KR100395135B1 - Cleaning method of ferritic stainless steel - Google Patents

Cleaning method of ferritic stainless steel Download PDF

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Publication number
KR100395135B1
KR100395135B1 KR10-1998-0062083A KR19980062083A KR100395135B1 KR 100395135 B1 KR100395135 B1 KR 100395135B1 KR 19980062083 A KR19980062083 A KR 19980062083A KR 100395135 B1 KR100395135 B1 KR 100395135B1
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pickling
stainless steel
acid
sulfuric acid
present
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KR10-1998-0062083A
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KR20000045524A (en
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류승기
하헌재
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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
    • 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
    • C23G1/08Iron or steel
    • C23G1/081Iron or steel solutions containing H2SO4
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D2211/00Microstructure comprising significant phases
    • C21D2211/005Ferrite

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

Abstract

본 발명은 18Cr계 스테인리스강의 청정 산세방법에 관한 것이며, 그 목적하는 바는종래의 산세방법이 혼산조(질산+불산)를 사용함으로써 NOx 발생으로 인한 환경오염과 과도한 소지금속 침식으로 인한 금속손실 및 재처리 비용의 소요를 피할 수 없었던 것에 대해, 본 발명에서는 혼산조를 생략함으로써, 근본적으로 이러한 문제를 방지할 뿐만 아니라, 금속 손실량을 줄임으로써, 금속 및 산회수 비용을 절감할 수 있는 페라이트계 스테인리스강의 산세방법을 제공하는데 있다.The present invention relates to a clean pickling method of 18Cr stainless steel, the purpose of the conventional pickling method is to use a mixed acid tank (nitric acid + hydrofluoric acid) due to environmental pollution due to NOx generation and metal loss due to excessive base metal erosion and While it was not possible to avoid the cost of reprocessing, in the present invention, by eliminating the mixed acid tank, the ferritic stainless steel which can fundamentally prevent such a problem and reduce the metal loss by reducing the amount of metal loss. To provide a method for pickling rivers.

상기 목적을 달성하기 위한 본 발명은 페라이트계 스테인리스강을 산세하는 방법에 있어서,The present invention for achieving the above object in the method of pickling ferritic stainless steel,

소둔 및 쇼트 블라스트(1) 처리를 거친 강판을 연삭 브러시(18)로 스케일의 일부를 제거한 다음, 황산(H2SO4)이 150~200g/ℓ이고, 산세를 촉진시키기 위한 질산철(Fe(NO3)3·9H2O)이 15~25g/ℓ로 조성되는 황산용액의 온도를 90~100℃로 하여 황산조만으로 산세하는 것을 특징으로 하는 폐라이트계 스테인리스강의 청정 산세방법에 관한 것을 그 요지로 한다.After the steel sheet subjected to the annealing and shot blasting (1) was removed with a grinding brush 18, a portion of the scale was removed, and then sulfuric acid (H 2 SO 4 ) was 150-200 g / l, and iron nitrate (Fe ( NO 3 ) The clean acid pickling method of waste-light stainless steel characterized by pickling with sulfuric acid bath only when the temperature of the sulfuric acid solution composed of 3 · 9H 2 O) is set to 90 to 100 ° C. Make a point.

Description

페라이트계 스테인리스강의 청정 산세방법Clean pickling method of ferritic stainless steel

본 발명은 18 Cr계 페라이트 스테인레스 열연강판의 산세방법에 관한 것으로서, 보다 상세하게는 종래의 스테인리스강의 산세방법에 있어서의 황산조와 혼산조로 이루어지는 복수의 산세조중 혼산조 처리를 생략하고 황산조 처리만 실시함으로써 비용을 절감하고 종래의 혼산조 처리에서 가장 문제가 된 NOx 발생 문제를 해결할 수 있는 폐라이트계 스테인레스 열연강판의 청정 산세방법에 관한 것이다.The present invention relates to a pickling method of an 18 Cr ferritic stainless hot rolled steel sheet, and more specifically, to a sulfuric acid bath treatment without omitting a mixed acid bath treatment of a plurality of pickling tanks consisting of a sulfuric acid tank and a mixed acid bath in a conventional method of pickling stainless steel. The present invention relates to a clean pickling method of a waste light stainless steel hot rolled steel sheet which can reduce costs and solve the NOx generation problem which is the most problematic in the conventional mixed acid treatment.

현재 사용하고 있는 연속소둔 산세라인의 작업공정을 도 1을 통하여 간략히설명하면 다음과 같다.The working process of the continuous annealing pickling line currently being used is briefly described with reference to FIG. 1 as follows.

열처리한 열연 소둔강판 표면의 치밀한 스케일은 화학적인 방법만 사용할 경우, 제거에 장시간을 요하기 때문에 쇼트 블래스터(Shot Blaster; 1)에서 지름 0.4mm 크기의 금속 구슬(Shot Ball)로 기계적 충격을 주어 스케일의 일부를 제거할 뿐만 아니라 잔존 스케일에 미세균열(Micro-Crack)을 형성시켜 이후 공정에서 산용액이 잘 침투하게 한다.The dense scale on the surface of heat-treated hot-rolled annealed steel sheet takes a long time to remove when chemical method is used. In addition to removing a portion of the micro-cracks on the residual scale (acid cracks) to allow the acid solution to penetrate well in subsequent processes.

대표적인 페라이트계 스테인리스강인 SUS430의 산세조건을 하기 표 1에 나타내었는데, 여기서 황산조(4)의 역할은 혼산조(6)에서 스케일의 제거가 용이하도록 기지와 스케일의 계면을 활성화시켜줄 뿐만 아니라 스케일의 일부를 제거시켜 준다.The pickling conditions of the representative ferritic stainless steel SUS430 are shown in Table 1 below, where the role of the sulfuric acid tank (4) not only activates the interface between the base and the scale to facilitate the removal of the scale in the mixed acid tank (6). Remove some.

[표 1]TABLE 1

또한, 혼산조(6)는 1번 및 2번 산세조들로 이루어져 있고, 혼산조의 역할은 황산조에서 제거되지 않은 잔류스케일을 완전히 제거시켜줄 뿐만 아니라 스테인fl스강의 표면에 보호피막을 형성시켜 주는 것이다.In addition, the mixed acid tank 6 is composed of pickling tanks 1 and 2, and the role of the mixed acid tank not only completely removes the residual scale not removed from the sulfuric acid tank, but also forms a protective film on the surface of the stainless steel plate. To give.

혼산조를 거쳐 강판은 브러쉬롤(8)과 세척기(9)를 통과한 다음 건조기(10)에서 표면의 수분을 완전히 제거하고 스킨패스롤(Skin Pass Roll; 11)에서 형상을 고르게 하여 권취기(13)에서 권취후 열연코일로서 제품 출하되거나 냉간압연을 위해냉연공장으로 보내진다.After passing through the mixing tank, the steel sheet passes through the brush roll 8 and the washing machine 9, and then completely removes water from the surface of the dryer 10, and evens the shape of the coil in the skin pass roll 11. After winding in 13), it is shipped as a hot rolled coil or sent to a cold rolling mill for cold rolling.

하지만, 상기와 같은 종래방법은 황산조보다 혼산조의 산세조건에 더 비중을 두어 혼산조에서 HF의 농도를 5∼10 g/ℓ로 , 금속 이온량을 최대 60g/ℓ로 관리함으로써 산세액 중에 금속이온 농도가 단시간에 급격히 증가함으로써 산의 활성이 떨어져, 산 수명을 단축할 뿐만 아니라 산 탱크와 열교환기 사이에 있는 배관(14)에 슬러지(주로 FeF3침전물)가 침전되어 배관 막힘을 일으켜 산 탱크(6)와 열교환기(15)사이에 산의 순환을 방해함으로써 산용액의 냉각능을 떨어뜨리며, 궁극적으로 배관을 완전히 막아버려 문제가 되고 있다.However, in the conventional method as described above, the concentration of HF in the mixed acid bath is more weighted than the sulfuric acid bath, so that the concentration of HF in the mixed acid bath is controlled to 5-10 g / l and the amount of metal ions up to 60 g / l. As the concentration of ions increases rapidly in a short time, the activity of the acid decreases, which not only shortens the acid life, but also sludge (primarily FeF 3 precipitate) precipitates in the pipe 14 between the acid tank and the heat exchanger, causing a blockage of the acid tank. Interfering with the circulation of acid between the 6 and the heat exchanger 15 reduces the cooling ability of the acid solution and ultimately blocks the piping completely.

이러한 문제점을 해결하기 위하여 본 발명자는 특허출원 1997-67750호에서 종래의 방법에 연삭 브러시와 혼산조의 질산 및 불산농도를 제어하는 것을 특징으로 하는 산세방법을 제안한 바 있다.In order to solve this problem, the present inventor has proposed a pickling method characterized in controlling the nitric acid and hydrofluoric acid concentration of the grinding brush and the mixed acid tank in the conventional method in the patent application 1997-67750.

그러나, 이러한 방법은 여전히 혼산조를 사용함으로써 NOx 발생을 근본적으로 해결할 수는 없었다.However, this method still could not fundamentally solve NOx generation by using a mixed acid bath.

본 발명은 상기 설명한 종래기술의 문제점을 해결하기 위하여 이루어진 것으로, NOx 발생에 의한 환경오염의 원인이 되는 혼산조를 사용하지 않고 황산조만을 사용하는 페라이트계 스테인리스강의 청정 산세방법을 제공함에 그 목적이 있다.The present invention has been made to solve the problems of the prior art described above, and an object thereof is to provide a clean pickling method for ferritic stainless steel using only sulfuric acid tanks without using a mixed acid tank that causes environmental pollution by NOx generation. have.

도 1은 일반적으로 사용되는 산세라인의 모식도;1 is a schematic diagram of a pickling line generally used;

도 2는 본 발명을 실시하기 위한 산세라인의 모식도이다.2 is a schematic diagram of a pickling line for carrying out the present invention.

<도면의 주요부분에 대한 부호의 설명><Description of the code | symbol about the principal part of drawing>

1:쇼트블래스터 2:브라이드롤 3:세척기 4:황산조1: Shot Blaster 2: Bride Roll 3: Washer 4: Sulfur Tank

5,9:세척기 6:혼산조 7:산스프레이 노즐 8:브러쉬롤5, 9: washing machine 6: mixed acid tank 7: acid spray nozzle 8: brush roll

10:건조기 11:스킨패스롤 13:권취기 14:배관 15:열교환기10: dryer 11: skin pass roll 13: winding machine 14: piping 15: heat exchanger

18:연마 브러쉬롤18: polishing brush roll

상기 목적을 달성하기 위한 본 발명의 청정 산세방법은 소둔 및 쇼트 블라스트 처리를 거친 강판을 연삭 브러시(18)로 스케일의 일부를 제거한 다음, 황산(H2SO4)이 150~200g/ℓ이고, 산세를 촉진시키기 위한 질산철(Fe(NO3)3·9H2O)이 15∼25g/ℓ로 조성되는 황산용액의 온도를 90~100℃로 하여 황산조만으로 산세하는 것을 특징으로 한다.In order to achieve the above object, the clean pickling method of the present invention removes a portion of the scale with a grinding brush 18 after annealing and shot blasting, and then sulfuric acid (H 2 SO 4 ) is 150 to 200 g / l, Iron nitrate (Fe (NO 3 ) 3 .9H 2 O) for promoting pickling is characterized in that pickling with only a sulfuric acid bath at a temperature of 90 to 100 ° C. for a sulfuric acid solution composed of 15 to 25 g / l.

이하에서는 양호한 실시예와 관련하여 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail with reference to preferred embodiments.

본 발명에서는 도 2 도시와 같이, 우선 소둔 및 쇼트 블래스터(Shot Blast; 1)를 거친 강판을 연삭 브러시(Brush) 등과 같은 연삭장치(18)를 이용하여 기계적으로 스케일의 일부를 제거한다.In the present invention, as shown in Fig. 2, first, a part of the scale is mechanically removed by using a grinding device 18 such as a grinding brush or the like on a steel sheet subjected to annealing and shot blast (Shot Blast) 1.

상기 연삭장치인 연삭 브러시(18)는 황산조(4)의 입측 전방에 설치된 것으로서, 상기 쇼트 블래스터(Shot Blast; 1)를 거친 강판 표면에 잔존하는 표면 스케일의 일부를 제거하기 위한 것이다.The grinding brush 18, which is the grinding device, is installed in front of the entrance side of the sulfuric acid tank 4 to remove a portion of the surface scale remaining on the surface of the steel sheet which has passed through the shot blaster (1).

즉, 연삭 브러시(18)는 통판하는 강판(S)의 상하부에 회전가능하도록 설치된 한 쌍의 브러시 롤에 의하여 강판 표면에 잔존하는 표면 스케일의 일부를 제거하는 것이다.That is, the grinding brush 18 removes a part of the surface scale which remain | survives on the steel plate surface by a pair of brush rolls rotatably installed in the upper and lower parts of the plate | plate steel plate S.

상기 연삭 브러시(18)의 작용에 의하여 일부 제거된 스케일 외에 잔존하는 스케일을 제거하기 위하여, 종래의 특허출원 제1997-67750호에 제안한 기술에서는 황산조 조건을 온도 90∼100℃, 농도를 120∼160g/ℓ, 혼산조 조건을 온도 40∼50℃, 질산농도를 100∼150g/ℓ, 불산농도를 1∼5g/ℓ로 하여 산세하였다.In order to remove the remaining scale in addition to the scale partially removed by the action of the grinding brush 18, in the technique proposed in the prior patent application No. 1997-67750, the sulfuric acid bath conditions the temperature 90 ~ 100 ℃, the concentration 120 ~ It was pickled at 160 g / l, mixed acid bath conditions at a temperature of 40 to 50 ° C, a nitric acid concentration of 100 to 150 g / l, and a hydrofluoric acid concentration of 1 to 5 g / l.

그러나 본 발명에서는 혼산조 사용으로 인한 NOx 발생을 근본적으로 없애기위하여, 혼산조를 사용하지 않고, 황산조(4)에서 혼산조 역할까지 동시에 수행할 수 있도록 결합수가 조성된 유수 질산철(Ferric Nitrate; Fe(NO3)3·9H2O)을 15∼25g/ℓ 첨가하여 기존의 산세 속도를 확보하도록 하였다.However, in the present invention, in order to fundamentally eliminate the generation of NOx due to the use of the mixed acid tank, without using the mixed acid tank, the combined flow of iron nitrate (Ferric Nitrate) in which the combined water composition can be performed simultaneously from the sulfuric acid tank (4) to the role of the mixed acid tank; 15-25 g / l of Fe (NO 3 ) 3 · 9H 2 O) was added to ensure the existing pickling rate.

상기 조건에서 질산철(Ferric Nitrate; Fe(NO3)3·9H2O)을 15g/ℓ이하나 25g/ℓ 이상으로 첨가하면 미산세가 발생하는 문제가 있다.Under the above conditions, ferric nitrate (Fe (NO 3 ) 3 .9H 2 O) is added in an amount of not more than 15 g / l but more than 25 g / l, which causes a problem of fine pickling.

또한, 본 발명에서는 황산조 온도를 90∼100℃, 농도를 150∼200g/ℓ로하여 산세 작업을 실시하는데, 이는 혼산조 대신에 황산조만으로 산세를 실시하므로 충분한 산세 작용이 발생하도록 농도를 종래 보다 높은 수치 범위로 한 것이다.In addition, in the present invention, the pickling operation is performed at a sulfuric acid tank temperature of 90 to 100 ° C and a concentration of 150 to 200 g / l. It is a higher numerical range.

상기의 방법으로 산세할 경우 라인속도는 30∼35mpm으로 종래와 같이 유지할 수 있다.When pickling in the above manner, the line speed can be maintained at 30 to 35mpm as in the prior art.

또한, 혼산조에서 불산에 의해 과도하게 소지금속이 침식되는 기존의 방법보다 용액에 녹아나는 금속량을 줄임으로써 산의 사용량을 줄일 수 있다.In addition, it is possible to reduce the amount of acid used by reducing the amount of metal dissolved in the solution than the conventional method in which the base metal is excessively eroded by hydrofluoric acid in the mixed acid bath.

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

[실시예]EXAMPLE

통상의 방법으로 열연 및 소둔한 SUS430 스테인리스 열연강판을 준비하여, 쇼트 블래스터 및 연삭 브러시(18)로 처리한 다음, 하기 표 2의 조건으로 산세하였다. 산세후의 산세성 및 산세로 인한 소지금속 손실량을 조사하였다. 산세성 평가는 완전산세(○), 백색도 불량(△), 미산세(×)로 나타내었다.A SUS430 stainless steel hot rolled steel sheet was hot-rolled and annealed by a conventional method, treated with a shot blaster and a grinding brush 18, and then pickled under the conditions shown in Table 2 below. After pickling, pickling and loss of base metal due to pickling were investigated. Pickling evaluation was shown as complete pickling (○), poor whiteness (△), and fine pickling (×).

[표 2]TABLE 2

상기 표2에 나타난 바와 같이 혼산조를 이용한 종래예(1,2)는 산세성은 확보되나, NOx발생으로 인해 환경오염이 발생하거나 또는 이를 방지하기 위한 재처리 비용이 소요되는 것이 불가피하다.As shown in Table 2, the prior art example (1, 2) using a mixed acid tank is secured pickling, it is inevitable that the environmental pollution occurs due to the NOx generation or a reprocessing cost to prevent it.

또한, 금속 손실량이 5.0∼7.5mg/㎠로 높아 용액중의 금속 및 산을 회수하기 위해서는 재처리 비용이 많이 소요된다.In addition, the metal loss amount is 5.0-7.5 mg / cm 2 and high, and the reprocessing cost is high in order to recover | recover the metal and acid in a solution.

그러나, 본 발명을 적용한 혼산조를 생략하고, 연삭 브러시(18)를 사용하여 기계적으로 스케일의 일부를 제거하고, Fe(NO3)3·9H2O를 사용하여 산세능을 향상시킨 발명예(1,2,3)에 의하면 산세성도 확보되면서, 금속 손실량도 2.2∼2.4mg/㎠으로 낮아, 종래의 산세방법 보다 훨씬 비용을 절감할 수 있다.However, an invention example in which a mixed acid tank to which the present invention is applied is omitted, a portion of the scale is mechanically removed using the grinding brush 18, and the pickling capacity is improved using Fe (NO 3 ) 3 .9H 2 O ( According to 1,2,3), while the pickling property is also secured, the metal loss amount is also low at 2.2 to 2.4 mg / cm 2, which can reduce the cost much more than the conventional pickling method.

한편, 비교예1은 질산철(Ferric Nitrate; Fe(NO3)3·9H2O)은 첨가하지 않고연삭 브러시(18)만 사용한 예로 미산세가 발생했으며, 비교예2에서와 같이 Fe(NO3)3·9H2O를 10g/ℓ 이하로 첨가하였을 때는 산세성은 어느 정도 확보되나 백색도가 70 이하로 낮게 나타났다. 또한, Fe(NO3)3·9H2O을 30g/ℓ이상 첨가한 비교예3도 백색도가 70 이하로 나타났다. 여기서, Fe(NO3)3·9H2O가 산세성을 촉진시키는 기구는 하기 식 1에서 설명될 수 있다.On the other hand, in Comparative Example 1 is an example of using the grinding brush 18 without the addition of ferric nitrate (Fe (NO 3 ) 3 · 9H 2 O), the fine pickling occurred, as in Comparative Example 2 Fe (NO 3 ) When 3 · 9H 2 O was added below 10 g / l, the pickling property was secured to some extent, but the whiteness was lower than 70. Also, Comparative Example 3 in which Fe (NO 3 ) 3 .9H 2 O was added 30 g / L or more also showed a whiteness of 70 or less. Here, the mechanism by which Fe (NO3) 3.9H2O promotes pickling property can be described in Equation 1 below.

Fe(NO3)3·9H2O → Fe3++ 3NO3 -+ 9H2O ------- (1) Fe (NO 3) 3 · 9H 2 O → Fe 3+ + 3NO 3+ 9H 2 O ------- (1)

위 반응식에서 Fe3+이온은 첨가량이 증가함에 따라 산세를 촉진하는 성질이 있다. NO3-(니트로기) 이온은 농도가 증가함에 따라 산세성을 촉진하다가 어느 농도 이상이 되면 오히려 산세를 방해하는 성질이 있다. 이것은 니트로기가 스테인리스강 표면에 보호피막을 형성하여 산이 소지금속과 반응하는 것을 방해하기 때문이다.In the above scheme, Fe 3+ ions have the property of promoting pickling as the amount added increases. NO 3- (nitro group) ion promotes pickling as the concentration increases, but when the concentration is higher than a certain property to interfere with the pickling. This is because the nitro group forms a protective film on the surface of the stainless steel, preventing the acid from reacting with the base metal.

즉, 비교예2에서는 질산철(Ferric Nitrate; Fe(NO3)3·9H2O)의 첨가량이 너무 적어 산세 촉진제로서 역할을 수행하지 못하였으며, 비교예3에서는 첨가량이 너무 많아 Fe3+의 산세 활성화능 보다 니트로기의 산세 방해능이 더 크게 작용하여 완전한 산세성을 확보하지 못했다.That is, in Comparative Example 2, the amount of ferric nitrate (Fe (NO 3 ) 3 .9H 2 O) was too small to act as an acid pickling accelerator, and in Comparative Example 3, the amount of Fe 3+ was too high. The pickling disturbance of the nitro group was greater than the pickling activating capacity, thus preventing complete pickling.

따라서, 본 발명에서의 질산철(Ferric Nitrate; Fe(NO3)3·9H2O)의 농도 범위는 15∼25g/ℓ로 제한한다.Therefore, the concentration range of ferric nitrate (Fe (NO 3 ) 3 .9H 2 O) in the present invention is limited to 15-25 g / l.

상술한 바와 같이, 본 발명에 의하면 18Cr계 스테인리스강의 열연 산세시, 종래의 혼산조를 생략함으로써 NOx 발생에 의한 환경오염과 혼산조 사용에 따른 과도한 금속 손실을 방지할 뿐만 아니라 근본적으로 산의 사용을 절감하여 비용절감을 도모할 수 있다.As described above, according to the present invention, in the case of hot-rolled pickling of 18Cr stainless steel, the conventional mixing tank is omitted to prevent environmental pollution due to the generation of NOx and excessive metal loss due to the use of the mixing tank, as well as essentially the use of acid. The cost can be reduced by saving.

Claims (1)

페라이트계 스테인리스강을 산세하는 방법에 있어서,In the method of pickling ferritic stainless steel, 소둔 및 쇼트 블라스트(1) 처리를 거친 강판을 연삭 브러시(18)로 스케일의 일부를 제거한 다음, 황산(H2SO4)이 150~200g/ℓ이고 산세를 촉진시키기 위한 질산철(Fe(NO3)3·9H2O)이 15∼25g/ℓ로 조성되는 황산용액의 온도를 90∼100℃로 하여 황산조만으로 산세하는 것을 특징으로 하는 폐라이트계 스테인리스강의 청정 산세방법.After the steel sheet subjected to the annealing and shot blasting (1) was removed with a grinding brush 18, a part of the scale was removed, and then sulfuric acid (H 2 SO 4 ) was 150-200 g / l and iron nitrate (Fe (NO) was used to promote pickling. 3 ) Clean acid pickling method for waste light stainless steel characterized by pickling only with sulfuric acid bath at the temperature of sulfuric acid solution having 3 · 9H 2 O) of 15 to 25 g / l at 90 to 100 ° C.
KR10-1998-0062083A 1998-12-30 1998-12-30 Cleaning method of ferritic stainless steel KR100395135B1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012093372A3 (en) * 2011-01-05 2012-12-13 Ecolab Usa Inc. Aqueous acid cleaning, corrosion and stain inhibiting compositions in the vapor phase comprising a blend of nitric and sulfuric acid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012093372A3 (en) * 2011-01-05 2012-12-13 Ecolab Usa Inc. Aqueous acid cleaning, corrosion and stain inhibiting compositions in the vapor phase comprising a blend of nitric and sulfuric acid
US8618037B2 (en) 2011-01-05 2013-12-31 Ecolab Usa Inc. Aqueous acid cleaning, corrosion and stain inhibiting compositions in the vapor phase comprising a blend of nitric and sulfuric acid

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