 착화시키는 점화 단계; 및 표층부가 점화된 배합원료의 평면에 마이크로웨이브를 조사하여 배합원료의 상층부를 가열시키는 가열 단계;를 포함한다.In the sintered ore manufacturing method according to an embodiment of the present invention, in the sintered ore manufacturing method using a downward suction sintering apparatus, the raw material supply step of supplying the top light and the blended raw material to the sintered trolley moving on the endless track; An ignition step of complexing the surface layer portion of the blended raw material charged into the sintering cart; And a heating step of heating the upper layer portion of the blended raw material by irradiating microwaves to the plane of the blended raw material on which the surface layer is ignited.

상기 가열 단계는, 주파수가 800㎒ ~ 3㎓인 마이크로웨이브를 조사하는 것이 바람직하다.In the heating step, the microwave is preferably irradiated with a frequency of 800MHz ~ 3kHz.

상기 가열 단계는, 마이크로웨이브를 10초 ~ 3분간 조사하는 것을 특징으로 할 수 있다.The heating step may be characterized in that for irradiating the microwave for 10 seconds to 3 minutes.

본 발명의 실시예에 따르면, 마이크로웨이브 가열로를 이용하여 연소가스의 흐름에 영향을 주지 않으면서 소결대차에 장입된 배합원료의 상층부에 필요한 열에너지를 공급함으로써, 소결광 품질 및 회수율을 향상시킬 수 있는 효과가 있다.According to an embodiment of the present invention, by supplying the heat energy required in the upper layer portion of the blended raw material charged in the sinter bogie without affecting the flow of the combustion gas using the microwave heating furnace, the sintered ore quality and recovery rate can be improved It works.

도 1은 일반적인 하방 흡입식(Dwight Loyd) 소결장치를 이용한 소결공정을 보여주는 개략도이고,1 is a schematic view showing a sintering process using a conventional double-low suction sintering apparatus,

도 2는 종래 일반적인 하방 흡입식 소결장치의 소결대차 위치별 회수율을 보여주는 도면이며,Figure 2 is a view showing the recovery rate for each position of the sintered cart of the conventional general down suction sintering apparatus

도 3는 본 발명의 일 실시예에 따른, 소결광 제조장치를 보여주는 개략도이고,3 is a schematic view showing a sintered ore manufacturing apparatus according to an embodiment of the present invention,

도 4는 본 발명의 일 실시예에 따른, 마이크로웨이브 가열로를 설명하기 위한 도면이며,4 is a view for explaining a microwave heating furnace, according to an embodiment of the present invention,

도 5는 본 발명의 일 실시예에 따른, 소결광 제조방법을 보여주는 순서도이고,5 is a flowchart showing a sintered ore manufacturing method according to an embodiment of the present invention,

도 6은 종래 일반적인 하방 흡입식 소결장치와 본 발명의 일 실시예에 따른 소결광 제조장치의 온도분포를 보여주는 도면이다.6 is a view showing a temperature distribution of a conventional general down suction sintering apparatus and a sintered ore manufacturing apparatus according to an embodiment of the present invention.

이하 첨부된 도면들을 참조하여 본 발명의 바람직한 실시예를 상세하게 설명하지만, 본 발명이 실시예에 의해 제한되거나 한정되는 것은 아니다. 참고로, 본 설명에서 동일한 번호는 실질적으로 동일한 요소를 지칭하며, 이러한 규칙 하에서 다른 도면에 기재된 내용을 인용하여 설명할 수 있고, 당업자에게 자명하다고 판단되거나 반복되는 내용은 생략될 수 있다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings, but the present invention is not limited or limited by the embodiments. For reference, in the present description, the same numbers refer to substantially the same elements, and may be described by referring to the contents described in the other drawings under these rules, and the contents determined to be obvious to those skilled in the art or repeated may be omitted.

도 3는 본 발명의 일 실시예에 따른, 소결광 제조장치를 보여주는 개략도이고, 도 4는 본 발명의 일 실시예에 따른, 마이크로웨이브 가열로를 설명하기 위한 도면이다.3 is a schematic view showing a sintered ore manufacturing apparatus according to an embodiment of the present invention, Figure 4 is a view for explaining a microwave heating furnace, according to an embodiment of the present invention.

도 3 및 도 4에 도시된 바와 같이, 본 발명의 일 실시예에 따른 소결광 제조장치는 무한궤도상으로 복수 개가 연결된 소결대차(15) 내부로 원료를 공급하는 원료 공급부와 각각의 소결대차(15)에 장입된 원료의 표층부를 착화시키는 점화로(17) 및 소결대차(15)에 장입된 원료의 표면에 마이크로웨이브를 조사하는 마이크로웨이브 가열로(30)를 포함한다.As shown in Figure 3 and 4, the sintered ore manufacturing apparatus according to an embodiment of the present invention is a raw material supply unit for supplying the raw material into the sintered trolley 15 is connected to a plurality of tracks in the orbit and each of the sintered trolley 15 And an ignition furnace 17 for igniting the surface layer portion of the raw material charged in the) and a microwave heating furnace 30 for irradiating the microwaves to the surface of the raw material charged in the sintering cart 15.

각각의 소결대차(15) 내부로 공급되는 원료는 상부광과 상부광의 상부에 적층되는 배합원료로 구성되며, 원료 공급부는 무한궤도로 형성된 주행레일을 따라 소결대차(15)가 이동되는 경로 일측 상부에 소결대차(15)의 폭방향으로 설치된 상부광 호퍼(14)와 상부광 호퍼(14) 후단에 배치된 써지 호퍼(12)로 구성된다.The raw material supplied into each of the sintered trolleys 15 is composed of a compound raw material stacked on top of the upper light and the upper light, and the raw material supply part is an upper portion of one side of the path along which the sintered trolley 15 moves along the running rail formed in an endless track. The upper light hopper 14 provided in the width direction of the sintering trolley | bogie 15 and the surge hopper 12 arrange | positioned at the rear end of the upper light hopper 14 are comprised.

상부광 호퍼(14)는 소결대차(15) 내부에 10 ~ 15mm 입도 범위를 갖는 상부광을 약 50mm 두께로 소결대차(15)에 장입시키며, 후단에 설치된 써지 호퍼(12)는 일정량의 수분이 첨가된 배합원료를 소결대차(15)에 공급한다.The upper light hopper 14 charges the upper light having a particle size range of 10 to 15 mm in the sintering cart 15 to the sintering cart 15 with a thickness of about 50 mm, and the surge hopper 12 installed at the rear end has a predetermined amount of moisture. The added blending raw material is supplied to the sintering cart 15.

이때, 써지 호퍼(12)는 하부에 설치된 드럼피더(13)가 회전되면 써지 호퍼(12) 내부에 수용된 배합원료가 소결대차(15) 내부로 불출되며 드럼피더(13)의 회전속도에 따라 배합원료의 불출량이 조절되며, 그 하부에는 불출되는 배합원료의 분급 현상을 유도하기 위한 경사 플레이트(Deflector Plate, 16)가 설치되어 써지 호퍼(12)에서 불출되는 배합원료가 경사 플레이트(16)를 따라 소결대차(15) 내부로 장입된다.At this time, the surge hopper 12 is rotated the drum feeder 13 installed in the lower portion of the blended raw material contained in the surge hopper 12 is discharged into the sintering cart 15 and blended according to the rotational speed of the drum feeder 13 The discharge amount of the raw material is controlled, and a lower plate (Deflector Plate, 16) is installed at the lower part to induce the classification phenomenon of the mixed raw material is discharged from the surge hopper 12 along the inclined plate (16) It is charged into the sinter cart 15.

점화로(17)는 소결대차(15)에 장입된 배합원료의 표층부를 착화시킬 수 있도록 그 상부에 복수의 버너가 소결대차(15)의 폭방향으로 일정간격 이격되어 설치되어 연속하여 그 하부를 통과되는 복수의 소결대차(15)에 장입된 배합원료의 표층부를 차례로 점화시킨다.The ignition furnace 17 is provided with a plurality of burners spaced apart at regular intervals in the width direction of the sintering bogie 15 so as to ignite the surface layer portion of the blended material charged into the sinter bogie 15, and continuously The surface layer portions of the blended raw materials charged into the sintered trolleys 15 to be passed are sequentially fired.

마이크로웨이브 가열로(30)는 복수의 소결대차(15)가 연속적으로 통과될 수 있도록 그 저면 및 양단이 개방된 터널 형상으로 형성되며 그 하부로 통과되는 소결대차(15)에 장입된 배합원료의 표층부에 마이크로웨이브를 조사할 수 있도록 그 천정에 마이크로웨이브 발진수단이 설치된다.The microwave heating furnace 30 is formed in a tunnel shape in which its bottom and both ends are open so that a plurality of sintering trolleys 15 can be continuously passed, and the raw material charged in the sintering trolley 15 passed below. Microwave oscillation means is installed on the ceiling to irradiate the microwaves to the surface layer.

일반적으로 마이크로웨이브는 전자기 에너지 중 낮은 주파수를 갖는 에너지의 한 형태로 800 ~ 300,000㎒의 주파수 범위를 갖고, 전자기장 범위 내에서 분자의 회전만을 야기시키고 분자 구조에는 영향을 미치지 않는다.In general, microwaves are a form of energy with a low frequency of electromagnetic energy and have a frequency range of 800 to 300,000 MHz, causing only the rotation of molecules within the electromagnetic field range and do not affect the molecular structure.

보다 구체적으로 마이크로웨이브는 전기장과 자기장으로 구성되는데 그 중 전기장이 물질을 가열시키는 역할을 하며, 광속으로 전파되고 광자 에너지(0.037㎉/mole)는 분자결합을 끊을 수 있는 에너지(80 ~ 120㎉/mole)에 비하여 낮기 때문에 물질을 가열시킬 뿐 분자 구조에는 영향을 주지 않는다.More specifically, the microwave is composed of an electric field and a magnetic field, of which the electric field serves to heat the material, propagates at the speed of light and the photon energy (0.037㎉ / mole) is the energy (80 ~ 120㎉ / It is lower than mole, so it only heats the material and does not affect the molecular structure.

이에, 본 발명의 일 실시예에 따른 마이크로웨이브 가열로(30)는 전도열을 이용하여 에너지 전달속도가 느리고 물질의 열평형까지 장시간이 소요되어 비효율적인 종래 일반적인 가열방식을 대체하여, 내외부 온도를 균일하고 빠르게 가열시킬 수 있는 마이크로웨이브를 조사한다.Thus, the microwave heating furnace 30 according to the embodiment of the present invention replaces the conventional inefficient conventional heating method by using energy conduction heat, which is slow in energy transfer rate and takes a long time until thermal equilibrium of materials, thereby uniformizing internal and external temperatures. Investigate microwaves that can be heated quickly.

이때, 사용되는 마이크로웨이브의 주파수는 800㎒ ~ 3㎓인 것이 바람직한데, 그 이유는 마이크로웨이브의 주파수가 3㎓를 초과하는 경우 비용이 상승되며 소결온도를 과도하게 상승시켜 생산되는 소결광의 품질을 저하시키는 문제점이 있으며, 800㎒ 미만인 경우 배합원료의 내부로 침투되는 깊이가 늘어나면서 에너지 밀도가 낮아져 입도가 5㎜ 미만인 반광이 발생되는 배합원료의 상층부를 충분히 가열하지 못하며 가열에 장시간이 소요되기 때문이다.At this time, the frequency of the microwave used is preferably 800MHz ~ 3kHz, the reason is that when the frequency of the microwave exceeds 3kHz the cost is increased and the sintering temperature is excessively raised to improve the quality of the sintered ore produced If it is less than 800MHz, the depth penetrated into the blending material is increased, and the energy density decreases, so that the upper part of the blending material having semi-gloss with a particle size of less than 5 mm is not sufficiently heated, and heating takes a long time. to be.

구분division 화학조성Chemical composition 온도(℃)Temperature (℃) 적철석(Hematite)Hematite Fe2O3 Fe 2 O 3 1,0001,000 자철석(Magnetite)Magnetite Fe3O4 Fe 3 O 4 700700 갈철광(Limonite)Limonite mFe2·nH2OmFe 2 nH 2 O 150150 석회암(Limestone)Limestone CaCO3 CaCO 3 200200 실리카(Silica)Silica SiO2 SiO 2 140140

표 1은 일반적으로 소결대차에 장입되는 배합원료의 주요 성분에 대하여 2kW용량, 2.4㎓의 마이크로웨이브를 1분간 조사한 후 그 온도를 측정하여 나타낸 표이다.Table 1 is a table showing the temperature measured after 1 minute irradiation of microwave of 2 kW capacity, 2.4 kW for 1 minute with respect to the main components of the blended raw materials charged in the sintering cart.

표 1에서 알 수 있듯, 마이크로웨이브를 사용하여 배합원료 가열시 단시간에 배합원료의 주요 성분을 가열시킬 수 있어, 마이크로웨이브를 소결대차(15)에 장입된 배합원료의 표면에 조사함으로써, 소결대차(15)의 전체 깊이에 대하여 배합원료의 평면으로부터 1/3 깊이까지 형성되는 상층부를 가열시켜 소결대차(15)의 하방에서 지속적으로 연소가스를 흡입함에 따라 차가운 공기에 의하여 냉각되는 온도를 보상하여 상층부의 반광 생성을 최소화할 수 있는 효과가 있다.As can be seen from Table 1, it is possible to heat the main components of the blended raw material in a short time when heating the blended raw material using the microwave, by irradiating the surface of the blended raw material charged in the sintered cart 15, microwaves By heating the upper part formed from the plane of the blended material to 1/3 depth for the total depth of (15) to compensate for the temperature cooled by the cold air as the continuous intake of the combustion gas under the sinter truck 15 There is an effect that can minimize the semi-light generation of the upper layer.

한편, 본 발명의 일 실시예에 따른 마이크로웨이브 가열로(30)는 각각의 소결대차(15)가 1 ~ 2분 동안 통과될 수 있는 길이로 형성되는 것이 바람직하다.On the other hand, the microwave heating furnace 30 according to an embodiment of the present invention is preferably formed to a length that each sintering cart 15 can pass for 1 to 2 minutes.

왜냐하면, 그 이유는 마이크로웨이브의 길이가 그 하부를 통과하는 소결대차(15)의 통과시간이 1분 미만으로 형성된 경우 소결대차(15)에 장입된 배합원료의 상층부를 충분히 가열하지 못하여 반광 생성량이 증가되며, 2분 이상 가열되도록 형성된 경우 제조원가 상승에 비하여 반광 발생 감소량이 미미하여 마이크로웨이브 가열로(30)의 길이는 소결대차(15)가 1 ~ 2분의 통과시간을 갖도록 형성되는 것이 바람직하다.This is because if the passage time of the sintered trolley 15 through which the length of the microwave passes below is less than 1 minute, the amount of semi-glossy cannot be sufficiently heated due to insufficient heating of the upper layer of the blended raw material charged into the sintered trolley 15. When it is formed to be heated for 2 minutes or more, the decrease in the amount of semi-light generation is insignificant compared to the increase in manufacturing cost, so that the length of the microwave heating furnace 30 is preferably formed such that the sintering cart 15 has a passage time of 1 to 2 minutes.

마이크로웨이브(2kW, 2.4㎓) 조사시간Microwave (2kW, 2.4㎓) irradiation time 반광 발생비Half light generation rate -- 33.2%33.2% 1분1 min 25.8%25.8% 2분 2 minutes 19.8%19.8%

표 2는 마이크로웨이브 조사 조건에 따른 반광 발생비를 나타낸 표로, 본 발명에서는 120㎏ 배합원료의 표면을 화염을 이용하여 착화시킨 후 마이크로웨이브(2kW, 2.4㎓)를 조사하여 상층부를 가열시킨 다음, 하방에서 1,600㎜Hq의 압력으로 연소가스를 흡입하고, 연소가 완전히 종료된 후 시료를 50㎜ 이하로 파쇄하고 드럼강도를 측정한 후 5㎜ 미만의 반광 발생량을 측정하였다.Table 2 is a table showing the rate of semi-glow generation according to the microwave irradiation conditions, in the present invention, after the surface of the 120kg blended material is ignited using a flame and irradiated with microwaves (2kW, 2.4㎓) to heat the upper layer, The combustion gas was aspirated at a pressure of 1,600 mmHq from below, and after combustion was completed, the sample was crushed to 50 mm or less, and the drum strength was measured.

표 2에서 알 수 있듯, 마이크로웨이브를 조사하지 않은 종래 하방 흡입식 소결장치에 비하여 마이크로웨이브를 1분간 조사한 경우 반광 발생량이 약 7.4% 감소되고, 2분간 조사한 경우 반광 발생량이 13.4% 감소되어 소결시 발생되는 반광 발생량을 현저히 감소시킬 수 있음을 알 수 있다.As can be seen from Table 2, when irradiating microwaves for 1 minute, the amount of semi-glow is reduced by about 7.4%, and when irradiated for 2 minutes, the amount of semi-glow is reduced by 13.4%, compared to the conventional down suction sintering apparatus that does not irradiate microwaves. It can be seen that the amount of semi-light generated can be significantly reduced.

마이크로웨이브(5kW, 2.4㎓) 조사시간Microwave (5kW, 2.4㎓) irradiation time 반광 발생비Half light generation rate -- 33.2%33.2% 10초10 sec 30.7%30.7% 30초30 seconds 24.4%24.4% 60초60 seconds 18.5%18.5%

표 3은 마이크로웨이브 파워를 5kW로 증가시켰을 때, 조사시간에 따른 반광 발생비를 나타낸 표로, 표 2의 2kW에 비하여 짧은 시간에 반광 발생비가 급격히 감소하는 것을 알 수 있다. Table 3 is a table showing the half light generation ratio according to the irradiation time when the microwave power is increased to 5 kW, it can be seen that the half light generation ratio decreases rapidly in a short time compared to 2 kW of Table 2.

따라서 표 2와 표 3의 측정 결과로부터 마이크로웨이브 파워가 증가함에 따라 조사시간은 현저히 감소될 수 있음을 알 수 있다.Therefore, it can be seen from the measurement results of Tables 2 and 3 that the irradiation time can be significantly reduced as the microwave power increases.

상기와 같이 구성되는 본 발명의 일 실시예에 따른 소결광 제조장치를 이용한 소결광 제조방법을 도면을 참조하여 설명한다.A sintered ore manufacturing method using a sintered ore manufacturing apparatus according to an embodiment of the present invention configured as described above will be described with reference to the drawings.

도 5는 본 발명의 일 실시예에 따른, 소결광 제조방법을 보여주는 순서도이다.5 is a flowchart showing a sintered ore manufacturing method according to an embodiment of the present invention.

도 5에 도시된 바와 같이, 본 발명의 일 실시예에 따른 소결광 제조방법은 원료공급 단계와 배합원료의 표면을 착화시키는 점화 단계 및 배합원료의 표층부에 마이크로웨이브를 조사하는 가열 단계를 포함한다.As shown in FIG. 5, the sintered ore manufacturing method according to an embodiment of the present invention includes a raw material supplying step, an ignition step of complexing the surface of the blended raw material, and a heating step of irradiating microwaves to the surface layer of the blended raw material.

원료공급 단계는 무한궤도상에서 이동되는 소결대차(15)의 내부에 상부광 호퍼(14) 및 써지 호퍼(12)를 이용하여 각각 상부광 및 배합원료를 순차적으로 공급시킨다.In the raw material supplying step, the upper light hopper 14 and the surge hopper 12 are sequentially supplied to the inside of the sintered trolley 15 which is moved on the track.

소결대차(15) 내부로 원료 공급이 완료되면, 원료가 장입된 소결대차(15)가 점화로(17)를 통과하면서 그 내부에 수용된 배합원료의 표층부를 점화시킨다.When the raw material supply is completed into the sintered trolley 15, the sintered trolley 15 loaded with the raw materials passes through the ignition furnace 17 to ignite the surface layer portion of the blended raw material contained therein.

도 6은 종래 일반적인 하방 흡입식 소결장치의 온도분포(a)와 본 발명의 일 실시예에 따른 소결광 제조장치의 온도분포(b)를 보여주는 도면이다.6 is a view showing the temperature distribution (a) of the conventional general down suction sintering apparatus and the temperature distribution (b) of the sintered ore manufacturing apparatus according to an embodiment of the present invention.

도 6에 도시된 바와 같이, 본 발명의 일 실시예에 따른 소결광 제조방법은 표층부 점화가 완료되면, 가열 단계에서 소결대차(15)에 장입된 배합원료의 표층부에 800㎒ ~ 3㎓인 마이크로웨이브를 1 ~ 2분간 조사하여 배합원료의 상층부를 가열시킨다.As shown in Figure 6, the sintered ore manufacturing method according to an embodiment of the present invention, when the surface layer ignition is completed, the microwave is 800MHz ~ 3 kHz at the surface layer portion of the blended raw material charged in the sintered cart 15 in the heating step Irradiate for 1 to 2 minutes to heat the upper layer of the blended raw material.

이에, 이후 하방에서 지속적으로 연소가스를 흡입함에 따라 냉각되는 배합원료의 상층부의 냉각온도를 보상해줄 수 있어 소결대차(15)에 장입된 배합원료의 상층부에 필요한 열에너지를 공급함으로써, 소결광 품질 및 회수율을 향상시킬 수 있는 효과가 있다.Therefore, the cooling temperature can be compensated by continuously inhaling the combustion gas from below to compensate for the cooling temperature of the upper part of the blended raw material, thereby supplying the heat energy necessary for the upper part of the blended raw material charged in the sintered bogie 15, thereby improving the sintered ore quality and recovery rate. There is an effect to improve.

또한, 마이크로웨이브를 이용하여 가열시킴으로써 연소가스의 흐름에 영향을 주지 않아 생산되는 소결광의 품질을 일정하게 하고, 생산성을 향상시킬 수 있는 효과가 있다.In addition, heating by using a microwave does not affect the flow of the combustion gas has the effect of making the quality of the sintered ore produced uniformly, improving the productivity.

상기와 같이 배합원료의 상층부 가열이 완료되면 메인 블로워(18)를 작동시켜 소결대차(15)의 하방으로 흡입력을 발생시켜 연소가스를 흡입하면서 소결광을 제조한다.When the heating of the upper portion of the blended raw material is completed as described above, the main blower 18 is operated to generate a suction force under the sinter truck 15 to produce a sintered ore while sucking the combustion gas.

상술한 바와 같이, 본 발명의 바람직한 실시예를 참조하여 설명하였지만 해당 기술분야의 숙련된 당업자라면 하기의 청구범위에 기재된 본 발명의 사상 및 영역으로부터 벗어나지 않는 범위 내에서 본 발명을 다양하게 수정 및 변경시킬 수 있음을 이해할 수 있을 것이다.As described above, although described with reference to the preferred embodiment of the present invention, those skilled in the art various modifications and variations of the present invention without departing from the spirit and scope of the invention described in the claims below I can understand that you can.

[부호의 설명][Description of the code]

10: 광석 빈 11: 드럼 믹서10: ore hollow 11: drum mixer

12: 써지 호퍼 13: 드럼피더12: Surge Hopper 13: Drum Feeder

14: 상부광 호퍼 15: 소결대차14: upper light hopper 15: sintered trolley

16: 경사 플레이트 17: 점화로16: tilt plate 17: ignition furnace

18: 메인 블로워 19: 챔버18: main blower 19: chamber

20: 윈드박스 30: 마이크로웨이브 가열로20: windbox 30: microwave furnace

Claims (6)

무한궤도상으로 다수의 소결대차를 연결하여 소결공정을 진행하는 소결광 제조장치에 있어서,In the sintered ore manufacturing apparatus that connects a plurality of sintered trolleys on the track, 상기 소결대차에 상부광 및 배합원료를 각각 공급하는 상부광 호퍼와 써지 호퍼를 포함하는 원료 공급부;A raw material supply unit including an upper light hopper and a surge hopper for respectively supplying upper light and a blended raw material to the sintered cart; 상기 소결대차의 진행방향으로 상기 원료 공급부 후단에 배치되어 상기 소결대차에 장입된 배합원료의 표층부를 착화시키는 점화로; 및An ignition furnace disposed at a rear end of the raw material supply part in the advancing direction of the sintered bogie to complex the surface layer portion of the blended raw material charged into the sintered bogie; And 상기 점화로의 후단에 배치되어 상기 소결대차에 장입된 배합원료의 표층부에 마이크로웨이브를 조사하는 마이크로웨이브 가열로;를 포함하는, 소결광 제조장치.And a microwave heating furnace disposed at a rear end of the ignition furnace and irradiating microwaves to the surface layer of the blended raw material charged into the sintering cart. 청구항 1에 있어서,The method according to claim 1, 상기 마이크로웨이브 가열로는,The microwave heating furnace, 주파수가 800㎒ ~ 3㎓인 마이크로웨이브를 조사하는 것을 특징으로 하는, 소결광 제조장치.Sintered ore manufacturing apparatus, characterized in that for irradiating microwaves with a frequency of 800MHz ~ 3kHz. 청구항 1에 있어서,The method according to claim 1, 상기 마이크로웨이브 가열로는,The microwave heating furnace, 상기 소결대차가 통과되면서 그 내부에 수용된 배합원료의 표면에 마이크로웨이브를 조사할 수 있도록, 상기 소결대차의 진행방향으로 양단이 개구된 터널형상으로 형성된 것을 특징으로 하는, 소결광 제조장치.Sintered ore manufacturing apparatus, characterized in that formed in a tunnel shape in which both ends are opened in the advancing direction of the sintered bogie so that the microwaves can be irradiated to the surface of the blended material contained therein while the sintered bogie passes. 하방 흡입식(Dwight Loyd) 소결장치를 이용한 소결광 제조방법에 있어서,In the method of manufacturing a sintered ore using a downward sintering apparatus, 무한궤도상에서 이동되는 소결대차에 상부광 및 배합원료를 공급하는 원료공급 단계;A raw material supply step of supplying the upper light and the blended raw materials to the sintered trolley moving on the endless track; 상기 소결대차에 장입된 배합원료의 표층부를 착화시키는 점화 단계; 및An ignition step of complexing the surface layer portion of the blended raw material charged into the sintering cart; And 표층부가 점화된 배합원료의 평면에 마이크로웨이브를 조사하여 배합원료의 상층부를 가열시키는 가열 단계;를 포함하는, 소결광 제조방법.And a heating step of heating the upper layer of the blended material by irradiating microwaves to the plane of the blended material ignited at the surface layer. 청구항 4에 있어서,The method according to claim 4, 상기 가열 단계는,The heating step, 주파수가 800㎒ ~ 3㎓인 마이크로웨이브를 조사하는 것을 특징으로 하는, 소결광 제조방법.A method of producing a sintered ore, characterized by irradiating a microwave having a frequency of 800 MHz to 3 kHz. 청구항 5에 있어서,The method according to claim 5, 상기 가열 단계는,The heating step, 마이크로웨이브를 10초 ~ 3분간 조사하는 것을 특징으로 하는, 소결광 제조방법.Sintered ore manufacturing method characterized in that for irradiating the microwave for 10 seconds to 3 minutes.
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