KR970002117B1 - Blowing method of powered metal - Google Patents

Blowing method of powered metal Download PDF

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KR970002117B1
KR970002117B1 KR1019940040301A KR19940040301A KR970002117B1 KR 970002117 B1 KR970002117 B1 KR 970002117B1 KR 1019940040301 A KR1019940040301 A KR 1019940040301A KR 19940040301 A KR19940040301 A KR 19940040301A KR 970002117 B1 KR970002117 B1 KR 970002117B1
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South Korea
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blast furnace
iron
slurry
lubricating oil
waste
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KR1019940040301A
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Korean (ko)
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KR960023097A (en
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김경태
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김만제
포항종합제철주식회사
신창식
재단법인산업과학기술연구소
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/008Composition or distribution of the charge
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/001Injecting additional fuel or reducing agents

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)

Abstract

The powdered metal from a dust collector or rolling mill in ironworks is blown into a blast furnace, by spraying a slurry mixing the powdered metal and a waste lubricant. The waste lubricant containing a crude Pb and Zn less than 200 ppm having low melting point and a iron powder less than 50 wt.% are mixed to give the slurry. The slurry fuel is sprayed into the blower through a blowing lance.

Description

분말철의 고로취입방법Blast Furnace Blowing Method of Powdered Iron

본 발명은 제철소의 집진설비 또는 압연설비등에서 발생되는 분말철을 고로에 취입하는 방법에 관한 것으로서, 보다 상세하게는 분말철을 폐윤활유와 혼합하여 고함철, 고발열량의 슬러리를 제조한 후 분무하여 고로의 풍구에 취입하는 방법에 관한 것이다.The present invention relates to a method of injecting powder iron generated from a dust collecting facility or a rolling mill of a steel mill into a blast furnace, and more particularly, by mixing powder iron with waste lubricating oil to prepare a slurry containing high iron and high calorific value and spraying It is about a method to blow into the blast furnace blast furnace.

보통 제철소의 각종 집진설비 또는 압연설비의 압연공정에서 부산물로 발생되는 분말철은 다량의 산화철을 함유하고 있어 고로의 원료로 재활용되고 있다.In general, powdered iron produced as a by-product from various dust collection facilities or rolling mills in steel mills contains a large amount of iron oxide and is recycled as a raw material for blast furnaces.

보통 분말철을 고로에 이용하기 위해서는 분말철을 소결에 의해 괴상화시켜 고로의 상부에 장입하는 방법이 널리 이용되고 있다. 특히, 폐유와 같은 탄화수소에 의해 오염된 분말철은 우선 오염물질을 소각시켜 없앤 후, 소결과정을 통해 괴상화시켜 고로의 상부를 통해 장입된다.Usually, in order to use powder iron in a blast furnace, the method of massifying powder iron by sintering and charging to the upper part of a blast furnace is widely used. In particular, powdered iron contaminated by hydrocarbons such as waste oil is first incinerated to remove contaminants and then agglomerated through sintering to be charged through the upper part of the blast furnace.

그러나, 고로상부를 통해 분말철을 투입하려면 괴상화를 위한 소결공정이 수반되어야 한다는 단점이 있다.However, in order to inject powder iron through the blast furnace portion, there is a disadvantage that a sintering process for bulking should be involved.

이러한 단점을 해결할 수 있는 방법중 한가지는 분말철을 그대로 고로의 풍구에 직접 취입하는 방법이 있으나 분말철을 풍구에 취입하여 재활용하고자 하는 경우 분말철을 환원시키고 용해시킬 수 있는 탄화수소류와 혼합되어야 한다. 이를 위해 분말철을 미분석탄 또는 중질유등과 혼합하는 방법을 생각해 볼 수 있으나, 이 경우 혼합물 제조 및 수송이 어려우므로 고로풍구에의 취입이 불가능하다.One way to solve this drawback is to directly inject the powdered iron into the blast furnace, but if you want to recycle the powdered iron in the blast furnace, it must be mixed with hydrocarbons that can reduce and dissolve the powdered iron. . For this purpose, a method of mixing the powdered iron with uncoated coal or heavy oil may be considered, but in this case, the mixture is difficult to manufacture and transport, and thus it is impossible to blow into the blast furnace.

따라서, 분말철을 고로풍구내로 그대로 취입할때 분말철을 용융환원시킬 수 있는 탄화수소매체가 필요하다.Therefore, there is a need for a hydrocarbon medium that can melt-reduce powder iron when the powdered iron is blown into the blast furnace vent.

한편, 산업의 발달 및 자동차등 수송수단의 증가와 함께 윤활유의 사용은 급증하며 이에따라 필연적으로 폐윤활유의 발생이 뒤따른다. 따라서 폐윤활유의 재활용은 자원의 이용 측면 뿐만 아니라 환경오염방지 측면에서 대단히 중요한 사안이다. 가령 소규모 배출업소의 경우 음성적으로 자체 연료를 사용하거나 일부 업체의 경우 불법 투기함으로서 대기환경 및 수질환경, 토양환경을 심각하게 오염시키고 있기도 하다.On the other hand, with the development of the industry and the increase of vehicles such as automobiles, the use of lubricating oil is rapidly increasing, which inevitably leads to the generation of waste lubricants. Therefore, recycling of waste lubricating oil is a very important issue in terms of resource utilization as well as environmental pollution prevention. For example, small companies use their own fuel negatively or some companies dump illegally, seriously polluting the air, water and soil environments.

이러한 폐윤활유는 재활용할 경우 사용목적에 따라 각기 다른 정제공정을 채택하여 정제처리한다. 현재 윤활유로 재생할 경우에는 감압증류공정 또는 산.백토처리 공정등이 채택되고 있는데, 그러나 이 방법들은 윤활유 가격의 하락, 운전비의 과다, 다량의 산슬러리 발생등으로 인해 경제성 및 환경처리 측면에서 불리한 처리공정으로 평가되고 있다.When the waste lubricant is recycled, it is purified by adopting different refining processes depending on the purpose of use. Currently, when regenerating with lubricating oil, decompression distillation process or acid and clay treatment process are adopted.However, these methods are disadvantageous in terms of economic and environmental treatment due to lower lubricating oil price, excessive operating cost, and large amount of acid slurry. It is evaluated as a process.

특히, 연료유로 재생할 경우에는 Salusinszky 공정(미국 특허 4,259,021)과 같은 화학처리/원심분리 공정이 활용되고 있는데, 이는 폐윤활유내에 다량 존재하는 중금속 및 기타 화분성분 등을 제거하기 위한 것이다. 그러나, 이와같이 정제된 폐윤활유일지라도 하기 표 1에 나타난 바와같이, 각종 중금속 및 회분이 여전히 함유되어 있기 때문에 산업용 보일러나 소성로등의 열공급설비에 이용할때 2차 대기오염 문제를 유발시킬 수 있다.In particular, when the fuel oil is recycled, a chemical treatment / centrifugation process such as the Salusinszky process (US Pat. No. 4,259,021) is used, which is intended to remove heavy metals and other pollen components present in a large amount of waste lubricant. However, even the refined waste lubricating oil, as shown in Table 1 below, may still cause secondary air pollution when used in heat supply facilities such as industrial boilers or kilns, since various heavy metals and ash are still contained.

따라서, 폐윤활유를 보일러등의 연료유로 사용하고자 할때는 정제공정이 복잡해지고 그에 따라 처리비용이 높아지는 문제점이 있다.Therefore, when using waste lubricant as fuel oil, such as a boiler, there is a problem that the refining process is complicated and the treatment cost increases accordingly.

이에 따라 본 발명자는 상기한 분말철 및 조정제된 폐윤활유를 고로에 사용할 수 있는 방안에 대하여 연구와 실험을 행하고 그 결과에 근거하여 본 발명을 제안하게 된 것으로서, 본 발명은 분말철을 고로의 풍구에 취입할때 분말철을 용융환원시킬 수 있는 탄화수소매체로 조정제된 폐윤활유를 사용하므로서, 분말철을 분말상태 그대로 취입할 수 있는 효과적인 고로 취입방법을 제공하고자 하는데, 그 목적이 있다.Accordingly, the present inventors have conducted studies and experiments on the method of using the above-described powdered iron and the adjusted waste lubricating oil in the blast furnace, and the present invention was proposed based on the results, and the present invention suggests that the powdered iron is the blast furnace. The purpose of the present invention is to provide an effective blast furnace blowing method for blowing powdered iron as it is, by using waste lubricant adjusted as a hydrocarbon medium capable of melt-reducing powdered iron when blowing into.

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

본 발명은 조정제된 폐윤활유에 50중량% 이하의 철분말의 혼합하여 슬러리를 제조한 다음, 이 슬러리 연료를 고로 풍구내로 분사하여 구성되는 분말철의 고로 취입방법에 관한 것이다.The present invention relates to a method for blowing blast furnace of powder iron, which is prepared by mixing a crude waste powder of crude oil of 50% by weight or less and then injecting the slurry fuel into the blast furnace tuyere.

이하, 본 발명에 대하여 상세히 설명한다.EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated in detail.

본 발명에서 사용되는 통상의 조정제된 폐윤활유를 고로의 풍구에 취입할 경우 Ca, Mg, 유황등은 광석 및 코크스, 석탄내의 슬래그성 물질과 함께 배출되기 때문에 대기공해 문제점이 없는 장점이 있다.When the conventional adjusted waste lubricating oil used in the present invention is blown into the blast furnace blast furnace, Ca, Mg, sulfur and the like are discharged together with the slag material in the ore, coke and coal, so there is no air pollution problem.

그러나, 폐윤활유중 함유되어 있는 Pb, Zn과 같은 저융점 금속은 폐윤활유중에 수천 ppm으로 함유되어 있으면 고로 풍구내로 취입시 고로괴상대(lumped zone)에서 상기 저융점물질들이 액상에서 응축되는 반복과정을 거쳐 고로의 장입물에 침적되므로서, 장입물의 하강을 어렵게 하거나 통기성을 악화시킬 수 있다. 따라서, 고로에 사용되는 폐윤활유는 조정제된 폐윤활유를 사용하여야 하는데, 조정제된 폐윤활유에 함유되는 Pb, Zn의 함량은 매우 적기 때문에 고로내에서 순환되면서 고로 장입물에 영향을 주지 않고 또한 로외로 배출되지 않는다.However, if the low melting point metals such as Pb and Zn contained in the waste lubricating oil contain thousands of ppm in the waste lubricating oil, the low melting point materials are condensed in the liquid phase in the lumped zone when blown into the blast furnace. By being deposited in the blast furnace charges, it is difficult to lower the charges or worsen breathability. Therefore, the waste lubricating oil used in the blast furnace should use the adjusted waste lubricating oil. Since the content of Pb and Zn contained in the refined waste lubricating oil is very small, it is circulated in the blast furnace and does not affect the blast furnace contents. It is not discharged.

특히, 조정제된 폐윤활유중에 함유된 Pb 및 Zn는 200ppm 이하로 하면 더욱 바람직하다.In particular, Pb and Zn contained in the adjusted waste lubricating oil are more preferably at most 200 ppm.

이러한 조정제 폐윤활유를 탄화수소 매체로 하여 철분말을 고로 풍구에 취입하기 위해서는, 철분말을 폐윤활유에 혼합하여 슬러리를 제조하는 것이 필요한데 이때, 제조된 슬러리는 펌핑(pumping)이 가능한 정도의 점도를 유지하고 분무될 수 있는 정도의 유동도를 가져야만 한다. 이를 위해 본 발명에서는 상기 조정제된 폐윤활유에 철분말을 50중량% 이하로 첨가하여 혼합하는 것이 바람직하다. 만일 철분말을 조정제 폐활유에 대하여 50중량% 이상으로 혼합시키면 슬러리연료의 발열량이 떨어질 뿐만 아니라 특히 분무성이 현저하게 저하되어 바람직하지 못하다.In order to blow iron powder into the blast furnace using the crude waste lubricating oil as a hydrocarbon medium, it is necessary to prepare the slurry by mixing the iron powder with the waste lubricating oil, wherein the prepared slurry maintains a viscosity that can be pumped. And have a degree of flow that can be sprayed. To this end, in the present invention, it is preferable to add the iron powder to the adjusted waste lubricating oil by adding 50% by weight or less. If the iron powder is mixed in an amount of 50% by weight or more with respect to the crude waste lubricant, the calorific value of the slurry fuel not only decreases, but the sprayability is remarkably lowered, which is not preferable.

이와같은 혼합슬러리내의 철 입자는 폐윤활유내에 첨가되어 있는 각종 계면활성제에 의해 윤활유내에 고루 분산되며 장기 저장시 침강문제도 없다.The iron particles in the mixed slurry are evenly dispersed in the lubricating oil by various surfactants added in the waste lubricating oil, and there is no sedimentation problem during long-term storage.

상기 방법에 의해 혼합된 조정제 폐윤활유/분말철 슬러리 연료는 고로의 풍구에 취입노즐을 설치하여 열풍과 함꼐 레이스웨이(raceway)에 공급하여 취입한다.The crude waste lubricating oil / powder iron slurry fuel mixed by the above method is blown by installing a blowing nozzle in the blast furnace blast furnace and supplying it to a raceway with hot air.

고로의 레이스웨이는 열풍과 코크스 및 미분석탄이 격렬하게 연소반응을 일으키는 영역으로서, 최대 2000℃ 이상의 고온영역이다. 이 영역에 본 발명에 의해 제조한 슬러리 연료를 취입하게 되면, 가연성 탄화수소의 연소와 함께 산화철 입자의 환원원, 용융과정이 급속하게 일어난다. 이때, 슬러리내에 존재하는 회분 및 기타 유황성분등은 슬래그화되어 타 슬래그와 함께 배출된다. 특히, 상기 슬러리 연료는 무화되어 취입되기 때문에 레이스웨이내에서의 연소 및 철입자의 환원용융이 매우 빠르게 되고, 현재의 고로기술인 미분탄 취입방식과 비교할때도 연소성이 훨씬 우수하다.The blast furnace raceway is a region in which hot air, coke and analytical coal react violently, and have a high temperature range of up to 2000 ° C. When the slurry fuel produced by the present invention is injected into this region, the reduction source and melting process of the iron oxide particles occur rapidly with the combustion of the flammable hydrocarbon. At this time, ash and other sulfur components present in the slurry are slag and discharged together with the other slag. In particular, since the slurry fuel is atomized and blown, combustion and reduction melting of iron particles in the raceway are very fast, and combustibility is much superior to that of the pulverized coal blowing method, which is the current blast furnace technology.

또한, 경제성 면에서 볼때 현재의 폐윤활유의 가격과 정제비용을 합치더라도 석탄 보다 원료가격이 싸며, 미분탄 취입시 석탄의 분쇄비용 등을 고려하면 본 발명에 따른 슬러리 연료 취입방법은 훨씬 경제적이다. 더구나, 본 발명의 슬러리에 의한 고로 취입방법은 분철을 다량 혼합시켜 사용하기 때문에 분철의 재활용면에서 가장 경제적이며 환경측면에서도 우수한 장점을 갖고 있다.In addition, in terms of economics, even if the combined price of the current waste lubricating oil and the refining cost are lower than raw material prices, considering the pulverization cost of coal when pulverized coal is blown, the slurry fuel blowing method according to the present invention is much more economical. In addition, the blast furnace blowing method of the slurry of the present invention is the most economical in terms of recycling of powdered iron and has excellent advantages in terms of environment because it is used by mixing a large amount of powdered iron.

이하, 본 발명을 실시예를 통하여 구체적으로 설명한다.Hereinafter, the present invention will be described in detail through examples.

[실시예 1]Example 1

상기 표 1과 같은 조성을 같은 조정제 폐윤활유와 분철을 하기 표 2와 같은 배합으로 혼합하여 슬러리를 제조하였다.Slurry was prepared by mixing the same composition as shown in Table 1 waste lubricant and powdered iron in the same formulation as Table 2 below.

이때 조정제유와 분말철의 혼합은 각각 일정량씩 평량한 후 총중량이 30kg이 되도록 혼합조에 넣고 약 30분 정도 상온에서 행하였다. 혼련후 이들 슬러리에 대하여 점도 및 분무성을 측정하여 평가하고, 그 결과를 하기 표 2에 나타내었다. 이때, 슬러리의 점도는 브룩필드사 제품모델 DV-Ⅱ 로 100rpm에서 측정하였다.At this time, the mixture of the crude oil and the powdered iron were each weighed in a predetermined amount and put in a mixing tank so that the total weight was 30 kg, and the mixture was performed at room temperature for about 30 minutes. After kneading, these slurries were measured and evaluated for viscosity and sprayability, and the results are shown in Table 2 below. At this time, the viscosity of the slurry is Brookfield Co., Ltd. model DV-Ⅱ Measured at 100 rpm.

상기 표 2에 나타난 바와 같이, 조정제 유에 분말철이 50중량% 이상으로 혼합된 비교예(1)(2)의 경우 분무성이 저하되어 고로 취입시 분무가 불가능함을 알 수 있다.As shown in Table 2, in the case of Comparative Example (1) (2) in which powder iron is mixed in 50% by weight or more of the crude oil, the sprayability is lowered and spraying is not possible when the blast furnace is blown.

이에 반하여, 발명예(1-5)의 경우에서 알 수 있듯이, 고로에 취입될 수 있을 정도의 분무성을 유지할 수 있기 위해서는 분말철이 최대 50중량%까지 가능함을 나타내고 있다.On the contrary, as can be seen in the case of Inventive Example (1-5), it is shown that up to 50% by weight of powdered iron is possible in order to maintain spraying ability to be blown into the blast furnace.

[실시예 2]Example 2

실시예 1과 같은 방법으로 조정제된 폐윤활유와 분말철을 하기 표 3과 같이 조성을 변화시키면서 슬러리를 제조하고, 제조된 슬러리 연료의 조성에 따른 발열량과 연소시의 단열화염 온도를 조사하고 그 결과를 하기 표 3에 나타내었다.Slurry was prepared by adjusting the composition of waste lubricant and powder iron adjusted in the same manner as in Example 1 as shown in Table 3, and the calorific value according to the composition of the prepared slurry fuel and the adiabatic flame temperature during combustion were investigated and the result It is shown in Table 3 below.

상기 표 3에 나타난 바와같이, 조정제된 폐윤활유에 분말철을 5-중량% 이상으로 혼합한 비교예(1)(2)의 경우 단열화염온도는 우수하나, 발열량이 미흡하고, 또한 실시예 1에서 알 수 있듯이 분무성이 저하되어 바람직하지 않음을 알 수 있다.As shown in Table 3, in Comparative Example (1) (2) in which powdered iron was mixed with more than 5% by weight of the adjusted waste lubricating oil, the thermal insulation flame temperature was excellent, but the calorific value was insufficient. As can be seen, the spraying property is lowered, which is not preferable.

반면에 조정제된 폐윤활유에 분말철이 50중량% 이하로 혼합된 발명예(5-8)의 경우에는 분무성이 양호할 뿐만 아니라 발열량 및 단열화염온도가 높기 때문에 고로의 레이스웨이에 취입하여도 레이스웨이를 냉각시킬 가능성은 없음을 알 수 있다.On the other hand, Inventive Example (5-8), in which powdered iron is mixed to 50% by weight or less of the adjusted waste lubricating oil, not only has good spraying properties but also has high calorific value and high thermal flame temperature. It can be seen that there is no possibility of cooling the way.

[실시예 3]Example 3

상기 발명예(5)(7)의 혼합슬러리를 분무하여 연소시킨 후, 분무노즐선단으로부터 0.5m, 1.0m에서 시료를 채취하는 방법으로 연소성 시험을 행하고, 그 결과를 하기 표 4에 나타내었다. 이때, 연소율은 가연분 함량 측정에 의해 다음 식을 이용하여 계산하였다.After spraying and burning the mixed slurry of Inventive Example (5) and (7), a combustibility test was conducted by taking a sample at 0.5 m and 1.0 m from the spray nozzle tip, and the results are shown in Table 4 below. At this time, the combustion rate was calculated by the following formula by the flammable content measurement.

연소율(%)=[1-{C(100-C)/C(100-C)}]×100Burn rate (%) = [1- {C (100-C) / C (100-C)}] × 100

여기서, C는 초기시료내 가연분함량(중량%), C는 연소후 채취시료 가연분함량(중량%).Where C is the flammable content (% by weight) in the initial sample and C is the flammable content (% by weight) of the sample taken after combustion.

상기 표 4에 나타난 바와같이, 본 발명에 따른 슬러리의 경우 1m 이내의 매우 짧은 연소영역에서 완전 연소됨을 알 수 있다. 특히, 슬러리의 연소시에 1m 지점에서 환원, 용융철의 생성을 확인할 수 있는 바, 이는 분말철을 고로의 레이스웨이에 취입할 때 조정제된 폐윤활유와 적절히 슬러리화 함으로써 직접 용융철을 생산할 수 있을 뿐만 아니라 고발열량의 열원공급이 가능함을 보여주고 있다.As shown in Table 4, it can be seen that the slurry according to the present invention is completely burned in a very short combustion zone within 1 m. Particularly, when the slurry is burned, it can be reduced at 1 m and the production of molten iron, which can be directly produced by directly slurrying powdered iron with the lubricated waste lubricating oil when injected into the blast furnace raceway. In addition, it shows that it is possible to supply a high heat generation heat source.

상술한 바와같이, 본 발명은 통상 괴상화물로 고로상부에 장입되는 분말철을 폐윤활유와 적절히 혼합하여 슬러리 연료로 제조한 다음 이를 고로 풍구내에로 취입하므로서, 분말철을 분말상태 그대로 사용이 가능하여 종래의 소결공정이 수반되는 괴상화를 통한 분말철 재활용 방법 및 미분탄 석탄 취입에 비하여 간단하고 효율적인 분말철의 고로 취입방법이 제공되어, 분말철 및 폐윤활유의 재활용 측면에서 보다 효과적이다.As described above, in the present invention, the powdered iron charged into the upper part of the blast furnace is usually mixed with waste lubricating oil to be prepared as a slurry fuel, and then injected into the blast furnace vent, so that the powdered iron can be used as it is. Compared to the conventional method of recycling the powdered iron through agglomeration accompanied by the sintering process and the blast furnace blowing method of powdered iron is simpler and more efficient than the pulverized coal coal blowing, it is more effective in terms of recycling the powdered iron and waste lubricating oil.

Claims (1)

조정제되어 저융점 금소인 Pb 및 Zn이 각각 200rpm 이하로 함유된 폐윤활유에 50중량% 이하의 철분말을 혼합하여 슬러리를 제조한 다음, 이 슬러리 연료를 고로 풍구내로 통상의 취입랜스에 의해 분사하여 구성됨을 특징으로 하는 분말철의 고로취입방법.The slurry was prepared by mixing up to 50% by weight of iron powder with waste lubricant containing Pb and Zn, each of which was adjusted to a low melting point of 200 rpm or less, and then injected into the blast furnace blast furnace by a conventional blowing lance. Blast furnace blowing method of powder iron, characterized in that configured.
KR1019940040301A 1994-12-31 1994-12-31 Blowing method of powered metal KR970002117B1 (en)

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