KR100411271B1 - Method for mixing lime stone dust into raw material of sintering - Google Patents

Method for mixing lime stone dust into raw material of sintering Download PDF

Info

Publication number
KR100411271B1
KR100411271B1 KR10-1999-0049888A KR19990049888A KR100411271B1 KR 100411271 B1 KR100411271 B1 KR 100411271B1 KR 19990049888 A KR19990049888 A KR 19990049888A KR 100411271 B1 KR100411271 B1 KR 100411271B1
Authority
KR
South Korea
Prior art keywords
raw material
dust
limestone
groove
limestone dust
Prior art date
Application number
KR10-1999-0049888A
Other languages
Korean (ko)
Other versions
KR20010046207A (en
Inventor
김병호
홍준
윤종옥
Original Assignee
주식회사 포스코
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.)
Filing date
Publication date
Application filed by 주식회사 포스코 filed Critical 주식회사 포스코
Priority to KR10-1999-0049888A priority Critical patent/KR100411271B1/en
Publication of KR20010046207A publication Critical patent/KR20010046207A/en
Application granted granted Critical
Publication of KR100411271B1 publication Critical patent/KR100411271B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/005Preliminary treatment of scrap

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

본 발명은 석회소성공장에서 생산하는 생석회 제조시 집진기에서 포집되는 석회석 더스트를 소결원료로 사용하는 방법에 관한 것으로서, 그 목적은 비산먼지로 인한 환경오염을 줄이면서 배합원료의 성분편차를 방지할 수 있는 소결원료의 균일혼합방법을 제공함에 있다.The present invention relates to a method of using limestone dust collected in a dust collector as a sintering raw material in the production of quicklime produced in a lime firing plant, the purpose of which can prevent the component deviation of the blended raw materials while reducing environmental pollution due to scattering dust. It is to provide a uniform mixing method of sintered raw materials.

상기 목적을 달성하기 위한 본 발명은, 원료저장조의 배합원료를 콘베어벨트로 이송하여 혼합기에 입조한 후 혼합하는 것을 포함한 소결광의 제조방법에 있어서, 상기 콘베어벨트상의 배합원료에 일정크기의 홈을 형성하고, 이 홈내로 석회석더스트를 투입한 직후에 홈내의 석회석더스트를 배합원료로 덮는 것을 포함하여 이루어지는 소결원료용 석회석 더스트의 균일혼합방법에 관한 것을 그 기술적요지로 한다.In order to achieve the above object, the present invention provides a method of manufacturing a sintered ore comprising the step of mixing the raw material storage tank blending material conveyed to the conveyor belt and granulated in the mixer, and forming a groove having a predetermined size in the compounding material on the conveyor belt. The technical gist of the present invention relates to a method for uniformly mixing limestone dust for sintered raw materials, which comprises covering limestone dust in the groove immediately with the addition of limestone dust into the groove.

Description

소결원료용 석회석 더스트의 균일혼합방법{Method for mixing lime stone dust into raw material of sintering}Method for mixing lime stone dust into raw material of sintering

본 발명은 석회소성공장의 석회석 더스트를 소결원료로 사용하는 방법에 관한 것으로서, 보다 상세하게는 석회석 더스트를 소결원료에 투입할때 비산을 방지하여 배합원료에 CaO성분의 편차를 줄여 소결광의 성분과 품질을 안정시킬 수 있는 소결원료용 석회석 더스트의 균일혼합방법에 관한 것이다.The present invention relates to a method of using limestone dust of a lime firing plant as a sintered raw material, and more particularly, to prevent scattering when limestone dust is added to a sintered raw material, thereby reducing the variation of CaO component in the blended raw material. The present invention relates to a homogeneous mixing method of limestone dust for sintering raw materials capable of stabilizing quality.

고로에서 사용되는 소결광은, 도 1에서와 같이 원료저장조(1)의 주원료(철광석), 부원료(석회석, 규석, 사문암, 생석회), 연료인 코크스를 혼합기(2)에서 혼합한 후에 배합원료저장조(6)에 입조한 다음, 이를 드럼형피더를 통하여 소결기대차(8)에 실고 점화로(7)를 거쳐 착화한 다음, 소결기가 진행하는 동안 배합원료가 소성과정을 통해 제조된다.The sintered ore used in the blast furnace is, as shown in Figure 1, after mixing the main raw material (iron ore), secondary raw materials (limestone, silica, serpentine, quicklime), and coke as fuel in the mixer (2) as shown in Figure 1 6), which is loaded into a sintering machine cart 8 through a drum feeder and ignited through an ignition furnace 7, and then a blended raw material is manufactured through a sintering process while the sintering machine is in progress.

도 1에서 미설명부호 3은 상부광저장조, 4는 집진기, 5는 주배풍기, 6은 배합원료저장조, 9는 파쇄기, 10은 냉각기이다.In FIG. 1, reference numeral 3 denotes an upper light storage tank, 4 a dust collector, 5 a main exhaust fan, 6 a compound material storage tank, 9 a crusher, and 10 a cooler.

부원료중에서 소결광의 원료로 사용되는 생석회는, 석회소성공장의 소성로를 통하여 석회석을 900∼1200℃로 가열시켜 제조된다. 생석회 제조과정중에 발생되는 석회석 더스트는 사이클론(cyclone) 집진기에 포집되며, 석회석 더스트의 성분 및 입도는 표 1과 같다.Quicklime, which is used as a raw material for sintered ore in an auxiliary material, is produced by heating limestone to 900 to 1200 ° C through a firing furnace in a lime firing plant. Limestone dust generated during quicklime manufacturing is collected in a cyclone dust collector, and the composition and particle size of limestone dust are shown in Table 1.

성분(%)ingredient(%) 입도(%)Particle size (%) SiO2 SiO 2 Al2O3 Al 2 O 3 CaOCaO MgOMgO -0.125mm-0.125mm 평균입도(mm)Average particle size (mm) 0.5∼0.80.5 to 0.8 0.1∼0.30.1-0.3 78.0∼81.078.0-81.0 2.5∼3.02.5 to 3.0 69.0∼73.069.0-73.0 0.35∼0.380.35 to 0.38

표 1에 제시된 바와 같이, 석회석 더스트는 -0.125mm 입도가 69∼73%을 차지하는 극미립의 입자로서 폐기물로 분류하여 매립하였다. 그러나, 석회석 더스트의성분중 CaO가 78∼81%의 고농축으로 CaO성분이 석회석 보다 1.4∼1.5배 높아서 석회석의 사용량을 절감할 수 있기 때문에 최근 자원재활용차원에서 소결원료로 사용하고 있다.As shown in Table 1, limestone dust was landfilled as a waste of fine particles having a particle size of -0.125mm occupying 69-73%. However, since the CaO content of the limestone dust is 78-81% high and the CaO component is 1.4-1.5 times higher than the limestone, the amount of limestone can be reduced, and thus it has been used as a raw material for sintering in recent years.

석회석더스트는 소결기의 원료저장조(1)의 원료가 도 2와 같이 콘베어벨트(16)를 통해 혼합기(2)로 공급될때 혼합기의 입측에 설치된 입자공급기(11)에 의해 콘베어벨트(16)상에 공급되고 있다. 이러한 공급과정에서 석회석 더스트가 콘베어벨트에 적재될때 비산이 일어나고, 또한, 석회석 더스트가 적재된 상부로 주부원료와 부원료가 쏟아지면 그 충격으로 다량의 먼지가 연속적으로 비산되고 있다. 이 비산먼지가 공장내부를 오염하는 것을 방지하기 위해 콘베어벨트 전체를 박스형태로 밀봉시키고, 상부에 연결된 닥트(14)로 비산먼지를 포집하고 있다.The limestone dust is formed on the conveyor belt 16 by the particle feeder 11 installed at the inlet side of the mixer when the raw material of the raw material storage tank 1 of the sintering machine is supplied to the mixer 2 through the conveyor belt 16 as shown in FIG. 2. Is being supplied to. In this supply process, when limestone dust is loaded on the conveyor belt, scattering occurs, and when the housewife raw material and the subsidiary material are poured into the upper part where limestone dust is loaded, a large amount of dust is continuously scattered by the impact. In order to prevent the scattering dust from contaminating the inside of the factory, the entire conveyor belt is sealed in the form of a box, and the scattering dust is collected by a duct 14 connected to the upper portion.

이러한 설비로 석회석 더스트의 비산을 막을 수 있지만, 소결원료에 CaO를 공급하기 위해 배합되는 석회석 더스트가 비산되어 집진기에 흡입되기 때문에 소결광성분중 CaO성분의 편차를 증가시켜서 소결광중 스라그(Slag) 함량이 감소되므로 소결광 품질이 악화되는 문제가 있다. 이러한 문제를 해결하기 위해 소결원료를 먼저 콘베어벨트에 적재하고 이 위에 석회석 더스트를 투입한 직후에 살수를 실시하고는 있으나, 여전히 비산먼지가 발생되어 소결배합비의 편차로 소결광의 품질이 떨어지는 문제가 있다.Although this facility prevents the scattering of limestone dust, the slag content of sintered ore is increased by increasing the variation of CaO component in the sintered ore because the limestone dust blended to supply CaO to the sintered raw material is scattered and sucked into the dust collector. There is a problem that the sintered ore quality is deteriorated since this is reduced. In order to solve this problem, the sintered raw material is first loaded on the conveyor belt and sprinkled immediately after the limestone dust is put therein, but there is still a problem in that the quality of the sintered ore is deteriorated due to the dispersion of the sintering compound ratio. .

본 발명은 상기 종래문제를 해결하기 위하여 안출된 것으로, 비산먼지로 인한 환경오염을 줄이면서 배합원료의 성분편차를 방지할 수 있는 소결원료의 균일혼합방법을 제공하는데, 그 목적이 있다.SUMMARY OF THE INVENTION The present invention has been made to solve the above conventional problem, and provides a uniform mixing method of sintered raw materials which can prevent the component deviation of the blended raw materials while reducing environmental pollution due to scattering dust.

도 1은 소결광의 제조공정도1 is a manufacturing process diagram of sintered ore

도 2는 종래의 석회석 더스트를 배합원료로 투입하는 개략도Figure 2 is a schematic diagram of adding a conventional limestone dust as a raw material

도 3은 본 발명에 따른 석회석 더스트의 투입하는 개략도Figure 3 is a schematic diagram of the input of limestone dust according to the present invention

*도면의 주요부분에 대한 부호의 설명** Description of the symbols for the main parts of the drawings *

1.....원료저장조 2.....혼합기1 ..... Raw material storage tank 2 ..... Mixer

12.....배합원료 16.....콘베어벨트12 ... Blended material 16 .. Conveyor belt

20.....입자공급기 22.....배출구20 ..... particle feeder 22 ..... outlet

30.....끌개 40.....덮개판30..Drag 40..Cover plate

상기 목적을 달성하기 위한 본 발명은, 원료저장조의 배합원료를 콘베어벨트로 이송하여 혼합기에 입조한 후 혼합하는 것을 포함한 소결광의 제조방법에 있어서, 상기 콘베어벨트상의 배합원료에 일정크기의 홈을 형성하고, 이 홈내로 석회석더스트를 투입한 직후에 홈내의 석회석더스트를 배합원료로 덮는 것을 포함하여 구성된다.In order to achieve the above object, the present invention provides a method of manufacturing a sintered ore comprising the step of mixing the raw material storage tank blending material conveyed to the conveyor belt and granulated in the mixer, and forming a groove having a predetermined size in the compounding material on the conveyor belt. And immediately after the limestone dust is introduced into the groove, covering the limestone dust in the groove with the compounding material.

이하, 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail.

본 발명은 배합원료에 홈을 형성하고, 이 홈내에 석회석 더스트를 장입한 직후에 홈외측에 있는 배합원료로 홈내에 있는 석회석더스트를 덮으므로서, 석회석더스트의 비산을 방지하여 배합원료에 일정량이 석회석더스트가 함유되도록 하여 소결배합원료의 성분이 균일하게 혼합하도록 하는데, 그 특징이 있다.The present invention forms a groove in the blended raw material and immediately covers the limestone dust in the groove with the blended raw material on the outer side of the groove immediately after charging limestone dust in the groove, thereby preventing the scattering of limestone dust to prevent a certain amount of the blended raw material. The limestone dust is contained to uniformly mix the components of the sintered blend raw material.

먼저, 원료저장조(1)에 있는 주원료, 부원료, 연료(코크스)를 콘베어벨트로 공급하여 혼합기(2)로 이송하면서, 콘베어벨트상에 배합원료의 적재층에 일정 깊이와 일정너비를 갖는 홈(35)을 만든다. 홈의 중심선은 배합원료층의 중심부와 일치하도록 하는 것이 좋으며, 상기 홈의 너비는 배합원료의 폭의 38∼50%이고, 그 깊이는 배합원료층 두께의 40∼50%가 되도록 하는 것이 좋다. 이는 석회석더스트의 공급량과 콘베어벨트의 손상을 고려하여 설정한 것이다.First, the main raw material, subsidiary material and fuel (coke) in the raw material storage tank 1 are supplied to the conveyor belt and transferred to the mixer 2, while the groove having a predetermined depth and a constant width in the loading layer of the compounding material on the conveyor belt ( 35) It is preferable that the center line of the grooves coincide with the center of the compounding material layer, and the width of the grooves is 38 to 50% of the width of the compounding material, and the depth thereof is to be 40 to 50% of the thickness of the compounding material layer. This is set in consideration of the amount of limestone dust supplied and the damage of the conveyor belt.

이 홈은 도 3에 일례로 도시된 끌개(30)로 형성할 수 있다. 끌개(30)는 지지대(34) 상부의 베어링블럭에 연결된 샤프트에 타단이 고정되고, 일단이 배합원료에 삽입되도록 설치되어 콘베어벨트가 이송되면서 배합원료의 적재층에 홈(35)이 형성되도록 한다. 끌개(30)는 콘베어벨트의 손상이 발생하지 않도록 설치한다.This groove may be formed with the drag 30 shown as an example in FIG. The other end 30 is fixed to the shaft connected to the bearing block on the upper support 34, and one end is installed to be inserted into the compounding material so that the conveyor belt is transported so that the groove 35 is formed in the loading layer of the compounding material. . Drag 30 is installed so that damage to the conveyor belt does not occur.

상기와 같이 콘베어벨트에 의해 이송되는 배합원료에 홈을 형성시킨 다음, 이 홈에 석회석더스트를 투입하고 바로 홈의 양측에 있는 배합원료로 홈내의 석회석더스트를 덮는다. 석회석더스트의 투입량은 표 2에 나타난 바와 같이, 석회석의 사용량도 줄이면서 생산성도 높이기 위해서 소결배합원료에 1.1∼1.5% 함유되도록 한다. 아래 표 2에는 석회석 더스트의 함유량에 따른 석회석의 사용비가 제시되어 있다.A groove is formed in the compounding material conveyed by the conveyor belt as described above, and then limestone dust is introduced into the groove, and the limestone dust in the groove is immediately covered with the compounding material on both sides of the groove. As shown in Table 2, the amount of limestone dust contained is 1.1 to 1.5% in the sintered blended raw material in order to reduce the amount of limestone used and increase productivity. Table 2 below shows the limestone usage rates according to the limestone dust content.

배합원료내 석회석 더스트의 함량Content of Limestone Dust in Blended Raw Materials ≤0.5≤0.5 0.6∼1.00.6 to 1.0 1.1∼1.51.1 to 1.5 1.6∼2.01.6 to 2.0 소결광 성분의 변화Change of Sintered Ore Components SiO2 SiO 2 -- -- 0.01이하0.01 or less 0.02이하0.02 or less CaOCaO 0.40∼0.450.40 to 0.45 0.90∼1.000.90 to 1.00 1.30∼1.401.30-1.40 1.75∼1.851.75-1.85 MgOMgO 0.02이하0.02 or less 0.04이하Less than 0.04 0.06이하0.06 or less 0.08이하Less than 0.08 석회석 변동비Limestone Variable Cost 0.8∼0.90.8 to 0.9 1.55∼1.751.55-1.75 2.35∼2.652.35-2.65 3.10∼3.503.10 to 3.50

석회석 더스트의 투입은 상기 끌개(30)의 후방 연장선에 입자공급기(20)를 설치하여 형성되는 홈내로 석회석 더스트가 투입되도록 한다.The injection of limestone dust causes the limestone dust to be introduced into the grooves formed by installing the particle feeder 20 in the rear extension line of the dragger 30.

또한, 홈내의 석회석 더스트를 배합원료를 덮는 것은, 도 3에 일례로 제시된 덮개판(40)을 이용할 수 있다. 덮개판(40)은 홈(35)내에 있는 석회석 더스트를 배합원료로 덮으면서 석회석더스트의 비산을 막도록 다양한 형상이 적용될 수 있다. 먼저, 배합원료를 홈내로 집어넣기 위해서는 덮개판(40)의 하단부의 양단이 홈 양측의 배합원료에 접하여 배합원료를 홈내로 밀어넣도록 하며, 상단부는 입자공급기의 배출관까지 신장하여 배출관을 포위하도록 설계하는 것이 바람직하다.In addition, the cover plate 40 shown as an example in FIG. 3 can be used for covering the compound raw material with the limestone dust in a groove | channel. Cover plate 40 may be applied to a variety of shapes to prevent the scattering of limestone dust while covering the limestone dust in the groove 35 with the compounding material. First, in order to insert the compounding material into the grooves, both ends of the lower end of the cover plate 40 are in contact with the compounding raw materials on both sides of the groove to push the compounding material into the grooves, and the upper end extends to the discharge pipe of the particle feeder to surround the discharge pipe. It is desirable to design.

이러한 덮개판은 일체로 형성할 경우 덮개판의 상단부는 배출관에 접하여 비산을 완전히 방지하도록 할 수 있다. 또한, 덮개판을 도 3과 같이 분리된 두 판의 날개 모양으로 형성할 수도 있다.When the cover plate is formed integrally, the upper end of the cover plate can be in contact with the discharge pipe to completely prevent scattering. In addition, the cover plate may be formed in the shape of a wing of two plates separated as shown in FIG.

본 발명에 따라 석회석 더스트가 혼합된 배합원료는 곧 바로 혼합기에 투입되어 물과 혼합된다. 따라서, 석회석더스트가 외부로 노출되는 것을 방지하여 더스트의 비산을 막을 수 있고, 석회석더스트의 손실을 막아 혼합비의 편차를 없앨 수 있다.According to the present invention, the raw material in which the limestone dust is mixed is immediately added to the mixer and mixed with water. Therefore, the limestone dust can be prevented from being exposed to the outside to prevent dust from scattering, and the loss of the limestone dust can be prevented to eliminate variations in the mixing ratio.

이하, 본 발명을 실시예를 통하여 보다 구체적으로 설명한다.Hereinafter, the present invention will be described in more detail with reference to Examples.

[실시예]EXAMPLE

유효화상면적이 40㎡이고 소결층후가 450mm의 소형 소결기에서 표 4와 같이, 주, 부원료조건으로 소결광을 제조하고 소결광의 품질 등 제반 제조여건을 알아보았다.In a small sintering machine having an effective image area of 40 m2 and a sintered layer of 450 mm, as shown in Table 4, the sintered ore was manufactured under primary and secondary raw material conditions, and the general conditions of the sintered ore were examined.

주원료(중량%)Main raw material (wt%) 부원료(중량%)Subsidiary Material (wt%) HAM.FHAM.F CAJ.FCAJ.F HIY.FHIY.F RBR.FRBR.F ScaleScale 규석burr 사문암Serpentine 석회석Limestone 생석회quicklime 18∼2018-20 22∼2522-25 23∼2623-26 9∼119 to 11 3∼53 to 5 0.3이하0.3 or less 2.0∼2.42.0 to 2.4 14∼1614-16 1.4∼1.61.4 to 1.6

구분division 비교예1Comparative Example 1 비교예2Comparative Example 2 발명예3Inventive Example 3 비교예4Comparative Example 4 석회석 더스트의 양(%)Amount of limestone dust (%) 0.5이하0.5 or less 0.6∼1.00.6 to 1.0 1.1∼1.51.1 to 1.5 1.6∼2.01.6 to 2.0 집진기 더스트중 CaO(%)CaO (%) in dust collector dust 8.2∼8.38.2-8.3 8.2∼8.38.2-8.3 8.2∼8.38.2-8.3 8.3∼8.58.3 to 8.5 소결광중 CaO편차(%)CaO deviation in sintered ore (%) 0.2∼0.30.2 to 0.3 0.2∼0.30.2 to 0.3 0.2∼0.30.2 to 0.3 0.2∼0.40.2 to 0.4 배합원료 입도중 -0.125mm-0.125mm in blended raw material 9.0∼9.29.0-9.2 9.0∼9.39.0 to 9.3 9.1∼9.49.1-9.4 9.1∼9.59.1 to 9.5 생산성(T/D/㎡)Productivity (T / D / ㎡) 38.0∼39.538.0-39.5 38.0∼39.538.0-39.5 38.0∼39.538.0-39.5 37.0∼38.537.0-38.5 강도(%)burglar(%) 90.0∼90.290.0 to 90.2 90.0∼90.390.0 to 90.3 90.1∼90.490.1 to 90.4 90.1∼90.590.1 to 90.5 석회석 사용비(%)Limestone Cost (%) 14.0∼16.014.0 to 16.0 12.5∼14.512.5-14.5 11.5∼13.511.5-13.5 10.0∼12.510.0-12.5

표 5에서 비교예(1)(2)는 석회석 더스트를 1.0% 사용한 경우로, 생산성과 품질에 변화요인은 없었다. 발명예(1)은 석회석 더스트를 1.1∼1.5% 첨가한 것으로, 이 경우 배합원료에 섞인 미립자(0.125mm이하)가 0.1∼0.2% 증가되어 공극율이 축소되며, 강도는 0.1∼0.2%향상되었고, 소결부원료로 사용하는 석회석은 2∼2.5% 사용비를 줄일 수 있었다. 비교예(3)은 석회석 더스트를 1.6∼2.0% 첨가한 것으로, 배합원료에 섞인 미립자(0.125mm이하)가 0.1∼0.3% 증가되어 강도는 발명예(1) 보다 양호하나, CaO성분 편차폭이 0.1∼0.2% 증가되고 통기성의 악화요인이 발생되므로 생산성은 0.5∼1.0T/D/㎡ 감소된다.In Table 5, Comparative Example (1) and (2) used 1.0% limestone dust, and there was no change in productivity and quality. Inventive Example (1) added 1.1 to 1.5% of limestone dust, in which case the fine particles (0.125 mm or less) mixed in the blended material increased by 0.1 to 0.2%, the porosity was reduced, and the strength was improved by 0.1 to 0.2%. Limestone used as sintered feedstock was able to reduce the use cost of 2 ~ 2.5%. In Comparative Example (3), 1.6 to 2.0% of limestone dust was added, and the fine particles (0.125 mm or less) mixed in the blended material increased by 0.1 to 0.3%, and the strength was better than that of Inventive Example (1). Productivity is reduced by 0.5 to 1.0 T / D / m 2 because of an increase of 0.1 to 0.2% and deterioration of breathability.

이 결과로서, 본 발명에 따라 석회석 더스트를 1.1∼1.5% 사용하면 소결광의 화학성분과 품질에 변동 없이 석회석의 사용비를 2∼2.5% 정도 줄일 수 있는 잇점이 있을 것을 파악되었다. 본 발명에 따른 조업결과와 종래의 조업결과를 비교하면아래 표 6과 같다.As a result, it has been found that the use of limestone dust in accordance with the present invention can reduce the use ratio of limestone by 2 to 2.5% without changing the chemical composition and quality of the sintered ore. Comparing the operation results according to the present invention and the conventional operation results are shown in Table 6 below.

구분division 집진기먼지중 CaO(%)Dust collection dust CaO (%) 소결광중 CaO편차(%)CaO deviation in sintered ore (%) 배합원료입도중 -0.125mm-0.125mm during blending raw material 생산성productivity 강도burglar 석회석 사용비Limestone Cost 종래예(1)Conventional example (1) 8.408.40 0.400.40 9.19.1 37.537.5 89.989.9 14.014.0 종래예(2)Conventional example (2) 8.608.60 0.500.50 9.29.2 37.037.0 89.789.7 15.015.0 종래예(3)Conventional example (3) 8.308.30 0.300.30 9.19.1 38.038.0 90.090.0 13.013.0 종래예(4)Conventional example (4) 8.508.50 0.450.45 9.09.0 37.837.8 89.889.8 14.014.0 발명예(2)Inventive Example (2) 8.258.25 0.250.25 9.39.3 38.538.5 90.390.3 12.512.5 발명예(3)Inventive Example (3) 8.208.20 0.200.20 9.29.2 39.539.5 90.490.4 11.511.5 발명예(4)Inventive Example (4) 8.308.30 0.300.30 9.09.0 38.038.0 90.190.1 13.013.0 발명예(5)Inventive Example (5) 8.258.25 0.210.21 9.19.1 39.039.0 90.290.2 13.513.5

표 6에서 알 수 있듯이, 본 발명에서는 소결광의 화학성분중 CaO편차가 0.30%이하로 감소되어 성분과 배합원료의 입도안정으로 생산성이 1.5T/D/㎡ 증가되고 강도는 0.3% 증가되어 종래의 방법 보다 조업실적이 향상되을 알 수 있었다.As can be seen from Table 6, in the present invention, the CaO deviation of the chemical composition of the sintered ore is reduced to 0.30% or less, so that the productivity is increased by 1.5T / D / m2 and the strength is increased by 0.3% due to the particle size stability of the ingredients and the blended raw materials. The operation performance could be improved more than the method.

상술한 바와 같이, 본 발명에서는 폐기처리되는 석회석 더스트를 배합원료에 첨가하여 재활용 할 수 있으며, 배합원료 수송과정에서 소실되는 배합비와 성분비의 편차폭을 줄여서 소결광의 화학성분과 강도를 안정시키며, 석회석의 사용량을 줄일 수 있는 유용한 효과가 있다.As described above, in the present invention, the limestone dust to be disposed of can be recycled by adding it to the blended raw material, and the chemical composition and strength of the sintered ore are stabilized by reducing the variation in the blending ratio and the component ratio lost during the transport of the blended raw material. There is a useful effect to reduce the amount of use.

Claims (3)

삭제delete 삭제delete 원료저장조의 배합원료를 콘베어벨트로 이송하여 혼합기에 입조한 후 혼합하는 것을 포함한 소결광의 제조방법에 있어서, 상기 콘베어벨트상의 배합원료에 일정크기의 홈을 형성하고, 이 홈내로 석회석더스트를 상기 배합원료에 1.1∼1.5% 함유되도록 투입한 직후에 홈내의 석회석더스트를 배합원료로 덮는 것을 포함하여 이루어지는 소결원료용 석회석 더스트의 균일혼합방법.In the method of manufacturing a sintered ore, which includes conveying a blended raw material of a raw material storage tank to a conveyor belt and mixing the mixed raw material into a mixer, a groove having a predetermined size is formed in the blended raw material on the conveyor belt, and the limestone dust is blended into the groove. A homogeneous mixing method of limestone dust for sintered raw materials, comprising covering the limestone dust in the groove with the blending raw material immediately after it is added so as to contain 1.1 to 1.5% of the raw material.
KR10-1999-0049888A 1999-11-11 1999-11-11 Method for mixing lime stone dust into raw material of sintering KR100411271B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR10-1999-0049888A KR100411271B1 (en) 1999-11-11 1999-11-11 Method for mixing lime stone dust into raw material of sintering

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR10-1999-0049888A KR100411271B1 (en) 1999-11-11 1999-11-11 Method for mixing lime stone dust into raw material of sintering

Publications (2)

Publication Number Publication Date
KR20010046207A KR20010046207A (en) 2001-06-05
KR100411271B1 true KR100411271B1 (en) 2003-12-18

Family

ID=19619536

Family Applications (1)

Application Number Title Priority Date Filing Date
KR10-1999-0049888A KR100411271B1 (en) 1999-11-11 1999-11-11 Method for mixing lime stone dust into raw material of sintering

Country Status (1)

Country Link
KR (1) KR100411271B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101719516B1 (en) * 2015-11-05 2017-03-24 주식회사 포스코 Method for manufacturing sintered ore

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58188235A (en) * 1982-04-24 1983-11-02 Nippon Steel Corp Transporting method of sintered material
JPS63130721A (en) * 1986-11-20 1988-06-02 Kawasaki Steel Corp Method for supplying sintered ore raw material
JPH04193914A (en) * 1990-11-28 1992-07-14 Kawasaki Steel Corp Method for supplying sintering raw material

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58188235A (en) * 1982-04-24 1983-11-02 Nippon Steel Corp Transporting method of sintered material
JPS63130721A (en) * 1986-11-20 1988-06-02 Kawasaki Steel Corp Method for supplying sintered ore raw material
JPH04193914A (en) * 1990-11-28 1992-07-14 Kawasaki Steel Corp Method for supplying sintering raw material

Also Published As

Publication number Publication date
KR20010046207A (en) 2001-06-05

Similar Documents

Publication Publication Date Title
CA1180952A (en) Method for melting and treating waste
JP5194378B2 (en) Method for producing sintered ore
JP5699567B2 (en) Method for producing sintered ore
JP5315659B2 (en) Method for producing sintered ore
JP6897859B2 (en) Manufacturing method of granulated sintering raw material
KR100217892B1 (en) Sintered steel manufacturing process
KR100411271B1 (en) Method for mixing lime stone dust into raw material of sintering
CN109402383B (en) Method and device for optimizing sintering moisture
KR101696328B1 (en) Apparatus for raw material process, method thereof and pellet
JP3319319B2 (en) Processing method of sintering raw material
JP3675105B2 (en) Sintering raw material processing method
KR100550756B1 (en) Optimum granulation method of inplant by-product
KR100234883B1 (en) Soil brick made by electric arc furnace dust and manufacturing method thereof
JPH01147023A (en) Manufacture of sintered ore
KR0118997B1 (en) Method and apparatus for sintering ore
KR100479997B1 (en) Method for manufacturing sintered ore by using CDQ dust
JP3294908B2 (en) Sintering operation method
JPS6221055B2 (en)
KR100469298B1 (en) SOx AND NOx REDUCING METHOD OF SINTERING DISCHARGING GAS BY USING ANTHRACITE HAVING LOW NITROGEN AND SULFUR
KR20030035700A (en) A method of iron ore sintering using anthracite and coke as fuel
KR100380741B1 (en) Method for granulation of sinter mixture
JPH10280058A (en) Treatment of sintering raw material
KR20010048809A (en) Sintered ore manufacturing using pulverized burnt lime
JP4238401B2 (en) Method for producing low SiO2 sintered ore
KR100929175B1 (en) Sintering productivity improving device and sintering productivity improving method using the same

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20121122

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20131129

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20141128

Year of fee payment: 12

FPAY Annual fee payment

Payment date: 20151202

Year of fee payment: 13

LAPS Lapse due to unpaid annual fee