KR101110252B1 - Sludge discharging method in pickling equipment for manufacturing orient electrical steel sheet - Google Patents

Sludge discharging method in pickling equipment for manufacturing orient electrical steel sheet Download PDF

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KR101110252B1
KR101110252B1 KR1020040113465A KR20040113465A KR101110252B1 KR 101110252 B1 KR101110252 B1 KR 101110252B1 KR 1020040113465 A KR1020040113465 A KR 1020040113465A KR 20040113465 A KR20040113465 A KR 20040113465A KR 101110252 B1 KR101110252 B1 KR 101110252B1
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sludge
specific gravity
steel sheet
electrical steel
discharge
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KR20060074660A (en
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박정동
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주식회사 포스코
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B45/00Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
    • B21B45/02Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for lubricating, cooling, or cleaning
    • B21B45/0269Cleaning
    • B21B45/0275Cleaning devices
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/36Regeneration of waste pickling liquors
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • C23G3/021Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously by dipping
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • C23G3/027Associated apparatus, e.g. for pretreating or after-treating

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

본 발명은 냉간압연전 표면이 미려한 전기강판을 생산하기 위해 예비소둔 및 숏블라스트(Shot Blaster) 처리된 표면을 염산으로 산세처리하는 과정에서 산용액속에 잔류한 실리카 슬러지(Silica Sludge)를 침전시켜 그 비중을 측정함으로써 이들이 굳어지기전 적정한 시점에서 원활히 배출될 수 있도록 제어하기 위해, 산세설비중 침전탱크의 하단 배출관로상에 설치된 감마레이를 이용한 비중측정기를 통해 침전된 슬러지의 비중이 1.55~1.70일 때 셧오프밸브를 개방함과 동시에 펌프를 구동시켜 배출처리토록 하고, 그 배출주기는 4~6시간으로 처리함으로써 미려한 표면을 갖는 방향성 전기강판을 제조할 수 있도록 하여 준다.The present invention precipitates silica sludge remaining in an acid solution in the course of pre-annealed and shot blasted (Shot Blaster) treated with hydrochloric acid in order to produce an electric steel sheet with a beautiful surface before cold rolling. The specific gravity of the sludge precipitated through the specific gravity meter using gamma ray installed on the lower discharge line of the sedimentation tank in the pickling tank was controlled to control the specific gravity to be discharged at the proper time before it solidified. When the shut-off valve is opened at the same time, the pump is driven to discharge treatment, and the discharge cycle is processed for 4 to 6 hours to produce a grain-oriented electrical steel sheet having a beautiful surface.

본 발명에 따르면 감마레이에 의해 측정된 SiO2 슬러지의 비중을 1.55 ~ 1.70에서 관리하고, 슬러지 배출주기를 4~6시간이 되도록 함으로써 배관 및 노즐의 막힘 문제를 해결하고, 표면품질을 확보하며, 유독물로부터 작업자를 보호하는 효과를 제공하게 된다.According to the present invention, the specific gravity of SiO 2 sludge measured by gamma ray is controlled at 1.55 to 1.70, and the sludge discharge cycle is 4 to 6 hours to solve the problem of clogging of pipes and nozzles and to secure surface quality. It provides the effect of protecting workers from toxics.

방향성, 전기강판, 산세탱크, 침전탱크, 비중측정기, 감마레이, 슬러지Directivity, electrical steel, pickling tank, sedimentation tank, specific gravity measuring instrument, gamma ray, sludge

Description

방향성 전기강판 제조용 산세설비에서 슬러지 배출방법{SLUDGE DISCHARGING METHOD IN PICKLING EQUIPMENT FOR MANUFACTURING ORIENT ELECTRICAL STEEL SHEET}SLUDGE DISCHARGING METHOD IN PICKLING EQUIPMENT FOR MANUFACTURING ORIENT ELECTRICAL STEEL SHEET}

도 1은 일반적인 방향성 전기강판 제조과정을 보인 공정도,1 is a process chart showing a general oriented electrical steel sheet manufacturing process,

도 2는 일반적인 제조과정을 거칠 때 염산순환탱크내에 SiO2가 침강되는 속도를 보인 그래프,Figure 2 is a graph showing the rate of precipitation of SiO 2 in the hydrochloric acid circulation tank during the general manufacturing process,

도 3 및 도 4는 본 발명을 설명하기 위한 장치의 구성 개요도.3 and 4 are schematic diagrams showing the configuration of an apparatus for explaining the present invention.

♧ 도면의 주요 부분에 대한 부호의 설명 ♧♧ description of the symbols for the main parts of the drawing ♧

10....침전탱크 12....비중측정기10..Sedimentation tank 12 ....

14....셧오프밸브 16....공업용수배관14 .... Shut-off valve 16 .... Industrial water piping

18....개폐밸브18 .... Open / close valve

본 발명은 냉간압연전 표면이 미려한 전기강판을 생산하기 위해 예비소둔 및 숏블라스트(Shot Blaster) 처리된 표면을 염산으로 산세처리하는 과정에서 산용액속에 잔류한 실리카 슬러지(Silica Sludge)를 침전시켜 그 비중을 측정함으로써 이 들이 굳어지기전 적정한 시점에서 원활히 배출될 수 있도록 제어하는 방향성 전기강판 제조용 산세설비에서 슬러지 배출방법에 관한 것이다.The present invention precipitates silica sludge remaining in an acid solution in the course of pre-annealed and shot blasted (Shot Blaster) treated with hydrochloric acid in order to produce an electric steel sheet with a beautiful surface before cold rolling. It relates to a sludge discharge method in pickling equipment for producing oriented electrical steel sheets that controls the specific gravity so that they can be discharged smoothly at an appropriate time before solidification.

주지된 바와 같이, 모터 및 변압기에 주로 사용되는 방향성 전기강판은 중량%로, C:0.046~0.058, Si:3.0~3.3, Mn:0.09~0.12, Cu:0.02, Sol-Al:0.027를 주요성분으로 하는 강판이다.As is well known, oriented electrical steel sheets mainly used in motors and transformers are in weight percent, with C: 0.046 to 0.058, Si: 3.0 to 3.3, Mn: 0.09 to 0.12, Cu: 0.02, and Sol-Al: 0.027. It is a steel plate made into.

이러한 방향성 전기강판은 도 1과 같이, 소재공급설비(1)로부터 강판(strip)이 공급된 후 예비소둔공정(2), 스케일제거공정(3), 산세공정(4) 및 권취공정(5)을 거쳐 제조된다.Such a grain-oriented electrical steel sheet is a pre-annealing step (2), descaling step (3), pickling step (4) and winding step (5) after the steel sheet (strip) is supplied from the material supply equipment (1) as shown in FIG. It is manufactured through.

이때, 열간압연된 소재중의 억제제(Inhibitor) 분포를 고르게 하기 위해 냉간압연전에 최고온도 1100℃의 가열대를 지나 900℃의 균열대에서 60초간 소둔과정을 거치게 된다.At this time, in order to evenly distribute the inhibitor (Inhibitor) in the hot-rolled material is subjected to an annealing process for 60 seconds in the crack zone of 900 ℃ past the heating zone of the maximum temperature 1100 ℃ before cold rolling.

소둔과정에서 열간압연시 580℃로 권취후 서서히 냉각하면서 강판표면에 치밀한 스케일층이 형성되게 되는데, 마그네타이트(Fe3O4)와 헤마타이트(Fe2O 3)가 주성분인 스케일층은 고온소둔 과정에서 위스타이트(FeO)로 환원되게 된다.By gradually cooling after coiling in the annealing process to 580 ℃ during hot rolling, there is presented a dense scale layer on the surface of the steel sheet form, magnetite (Fe 3 O 4) and hematite (Fe 2 O 3) is a main component of the scale layer has a high temperature annealing process Is reduced to Wistatite (FeO) at.

그리고, 소둔로 후단의 공냉대에서 750℃로 서냉된후 Water Spray를 통해 상온으로 급냉되게 되는데, 이때 급냉이 짧은시간에 이루어지므로 환원된 위스타이트(FeO)층은 대부분 상온까지 산화되지 않고 잔류하여 산세처리가 용이한 스케일층을 형성하게 되며, 이 위스타이트(FeO)층은 쉽게 박리되는 특징이 있어 강판과 스케일층과의 냉각속도 차이만으로도 박리가 일어나게 된다. In addition, after cooling to 750 ° C. in the air-cooling zone at the end of the annealing furnace, it is quenched to room temperature by water spray. At this time, since the quenching takes place in a short time, most of the reduced Wistatite (FeO) layer remains without oxidation to room temperature. The pickling layer forms a scale layer that is easy to pickle, and the Wistatite (FeO) layer is easily peeled off, and the peeling occurs only by a difference in cooling rate between the steel sheet and the scale layer.                         

소둔로를 지나 유리하게 형성된 스케일층을 냉간압연에 적합한 상태로 디스케일하기 위한 방법에는 두 가지가 있다.There are two ways to descale the scale layer advantageously past the annealing furnace into a state suitable for cold rolling.

그중 하나는 기계적인 방법으로 터빈에 의해 가속된 0.6mm 숏트볼(Shot Ball)을 강판표면에 분사하여 물리적으로 스케일을 제거하는 방법인데, 이때 스케일 제거는 터빈의 회전속도, 숏트볼의 투사량 등을 조절함으로써 표면조도 및 스케일 제거 정도를 감안하여 제어할 수 있다.One of them is the mechanical method of spraying the 0.6mm shot ball accelerated by the turbine on the surface of the steel sheet to physically remove the scale. In this case, the removal of the scale is the rotational speed of the turbine, the projected amount of the shot ball, etc. It can be controlled by adjusting the surface roughness and the degree of scale removal.

다른 하나는 화학적인 방법으로 18%의 염산을 철판과 반응이 이뤄지는 산세조에 공급하므로서 기계적인 방법으로 제거되지 않은 미세한 잔류 스케일들과 반응시켜 화학적으로 제거하는 것인데 그 대표적인 반응식은 아래와 같다.The other method is to chemically remove 18% of hydrochloric acid by chemically supplying the pickling tank which reacts with the iron plate and reacting with fine residual scales which have not been removed by mechanical method.

FeO + 2HCl → FeCl2 + H2O -------(1)FeO + 2HCl → FeCl 2 + H 2 O ------- (1)

우수한 자기적 성질을 얻기 위해 방향성 전기강판중에는 비저항 증가에 가장 유효한 합금성분인 Si 성분을 3% 정도 함유시켜, 철손이 낮고 자성이 양호한 제품을 생산할 수 있게 되는 장점이 있다.In order to obtain excellent magnetic properties, the grain-oriented electrical steel sheet contains about 3% of the Si component, which is the most effective alloy component for increasing the resistivity, and thus has the advantage of being able to produce a product having low iron loss and good magnetic properties.

반면에, 강중의 Si 성분은 염산과 산화층이 화학적 반응을 일으키는 중에 산용액중에 잔류하게 되어 산세설비에 슬러지 침적을 발생시키는 유해한 요소로 작용하게 된다.On the other hand, the Si component in the steel remains in the acid solution during the chemical reaction between the hydrochloric acid and the oxide layer, which acts as a detrimental factor for the sludge deposition in the pickling facility.

즉, 강중의 Si 성분중 일부는 표면산화층(Fe2O3, Fe3O4, FeO) 하부에 Fe2SiO4로 존재하게 되며, 상기 (1)식과 같이 염산과의 화학반응을 통해 산화층을 제거하는 과정에서 지철 상부에 위치한 Fe2SiO4층도 염산과 반응하게 된다. That is, some of the Si components in the steel are present as Fe 2 SiO 4 under the surface oxide layer (Fe 2 O 3 , Fe 3 O 4 , FeO), and the oxide layer is formed by chemical reaction with hydrochloric acid as shown in Equation (1). During the removal process, the Fe 2 SiO 4 layer on the top of the iron is also reacted with hydrochloric acid.

이때, 철분(Fe)은 염산과 반응하여 염화철(FeCl2,FeCl3)을 형성하지만, 화학적으로 안정된 SiO2 성분은 반응하지 않고 염산용액속에 잔류하게 된다.At this time, iron (Fe) reacts with hydrochloric acid to form iron chlorides (FeCl 2, FeCl 3 ), but the chemically stable SiO 2 component does not react and remains in the hydrochloric acid solution.

SiO2 성분은 입도범위가 0.3 ~ 100㎛로 염산용액이 순환되는 과정에서 시간의 경과에 따라 순환시스템 내에서 침전되고 굳어져 탱크내에 슬러지층을 형성하거나 배관막힘을 일으키게 되며, 각 탱크별 침강특성은 도 2에 그래프로 나타내었다.The SiO 2 component has a particle size range of 0.3 ~ 100㎛ and precipitates and solidifies in the circulation system as the hydrochloric acid solution circulates over time, forming a sludge layer in the tank or clogging the pipe. Is shown graphically in FIG. 2.

특히, 주기적인 정비나 설비문제로 인해 정지되었을 경우는 더욱 침전량이 많아지게 된다. 그러므로, 막힘문제를 예방하기 위해 순환 탱크내에 침적된 슬러지층은 2~3개월 마다 주기적인 청소로 제거하고 있다.In particular, when stopped due to periodic maintenance or equipment problems, the amount of precipitation is increased. Therefore, the sludge layer deposited in the circulation tank is removed by periodic cleaning every two to three months to prevent clogging problems.

뿐만 아니라, 산탱크내에는 인체에 유해한 고농도의 염산이 잔류하고 있어 작업자가 들어가 슬러지층을 제거하는 작업은 작업환경 개선면에서도 시급히 해소되야 할 작업이다.In addition, there is a high concentration of hydrochloric acid harmful to the human body in the acid tank, so the work to remove the sludge layer is to be urgently solved in terms of improving the working environment.

기존에도 염산 순환시스템중에 별도의 침전 탱크로 일정량의 산액을 순환시키며 침전 탱크내에 침강시킴으로 SiO2 제거를 도모하였으나, 순환탱크 내부의 SiO2 침적상태를 확인할 수 있는 방법이 없어 작업자의 경험에 의존하여 일정시간 마다 배출하고 있었다.In the existing hydrochloric acid circulation system, a separate settling tank circulated a certain amount of acid solution and settled in the settling tank to remove SiO 2 , but there was no way to check the SiO 2 deposition status in the circulating tank. It was discharged every time.

나아가, 슬러지 침적상태는 처리강종 및 라인상황에 따라 다르기 때문에 작업자의 경험에 의존하는 경우 시간이 너무 짧으면 과도한 묽은 슬러지 배출로 염산손실을 초래하고, 시간이 지나치게 길면 침강된 슬러지 성분이 굳어져 배출이 어렵게 되는 단점이 있었다. Furthermore, since the sludge deposition condition depends on the treated steel grade and line conditions, if the operator's experience is too short, excessive thin sludge discharge causes hydrochloric acid loss, and if the time is too long, the precipitated sludge component hardens and discharges. There was a disadvantage that became difficult.                         

침강법 외에 SiO2 제거방법으로 SRP, 원심분리, 마이크로필터를 이용하는 방법 등이 있으나 SRP 설비는 암모니아를 이용한 중화법을 사용하므로 지속적으로 18% 염산을 요구하는 산세설비에서는 적용이 불가능하고, 원심력을 이용한 원심분리방법, 마이크로필터를 이용하는 방법 등은 실적용에는 이르지 못하고 있는 실정이다.In addition to the sedimentation method, there are SRP, centrifugal separation, and micro-filter method for removing SiO 2 , but since SRP facility uses neutralization method using ammonia, it is not applicable to pickling facilities that require 18% hydrochloric acid. The centrifugal separation method, the method using a micro filter, etc. are not used for performance.

본 발명은 상술한 바와 같은 종래 기술이 갖는 한계점을 감안하여 이를 해결하고자 창출한 것으로, 침전탱크 하부에 감마레이를 설치하고, 침전탱크내의 비중 변화를 검출하여 시간에 따른 슬러지 침전상태를 운전실에서 확인하고, 일정한 값에 도달하면 후단에 있는 펌프를 기동하여 배출함으로써 작업자의 개입없이 온라인상에서 자동으로 슬러지를 배출처리하여 침적에 의한 배관 막힘현상을 방지하고, 주기적인 자동배출을 통해 슬러지 경화가 발생되지 않아 염산 사용빈도가 줄어들게 되어 비용이 절감되며, 설비의 유지, 보수 및 청소가 용이한 방향성 전기강판 제조용 산세설비에서 슬러지 배출방법을 제공함에 그 목적이 있다.The present invention was created to solve this in consideration of the limitations of the prior art as described above, by installing a gamma ray in the lower portion of the sedimentation tank, detecting the change in specific gravity in the sedimentation tank to check the sludge sedimentation state with time in the cab When reaching a certain value, the pump in the rear stage is started and discharged to automatically discharge the sludge online without operator's intervention to prevent the blockage of pipes due to deposition and to prevent sludge hardening through periodic automatic discharge. The purpose is to provide a sludge discharge method in the pickling equipment for producing oriented electrical steel sheet is easy to maintain, repair and clean the facility because the frequency of hydrochloric acid is reduced.

본 발명은 상기한 기술적 과제를 달성하기 위하여, 산세설비중 침전탱크의 하단 배출관로상에 설치된 감마레이를 발광하는 발광부및 감마레이를 수광하는 수광부로 이루어진 비중측정기를 통해 침전된 슬러지의 비중을 측정하고, 측정된 슬러지의 비중이 1.55~1.70일 때 상기 배출관로상에 마련된 셧오프밸브를 개방함과 동시에 펌프를 구동시켜 배출처리토록 하고, 슬러지의 배출주기는 4~6시간으로 제어하는 방향성 전기강판 제조용 산세설비에서 슬러지 배출방법을 제공함에 그 특징이 있다.In order to achieve the above technical problem, the specific gravity of the sludge precipitated through the specific gravity meter consisting of a light emitting unit for emitting a gamma ray and a light receiving unit for receiving a gamma ray installed in the bottom discharge pipe of the precipitation tank in the pickling facility When the measured sludge has a specific gravity of 1.55 to 1.70, the shutoff valve provided on the discharge line is opened and the pump is driven to discharge treatment, and the sludge discharge period is controlled to 4 to 6 hours. It is characterized by providing sludge discharge method in pickling equipment for manufacturing electrical steel sheet.

이하에서는, 첨부도면을 참고하여 본 발명을 보다 상세하게 설명하기로 한다.Hereinafter, the present invention will be described in more detail with reference to the accompanying drawings.

도 3 및 도 4는 본 발명을 설명하기 위한 장치 구성도이다.3 and 4 are device configuration diagrams for explaining the present invention.

도 3 내지 도 4에 도시된 바와 같이, 침전탱크(10)의 하단 배출관상에는 발광부(12a)와 수광부(12b)로 이루어진 비중측정기(12)가 설치되고, 그 직하방의 관로상에는 셧오프밸브(14)가 마련되며, 그 후단에는 공업용수배관(16)이 개폐밸브(18)의 개재하에 설치된다.As shown in Figure 3 to 4, the specific gravity measuring instrument 12 consisting of the light emitting portion 12a and the light receiving portion 12b is provided on the lower discharge pipe of the settling tank 10, the shut-off valve on the pipeline directly below 14 is provided, and the industrial water pipe 16 is provided under the opening / closing valve 18 at the rear end thereof.

아울러, 상기 공업용수배관(16)이 연결된 배출관의 최하단에는 배출펌프(P)가 설치된다.In addition, a discharge pump (P) is installed at the lower end of the discharge pipe connected to the industrial water pipe (16).

또한, 상기 비중측정기(12)는 감마레이를 사용함이 바람직하다.In addition, it is preferable that the specific gravity measuring device 12 uses gamma ray.

이러한 설비구성을 갖는 본 발명은 도 1의 예시와 같은 공정을 거쳐 방향성 전기강판을 제조하게 되는데, 이때 예비소둔후 숏트블라스트(Shot Blaster)에서 기계적인 스케일 제거를 하고난 뒤 표면에 잔류한 4.5㎛ 미만의 스케일층을 제거하기 위해 18%의 염산을 염산순환 탱크로 공급해 준다.According to the present invention having such an arrangement, a grain-oriented electrical steel sheet is manufactured through a process as illustrated in FIG. 1, in which the mechanical scale is removed from the shot blaster after preliminary annealing and 4.5 μm remains on the surface. 18% hydrochloric acid is fed to the hydrochloric acid circulation tank to remove less scale layers.

이 경우, 산용액은 순환 탱크내의 산세조에서 반응하고 SiO2를 다량 함유한 저농도의 회수된 산과 합해져 순환 탱크별로 8 ~ 15% 농도를 가지게 된다.In this case, the acid solution reacts in the pickling tank in the circulation tank and is combined with the low concentration of recovered acid containing a large amount of SiO 2 to have a concentration of 8 to 15% for each circulation tank.

이 과정에서, 반응하면서 발생되는 SiO2 침적물을 제거하기 위해 순환탱크에 서 SiO2 제거장치 쪽으로 별도의 순환라인을 형성하여 온라인(On-line)상에서 SiO2를 계속해서 제거할 수 있게 된다.In this process, in order to remove SiO 2 deposits generated during the reaction, a separate circulation line is formed from the circulation tank toward the SiO 2 removal device, thereby continuing to remove SiO 2 on-line.

그리고, SiO2 제거장치중에 일정한 침적시간을 확보할 수 있는 대용량의 침전 탱크에서는 SiO2 자체로도 비중차에 의해 침전제거할 수 있으나, 침전효과를 증진시키기 위해 침강제를 첨가하여 줌이 바람직하다.In addition, in a large sedimentation tank capable of securing a constant deposition time in the SiO 2 removal apparatus, SiO 2 itself can be precipitated by specific gravity difference, but it is preferable to add a settling agent to enhance the precipitation effect. .

상기 침강제는 용액형과 분말형으로 나누어질 수 있으며, 그 사용량에 있어 용액형은 10% 용액으로 희석하여 6.85ℓ/hr를, 분말형은 0.05% 용액으로 희석하여 8.22ℓ/hr를 투입하여 준다.The settling agent may be divided into a solution type and a powder type, in which the solution type is diluted with a 10% solution to 6.85ℓ / hr, and the powder type is diluted with a 0.05% solution to 8.22ℓ / hr give.

이때, 침강제의 효과는 60℃ 이하에서 가장 효과적이다.At this time, the effect of the settling agent is most effective at 60 ℃ or less.

그리하여, 침전탱크로 유입되는 SiO2 함유산액은 탱크내에서 오버플로우(Overflow) 라인을 통해 각 순환탱크로 회수될 때까지 충분한 침전시간을 가지고 바닥으로 침강하게 된다.Thus, the SiO 2 -containing acid solution flowing into the settling tank is settled to the bottom with sufficient settling time until recovered to each circulation tank through the overflow line in the tank.

침강된 SiO2는 하부의 셧오프밸브(Shut Off valve)(14) 상부로부터 쌓이게 되며, 이때 감마레이 비중측정기(12)를 통해 슬러지의 비중변화를 측정하게 된다.Precipitated SiO 2 is accumulated from the top of the shut-off valve (14) at the bottom, and the specific gravity change of the sludge is measured through the gamma ray specific gravity measuring instrument (12).

규정된 비중변화가 일어나면 슬러지를 배출하게 되는데, 이때 슬러지 배출후 공업용수배관(Industrial Water pipe)(16)을 통해 플러싱(Flushing) 함으로써 배출관내 잔류된 슬러지를 피트(Pit)까지 완전하게 밀어낼 수 있게 된다.When the specified specific gravity change occurs, sludge is discharged. At this time, after the sludge is discharged, the sludge remaining in the discharge pipe can be completely pushed out to the pit by flushing through the industrial water pipe 16. Will be.

따라서, 잔류물이 배출관로 상에서 경화되어 배출관을 폐쇄하는 것을 방지한 다.Thus, the residue is cured on the discharge duct to prevent closing the discharge duct.

특히, 셧오프밸브(14)의 직상방 위치에는 물이 일정부분 고여있게 하여 감마레이 비중측정기(12) 직후단부로부터 다음 슬러지 배출을 원활하게 하며 비중측정기(12)의 기능을 유지할 수 있도록 함이 더욱 바람직하다.Particularly, in the position immediately above the shutoff valve 14, water is accumulated to allow a certain portion of water to be discharged from the end immediately after the gamma ray specific gravity measuring instrument 12 and to maintain the function of the specific gravity measuring instrument 12. More preferred.

상술한 과정을 통해 슬러지를 배출할 때에 슬러지의 비중에 따른 가장 효율적인 배출을 달성해낼 수 있도록 하기한 표 1,2의 비교예들을 통해 감마레이 비중측정기(12)의 사용상 최적조건을 찾아 보았다.When the sludge is discharged through the above-described process, the optimum conditions for the use of the gamma ray specific gravity measuring instrument 12 are found through the comparative examples of Tables 1 and 2 below to achieve the most efficient discharge according to the specific gravity of the sludge.

이때, 감마레이 비중측정기(12)에 의해 검출된 측정비중 및 배출시간에 따라 변화하는 슬러지내의 염산농도, 잔류 Si, 염산소비량을 구분하여 그 결과를 표 1과 표 2에 나타내었다.At this time, the hydrochloric acid concentration, residual Si, and hydrochloric acid consumption in the sludge varying according to the measurement specific gravity and discharge time detected by the gamma ray specific gravity measuring instrument 12 are shown in Table 1 and Table 2.

또한, 판정조건은 배출주기에 따라 Si 제거설비에서 오버플로우되어 산세탱크로 회수되는 용액중의 잔류 Si 농도와 염산소비량으로 하여 가장 효과적인 조건을 찾고자 하였다. In addition, the determination condition was to find the most effective condition by the residual Si concentration and hydrochloric acid consumption in the solution overflowed in the Si removal equipment and recovered to the pickling tank according to the discharge cycle.                     

Figure 112004061845181-pat00001
Figure 112004061845181-pat00001

상기 표 1의 배출주기에 따른 결과를 보면, 비교예1의 경우 아직 비중이 낮고 묽어 염산소비량이 과다한 반면, 회수되는 염산용액중의 잔류 Si는 낮게 나타났다.In the results according to the discharge cycle of Table 1, in the case of Comparative Example 1, the specific gravity is still low and dilute, excessive consumption of hydrochloric acid, while the residual Si in the recovered hydrochloric acid solution was low.

그리고 비교예2는 8시간으로 주기를 늘렸을 때, 염산소비량이 약간 감소한 반면 잔류 Si가 급격히 증가하여 SiO2 제거효과가 미흡한 것으로 나타났다.In Comparative Example 2, when the cycle was increased to 8 hours, the hydrochloric acid consumption slightly decreased, but the residual Si rapidly increased, indicating that the SiO 2 removal effect was insufficient.

그러나, 발명예1은 배출주기를 4시간으로 한 경우로 잔류 Si는 낮은 상태로 유지하면서 염산소비량은 상당부분 감소하는 것을 보여 주었고, 발명예2는 주기를 6시간으로 늘렸을 경우로 잔류 Si는 약간 증가 하나, 염산소비량은 상당히 감소하였다.However, Inventive Example 1 showed that the discharge cycle was 4 hours, while the residual Si was kept low while reducing the amount of hydrochloric acid, while Inventive Example 2 was increased when the cycle was increased to 6 hours. Although slightly increased, the consumption of hydrochloric acid decreased considerably.

종래예는 비중측정기(12)가 없는 샘플을 채취하여 측정한 값으로 발명예에 비해 불량하게 나타났다.Conventional example is a value measured by taking a sample without the specific gravity measuring instrument 12, it was poor compared to the invention example.

결론적으로, 잔류 Si가 낮고, 염산소비량도 낮게 관리할 수 있는 발명예1,2 가 종래예 및 비교예1,2에 비해 양호한 것을 알 수 있었다.In conclusion, it was found that Inventive Examples 1 and 2, which can manage low residual Si and low hydrochloric acid consumption, are better than the conventional examples and Comparative Examples 1,2.

Figure 112004061845181-pat00002
Figure 112004061845181-pat00002

상기 표 2의 경우는 감마레이 측정 비중별로 측정을 한 것으로 비중값을 1.55이하로 할 경우 비교예1과 같이 염산소비량이 과다하게 증가되며, 비중값을 1.70 이상으로 할 경우는 잔류 Si가 급격히 증가하는 경향을 보여주고 있다.In the case of Table 2, when the specific gravity value is measured by the specific gravity of gamma ray, when the specific gravity value is 1.55 or less, the amount of hydrochloric acid is excessively increased as in Comparative Example 1, and when the specific gravity value is 1.70 or more, the residual Si increases rapidly. The trend is to

그러므로, 잔류 Si와 염산소비량이 바람직한 범위를 가지는 발명예1과 2가 적정조건이라고 판단할 수 있다.Therefore, it can be judged that Inventive Example 1 and 2 which have a preferable range of residual Si and hydrochloric acid consumption are suitable conditions.

이상에서 상세히 설명한 바와 같이, 본 발명에 따르면 감마레이에 의해 측정된 SiO2 슬러지의 비중을 1.55 ~ 1.70에서 관리하고, 슬러지 배출주기를 4~6시간이 되도록 함으로써 배관 및 노즐의 막힘 문제를 해결하고, 표면품질을 확보하며, 유독물로부터 작업자를 보호하는 효과를 제공하게 된다.As described in detail above, according to the present invention, the specific gravity of SiO 2 sludge measured by gamma ray is controlled at 1.55 to 1.70, and the sludge discharge cycle is 4 to 6 hours to solve the problem of clogging of pipes and nozzles. It ensures the surface quality and provides the effect of protecting workers from toxics.

Claims (2)

방향성 전기강판을 제조할 때에,When manufacturing oriented electrical steel sheet, 산세설비중 침전탱크의 하단 배출관로상에 설치된 감마레이를 발광하는 발광부 및 감마레이를 수광하는 수광부로 이루어진 비중측정기를 통해 침전된 슬러지의 비중을 측정하고, 측정된 슬러지의 비중이 1.55~1.70일 때 상기 배출관로상에 마련된 셧오프밸브를 개방함과 동시에 펌프를 구동시켜 배출처리토록 하고, 슬러지의 배출주기는 4~6시간으로 제어하는 것을 특징으로 하는 방향성 전기강판 제조용 산세설비에서 슬러지 배출방법.In the pickling facility, the specific gravity of the sludge deposited is measured by a specific gravity meter consisting of a light emitting part emitting a gamma ray and a light receiving part receiving a gamma ray installed on the lower discharge pipe of the sedimentation tank, and the measured specific gravity of the sludge is 1.55 to 1.70. Sludge discharge from pickling equipment for producing oriented electrical steel sheet, characterized in that to open the shut-off valve provided on the discharge pipe at the same time to drive the pump discharge treatment, the discharge cycle of the sludge is controlled 4 to 6 hours Way. 청구항 1에 있어서,The method according to claim 1, 상기 슬러지를 배출처리한 후에는 상기 배출관로상의 셧오프밸브 하부에 연통배관된 공업용수배관을 통해 공업용수를 이용하여 플러싱시키는 과정을 더 수행하는 것을 특징으로 하는 방향성 전기강판 제조용 산세설비에서 슬러지 배출방법.After the sludge is discharged, the sludge is discharged from the pickling facility for manufacturing a grain-oriented electrical steel sheet further comprising the step of flushing the industrial sludge using industrial water through an industrial water pipe connected to a lower portion of the shutoff valve on the discharge line. Way.
KR1020040113465A 2004-12-28 2004-12-28 Sludge discharging method in pickling equipment for manufacturing orient electrical steel sheet KR101110252B1 (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06158370A (en) * 1992-11-30 1994-06-07 Kawasaki Steel Corp Method and device for removing sludge in pickling vessel for stainless steel strip
JPH0790649A (en) * 1993-09-17 1995-04-04 Kawasaki Steel Corp Treatment of pickling solution
JPH1018068A (en) * 1996-07-05 1998-01-20 Kawasaki Steel Corp Method for removing sludge in stainless steel strip pickling tank, and stainless steel strip pickling equipment

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06158370A (en) * 1992-11-30 1994-06-07 Kawasaki Steel Corp Method and device for removing sludge in pickling vessel for stainless steel strip
JPH0790649A (en) * 1993-09-17 1995-04-04 Kawasaki Steel Corp Treatment of pickling solution
JPH1018068A (en) * 1996-07-05 1998-01-20 Kawasaki Steel Corp Method for removing sludge in stainless steel strip pickling tank, and stainless steel strip pickling equipment

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