KR810000367B1 - Method for manufacturing descaling agents for stainless steel - Google Patents

Method for manufacturing descaling agents for stainless steel Download PDF

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KR810000367B1
KR810000367B1 KR770003065A KR770003065A KR810000367B1 KR 810000367 B1 KR810000367 B1 KR 810000367B1 KR 770003065 A KR770003065 A KR 770003065A KR 770003065 A KR770003065 A KR 770003065A KR 810000367 B1 KR810000367 B1 KR 810000367B1
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acid
solution
stainless steel
water
manufacturing
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쇼오이찌 와다나베
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쇼오이찌 와다나베
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Abstract

The manufacturing process of the scale remover of stainless steel is as follows: process of blending agents with one or more than two species of the group composed of water, hydrolic acid, nitric acid, etc., the process of making a solution by adding and dissolving one or more species of soluble Mg salt stable in acid in the above solution, the process of manufacturing a viscous material by blending and leaving the mixed solution produced through the above process viscous, and making the viscous material dilute by adding the liquid agents to one or two kinds of the group of water, nitric acid and fluoric acid.

Description

스텐레스 강의 스케일 제거제의 제조법Preparation method of descaling agent of stainless steel

본 발명은 스텐레스강의 스케일 제거제의 제조법에 관한 것이다.The present invention relates to a method for producing a descaling agent of stainless steel.

종래부터 스텐레스강의 용도는 극히 광범위하여서 해마다 그 사용량은 증대하는 경향에 있으나, 스텐레스강재에 열처리 또는 용접가공을 실시할때에 발생하는 스케일, 산화막 등의 오손물의 제거, 혹은 스텐레스강재의 보일러, 탱크등의 외면에 세척에는 아직도 이상적인 것이 발명되지 않아서 극히 불충분하고 결점이 많은 처리법이 실시되어 있었던 것에 불과하였다.Conventionally, the usage of stainless steel is extremely wide, and its usage tends to increase year by year. However, it is possible to remove scales, oxides, etc. that occur when heat treatment or welding processing is performed on stainless steel, or stainless steel boilers, tanks, etc. On the outside, still no ideal for cleaning was invented, which was an extremely inadequate and flawed treatment.

이 실정에 비추어 본 발명자는 일본국 특허공보 소 49-37010호(이하 기본발명이라 약칭한다)에 기재된 발명을 개발하였으나, 그 발명의 구성요지는 그 명세서의 특허청구의 범위에 기재한 바와 같으며, 이것을 구성요건으로 분석하면 다음의 제1-3공정의 순차 결합에 의하여 이루어진 것이라고 말할 수 있다.In view of this situation, the present inventor has developed the invention described in Japanese Patent Publication No. 49-37010 (hereinafter abbreviated as basic invention), but the elements of the invention are as described in the claims of the specification. Analyzing this as a configuration requirement, it can be said that it is achieved by the sequential combination of the following 1-3 steps.

[제1공정][Step 1]

질산, 불산에 수산, 물을 가한 혼화액에 아크릴 아마이드 중합물, 또는 내산성의 계면활성제를 혼입하고, 교반하며 이때 발생하는 열을 방냉(放冷)하여 원액을 만든다.An acrylamide polymer or an acid resistant surfactant is mixed with a mixed solution of nitric acid, hydrofluoric acid, and water, and stirred to cool the resulting heat to form a stock solution.

[제2공정][Step 2]

마그네슘 염류의 1종 또는 수종의 혼합재에 원액을 주입교반하여 점결성 물질을 만든다.The caking is prepared by injecting and stirring the stock solution into one or several mixtures of magnesium salts.

[제3공정][Step 3]

점결성 물질에 원액을 가하여 냉각하고 점도를 cps(20℃)200-300쯤으로 조정한다.Cool the solution by adding the stock solution to the caking material and adjust the viscosity to about 200-300 cps.

그러나 이러한 상기한 기본발명의 제조법에도 하기와 같은 문제점이 있다.However, the above-described manufacturing method of the present invention has the following problems.

즉,In other words,

a) 냉각조작이 2회 필요하므로 대량생산에 있어서 작업시간의 손실이 크며, 특히 점도를 200-300cps로 하기 위한 방치시간이 48시간부터 60시간에 이르른다.a) Since the cooling operation is required twice, the loss of working time in mass production is large, especially the leaving time for setting the viscosity to 200-300 cps ranges from 48 hours to 60 hours.

b) 점결성 물질의 점도(60000cps이상)가 과도하게 높은점과 그 물질은 균일성이 없고 유연한 고형물이 혼재하여서 원액에 의한 희석의 작업성은 매우 불량하다.b) The viscosity of caking substances (over 60000 cps) is too high and the materials are not uniform and mixed with flexible solids.

c) 실시예(Ⅲ)에서 볼 수 있는 바와같이, 원액에 탄산마그네슘을 가할 때, 탄산가스가 발생하기 때문에 작업능률이 나쁘게되고 안전면에서도 주의를 요한다.c) As can be seen in Example (III), when magnesium carbonate is added to the stock solution, carbonic acid gas is generated, resulting in poor work efficiency and attention in terms of safety.

본 발명은 상술한 바와같이 기본발명에 내재하고 있었던 결점을 기본적으로 그 발명방법의 각 공정의 결합순서를 변경하는 것에 의하여 일거에 해소하는 것으로서 기술적 효과도 비약적으로 증대한 스텐레스강의 스케일 제거제의 제조법을 제공하는 것을 목적으로 한다.The present invention solves the defects inherent in the basic invention as described above by basically changing the bonding order of the respective steps of the method of the present invention. It aims to provide.

즉 본 발명 제조법은 기본적으로는 다음의 4개 공정의 순차 결합으로부터 이루어지는 것이다.That is, the manufacturing method of this invention consists essentially of the sequential bonding of the following four processes.

[제1공정][Step 1]

물, 염산, 질산, 황산, 인산, 취산, 지오그리콜산으로부터 이루어지는 군에서 선택된 1 또는 2이상을 혼화하는 공정.A step of admixing one or two or more selected from the group consisting of water, hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, vulcanized acid and geoglycolic acid.

[제2공정][Step 2]

다음에 제1공정에서 얻어지는 액에 가용성이며, 산에 안정된 마그네슘염의 1종 또는 3종이상을 첨가 용해시켜서 용액으로 하는 공정.Next, a step of dissolving one kind or three or more kinds of magnesium salts which are soluble in a solution obtained in the first step and stable in an acid to form a solution.

[제3공정][Step 3]

제2공정에서 얻어지는 용액에 불산 혹은 불화암모늄, 혹은 그 수용액 및 아크릴계 중합물과 내산성의 계면활성제를 가하여 혼합액으로 하는 공정.A step of adding a hydrofluoric acid or ammonium fluoride, an aqueous solution thereof, an acrylic polymer and an acid resistant surfactant to a solution obtained in the second step to form a mixed solution.

[제4공정][Step 4]

제3공정에서 얻어지는 혼합액을 30-60분간 교반한 후 1-10시간 방치하여 점성물로 하는 공정.A step in which the mixed liquid obtained in the third step is stirred for 30 to 60 minutes and then left for 1 to 10 hours to form a viscous substance.

상기 제4공정에서 최종적으로 얻어진 점성물의 점도는 약 300-3000(cps)이다.The viscosity of the viscosities finally obtained in the fourth step is about 300-3000 (cps).

이 점성물을 그대로 희석해서 사용할 수도 있고, 또는 물, 질산, 불산으로부터 이루어지는 군에서 선택된 1종 또는 2종이상의 액체를 가해서 희석해서 점도를 약 300-600(cps)로 조절하여 사용할 수도 있다.The viscous substance may be diluted and used as it is, or it may be diluted by adding one or two or more liquids selected from the group consisting of water, nitric acid and hydrofluoric acid to adjust the viscosity to about 300-600 (cps).

상술한 본 발명 스텐레스강의 스케일 제거제의 제조법에 있어서 먼저 첫째로 사용하는 산의 성분은 스텐레스강의 표면, 강에 첨가하는 금속의 종류(예컨대 크롬, 니켈, 텅스텐, 동 등)에 따라 다종 다양하게 사용하며, 첨가하는 금속의 강에의 배합비 및 강의 두께도 다양하므로 용접등에 의하여 생성하는 스케일도 필연적으로 그 성상(性狀)이 다른 것인것에 비추어, 그 제거처리에 필요한 산도 불산을 기본으로 하여 이것에 결합시키는 산의 종류도, 질산, 염산, 황산, 인산, 취산, 지오그리콜산으로서 다종다양하게 사용하는 것인바, 총산의 량은 5-35%의 범위가 양호하다. (산은 모두 100%로 환산하여 합계한다) 다음에 가용성이며, 산에 안정한 마그네슘 염으로서 들 수 있는 것으로는 황산마그네슘, 염화마그네슘, 취화마그네슘, 인산마그네슘 등이 있으며, 마그네슘염류의 총량은 10-30%의 범위이다.In the manufacturing method of the above-described descaling agent of stainless steel of the present invention, first, the acid component used is variously used depending on the surface of stainless steel and the type of metal added to the steel (eg chromium, nickel, tungsten, copper, etc.). Since the mixing ratio of the metal to be added to the steel and the thickness of the steel are also varied, the scale produced by welding, etc., inevitably has different properties, and is bonded to this based on the acidity hydrofluoric acid required for the removal treatment. The type of acid to be used is also variously used as nitric acid, hydrochloric acid, sulfuric acid, phosphoric acid, quenching acid, and geoglycolic acid, and the amount of total acid is preferably in the range of 5-35%. (All acids are added and converted to 100%.) Next, soluble, acid-stable magnesium salts include magnesium sulfate, magnesium chloride, magnesium embrittlement, and magnesium phosphate, and the total amount of magnesium salts is 10-30. Range of%.

(마그네슘염은 모두 무수염으로 환산하여 합계한다)(All magnesium salts are added in anhydrous salts)

또 아크릴계 중합물에 대하여 설명하면, 불산과 마그네슘 이온등에 의하여 형성되는 점성 코로이드는 시간이 지남에 따라 혹은 교반에 의하여 점도저하를 일으키는 경향이 보임으로 점도유지의 관점에서 코로이드성의 보강이 필요하며, 아크릴계 중합물은 다음의 조건을 만족시키지 않으면 안된다.In addition, when explaining the acrylic polymer, viscous colloids formed by hydrofluoric acid and magnesium ions are required to reinforce the colloidal properties from the viewpoint of viscosity, since the viscosity decreases over time or by stirring. The acrylic polymer must satisfy the following conditions.

즉,In other words,

(ㄱ) 산액중에서 코로이드가 파괴되어 분리 침전을 일으키지 않는다.(A) The colloid is destroyed in the acid solution and does not cause sedimentation.

(ㄴ) 산액에 될 수 있는한 쉽게 용해되고 또한 부유물을 남기지 않는다.(B) dissolves as easily as possible in the acid solution and also does not leave a float.

(ㄷ) 염가로 입수하기 쉬운 경제성의 특징(C) Economic features that are easy to obtain at a low cost

이 (ㄱ)-(ㄷ)의 조건을 충족하는 것으로서 아크릴산 메타아크릴산 중합물 아크릴산 아마이드, 메타아크릴산 아마이드 중합물, 아크릴산 에스텔, 메타아크릴산 에스텔 중합물 및 이들 아크릴산계의 공중합물이 있으며, 이들 아크릴산계 중합물의 배합에 의하여 제조에 있어서 점결작용 속도의 조정에 유효하고, 또 제품에 있어서는 점도의 안정화에 유효하다.As satisfying the conditions of (a)-(c), there are acrylic acid methacrylate acrylic acid acrylate, methacrylic acid amide polymer, acrylic acid ester, methacrylic acid ester polymer and copolymers of these acrylic acid-based polymers. It is effective for adjustment of a caking effect in manufacture, and also for stabilization of a viscosity in a product.

이 아크릴산 중합물의 배합량은 수지분 100%로 환산하여 0.05-1.0%이다.The compounding quantity of this acrylic acid polymer is 0.05-1.0% in conversion of 100% of resin.

또한 내산성 계면활성제에 대하여 설명하면 사용할때에 있어서 스텐레스강의 스케일면에 부착하고 있는 유분의 제거 및 유막에의 침투를 양호하게 하며, 스케일면과 제품과의 밀착을 충분히 하여서 제품의 작용을 완전하게 하며, 그리고 최종적으로 행하는 수세의 완성을 위하여 배합하는 것으로서 최근의 계면 활성제에 의한 공해를 방지하는 입장에서 독성이 적은 것을 선택할 필요가 있으므로, 폴리옥시 에치렌 알킬페놀 에텔계중에서 옥시에치렌의 수가 12이상의 것을 사용함이 양호하다.In addition, when the acid-resistant surfactant is described, it is possible to remove oil adhering to the scale surface of stainless steel and to penetrate into the oil film when using it. In addition, since it is necessary to select the one which is less toxic from the standpoint of preventing the pollution by the recent surfactant, it is necessary to select the number of oxyethylenes in the polyoxyethylene alkylphenol ether system to be 12 or more. It is good to use it.

(이와 관련하여 옥시에치렌의 수가 12이하의 것은 산액중에서 시간이 지남에 따라 분리되기 쉽다)(In this connection, the number of oxyethylenes of 12 or less is likely to separate in the acid solution over time.)

이 내산성 계면활성제 배합량은 0.05-2.0%이다.This acid resistant surfactant compounding quantity is 0.05-2.0%.

이하 본 발명의 실시예를 표시한다.Examples of the present invention are shown below.

[실시예 1]Example 1

물 30g, 질산(67%) 18.5㎏을 교반하면서 혼화하고, 황산마그네슘(7수염) 35㎏을 가하여 용해해서, 불산(55%) 15㎏ 아크릴계 중합물 0.5㎏, 내산성 계면활성제 1㎏을 순차로 가하여 30-60분 교반을 계속한후 10시간 이상 방치하였다.30 g of water and 18.5 kg of nitric acid (67%) were mixed with stirring, 35 kg of magnesium sulfate (7 hydrochloride) was added and dissolved, and 0.5 kg of hydrofluoric acid (55%) and 0.5 kg of acrylic polymer and 1 kg of acid resistant surfactant were sequentially added. The stirring was continued for 30 to 60 minutes and then left for at least 10 hours.

본품을 그대로 제품화하거나 물 혹은 물, 질산(67%), 불산(55%)을 10 : 7 : 3의 비례로서 혼합한 혼액을 5-10㎏ 가하여 제품으로 하였다.Product was produced as it is, or 5-10 kg of a mixture of water or water, nitric acid (67%) and hydrofluoric acid (55%) in a proportion of 10: 7: 3 was added to the product.

상술한 제조법에 의하여 제조된 도포제 50㎏를 피세정 표면적(17.5㎠)의 청주저장용 탱크의 스케일 부착면 및 탱크내면의 불순물 제거를 위하여 솔로서 도포하고, 도포 완료 후, 약 60분 방치하여 수세를 행하였다.50 kg of the coating agent prepared according to the above-described manufacturing method is applied as a brush to remove impurities from the scale-attachment surface and the tank inner surface of the sake storage tank having the surface area to be cleaned (17.5cm2), and after application is complete, it is left to stand for about 60 minutes to wash with water. Was performed.

그 결과 탱크의 제조공정중에 용접에 의해 발생된 열영향부는 당연한 것이지만, 그라인더에 의한 연마작업중에 부착한 불순물도 완전히 제거되어 광택이 있고 얼룩지지 않은 표면으로 가공되었다.As a result, the heat affected zone generated by welding during the manufacturing process of the tank is natural, but impurities adhered during the grinding operation by the grinder were completely removed and processed to a glossy and unstained surface.

이것은 도포한 약제가 흐르거나, 밀리지 않아서 스텐레스강 세정의 목적인 부동태화처리(不動態化處理)까지도 아울러 행하게 된 것이어서, 세정의 목적을 달성한 것이다.This is because the applied chemicals do not flow or are pushed, and the passivation treatment, which is the purpose of cleaning stainless steel, is also performed, thereby achieving the purpose of cleaning.

또한 탱크재질은 sus304, 판 3㎜이다.The tank material is sus304 and plate 3 mm.

[실시예 2]Example 2

물 37㎏, 질산(67%) 22.5㎏을 교반하면서 혼화하고, 염화마그네슘(6수염) 25㎏을 가하여 용해하고, 다음에 내산성 계면활성제 1.5㎏, 아크릴계 중합물 0.5㎏, 불산(55%) 14㎏을 순차 혼합을 확인하면서 가하여, 30-60분 교반을 계속한 후, 본품을 그대로 제품화하거나 물 또는 30% 황산을 5㎏ 가하여서 제품으로 하였다.37 kg of water and 22.5 kg of nitric acid (67%) were mixed with stirring, 25 kg of magnesium chloride (hexahydrate) was added and dissolved, followed by 1.5 kg of acid-resistant surfactant, 0.5 kg of acrylic polymer, and 14 kg of hydrofluoric acid (55%). Was added while checking the mixing sequentially, and the stirring was continued for 30-60 minutes, and then the product was commercialized as it was, or 5 kg of water or 30% sulfuric acid was added to make the product.

응력제거의 필요에서 소둔처리한 송풍기의 스텐레스강의 표면에 시판하는 약제를 도포 사용하는 경우에는 통상 2-3회의 도포를 반복하지 않으면 진한 흑색으로 소둔된 스케일은 제거되지 않는 것인바, 상술한 바에 의하여 제조한 본제 사용에 의하여 1회의 도포후 약 15분 경과하였을 때에 약 80%의 스케일이 제거되며, 약 40분간 고압수분사에 의한 세정을 행하면 스텐레스강의 표면이 나타나서 세정의 목적이 달성된다.In the case of using a commercially available chemical agent on the surface of the stainless steel of the annealing blower in order to eliminate the stress, the scale which is darkly annealed is not removed unless the application is repeated 2-3 times. By using the prepared agent, about 80% of scale is removed when about 15 minutes have elapsed after one application. When cleaning by high pressure water spray is performed for about 40 minutes, the surface of stainless steel appears and the purpose of cleaning is achieved.

또한 스텐레스강의 재질은 316, 판두께는 6㎜이다.In addition, the material of stainless steel is 316, and the plate thickness is 6 mm.

[실시예 3]Example 3

물 35㎏, 질산 21㎏, 수산 1㎏을 교반하면서 혼화하고, 황산마그네슘(7수염) 20㎏, 염화마그네슘(6수염) 7.5㎏을 가하여 용해해서, 다음에 내산성 계면활성제 1㎏, 아크릴계 중합물 0.5㎏ 및 불산(55%) 14㎏을 순차 혼화됨을 확인하면서 첨가하였다.35 kg of water, 21 kg of nitric acid, and 1 kg of oxalic acid were mixed with stirring, 20 kg of magnesium sulfate (7 hydrate) and 7.5 kg of magnesium chloride (hexahydrate) were added and dissolved, followed by dissolving 1 kg of acid-resistant surfactant and 0.5 of an acrylic polymer 0.5. Kg and 14 kg of hydrofluoric acid (55%) were added while confirming that they were mixed sequentially.

약 30-60분 교반을 계속한 후, 7시간 이상 방치한 본품을 그대로 제품화하거나, 물 또는 20% 초산 5-10㎏을 첨가하여 제품으로 하였다.After continuing stirring for about 30-60 minutes, this product left to stand for 7 hours or more was commercialized as it was, or it was made into the product by adding 5-10 kg of water or 20% acetic acid.

상술한 바에 의해 제조된 도포제를 모 양주회사의 기설배관의 용접면(스텐레스강)에 부분적으로 도포하The coating agent prepared as described above is partially applied to the welding surface (stainless steel) of the existing pipe of the liquor company.

(4p 누락)(4p missing)

이프) 8600개의 관판면에 스프레이 취부도포하고 약 2시간 방치한 후 고압수세를 행하였다.If) 8600 tube plates are spray-coated and left for about 2 hours, high pressure washing is performed.

본기는 내해수용으로 특별 제조된 것으로서 그 화학성분 때문에 스케일의 제거는 아주 극히 곤란한 것으로 되어 있으나, 본제로는 목적은 달성되었다.This machine is specially manufactured for seawater, and because of its chemical composition, it is very difficult to remove scale, but the purpose has been achieved.

[실시예 8]Example 8

물 49.5㎏에 질산마그네슘(6수염) 20㎏, 황산마그네슘(7수염) 15㎏을 교반하면서 첨가하여 용해하고, 다음에 아크릴계 중합물 0.5㎏ 내산성 계면활성제 1㎏ 및 불산(55%) 14㎏을 순차로 혼화 확인하면서 첨가하여 이후 30분 교반하여 10시간 이상 방치하여 제품으로 하였다.20 kg of magnesium nitrate (hexahydrate) and 15 kg of magnesium sulfate (seven salt) were added to 49.5 kg of water with stirring, followed by dissolving. Then, 1 kg of an acrylic polymer 0.5 kg of an acid resistant surfactant and 14 kg of hydrofluoric acid (55%) were sequentially added. After confirming that the mixture was added to the mixture was stirred for 30 minutes and left for at least 10 hours to obtain a product.

상술한 바에 의하여 제조된 도포제를 재질 하스테로이 B로서 제작한후, 유황용해 탱크의 내외면에 도포하고, 약 60분간 방치후 고압 수세정을 행하였다.The coating agent prepared as described above was prepared as the material Hastelloy B, and then applied to the inner and outer surfaces of the sulfur dissolution tank, and left for about 60 minutes, followed by high pressure water washing.

용접부분은 물론 전체에 얼룩진 곳이 없이 미려하게 가공되었다.The welded part was of course beautifully processed without spots on the whole.

본 재질은 스텐레스강으로는 사용에 견디지 못하는 염화수소가스, 황산동 등에 견딜 수 있는 특성을 보유하는 특수 합금이며, 그 내열식, 내마모는 높이 평가되어 플랜트 심장부에 널리 이용되고 있었던 만큼 본제의 개발은 재질과 마찬가지로 높이 평가되는 것이다.This material is a special alloy that has properties that can withstand hydrogen chloride gas, copper sulfate, etc., which cannot be used in stainless steel, and its heat resistance and abrasion resistance are highly evaluated and widely used in the heart of the plant. As is appreciated.

[실시예 9]Example 9

물 43㎏, 질산(67%) 30㎏을 교반하면서 혼화하고, 인산마그네슘(5수염) 10㎏을 가하여 용해한 후, 불산(55%) 15㎏, 아크릴계 중합물 1㎏, 내산성 계면활성제 1㎏을 순차혼화 확인하면서 첨가하고, 이후 30분간 교반하고 10시간 이상 방치하여 제품으로 하였다.After mixing 43 kg of water and 30 kg of nitric acid (67%) with stirring, 10 kg of magnesium phosphate (pentarate) was added and dissolved, 15 kg of hydrofluoric acid (55%), 1 kg of acrylic polymer, and 1 kg of acid resistant surfactant were sequentially added. The mixture was added while checking for miscibility, and then stirred for 30 minutes and left for 10 hours or more to obtain a product.

상술한 바와같이 제조된 도포제를 스텐레스강 sus304L재로서 제작된 에치렌그리콜 저장탱크 내면적 3000㎡에 스프레이로서 취부도포하고, 약 16시간 방치한 후, 고압수세정을 행하였다.The coating agent prepared as described above was spray-coated onto an inner surface area of 3000 m 2 of an ethylene glycol storage tank made of stainless steel sus304L, and left for about 16 hours, followed by high-pressure water washing.

에치렌 그리콜 저장탱크는 세정검사가 대단히 엄격하나 본제 사용에 의하면 용접 스케일을 포함하는 불순물이 완전히 제거되어 검사에 합격하였다.The ethylene glencol storage tank has a very strict cleaning test, but according to the use of this product, impurities including welding scale have been completely removed and passed the test.

또 본제를 알미늄제의 탱크용접면의 스케일 제거에 응용하였던 바, 도포후, 약 5분간으로서 스케일은 제거되며, 수세후에도 산의 잔류가 없고, 알미늄재에 대한 부식도 없었다.In addition, the present application was applied to descaling the tank welding surface made of aluminum. After application, the scale was removed for about 5 minutes, and there was no residual of acid even after washing with water, and no corrosion to the aluminum material.

따라서 형상에도 연유하지만 알미늄재에의 사용은 가능하다.Therefore, although it is soft in shape, it can be used for aluminum materials.

Claims (1)

물, 염산, 질산, 인산, 취산, 지오그리콜산으로부터 이루어지는 군에서 선택된 1 또는 2이상을 혼화하는 공정, 다음에 상기한 액에 가용성으로서 산에 안정한 마그네슘염의 1종이상을 첨가 용해하여서 용액으로하는 공정, 이 용액에 불산 혹은 불화암모늄 혹은 그 수용액 및 아크릴계중합물과 내산성의 계면활성제를 가하여 혼합액으로 하는 공정, 이 혼합액을 교반하여 방치한 후, 점성물로하는 공정으로 이루어지거나 또는 전기한 제조방법에 의해 최종적으로 얻어진 점성물에 물, 질산, 불산으로부터 이루어지는 군에서 선택된 1종 또는 2종이상의 액체를 가하여 희석하는 것을 포함하는 스텐레스강의 스케일 제거제의 제조법.Mixing one or two or more selected from the group consisting of water, hydrochloric acid, nitric acid, phosphoric acid, bleeding acid and geoglycolic acid, and then adding and dissolving one or more of the acid-stable magnesium salts into a solution to dissolve the solution. To a solution prepared by adding hydrofluoric acid or ammonium fluoride or its aqueous solution, an acrylic polymer, and an acid-resistant surfactant to this solution to form a mixed solution, stirring and leaving the mixed solution to form a viscous substance. A method for producing a descaling agent for stainless steel, comprising diluting and adding one or two or more liquids selected from the group consisting of water, nitric acid and hydrofluoric acid to the viscous substance finally obtained.
KR770003065A 1977-12-28 1977-12-28 Method for manufacturing descaling agents for stainless steel KR810000367B1 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008137796A1 (en) * 2007-05-04 2008-11-13 Ecolab Inc. Mg++chemistry and method for fouling inhibition in heat processing of liquid foods and industrial processes
US8247363B2 (en) 2007-05-04 2012-08-21 Ecolab Usa Inc. MG++ chemistry and method for fouling inhibition in heat processing of liquid foods and industrial processes
KR101327187B1 (en) * 2013-07-24 2013-11-06 손경업 Descaling and passive state processing composition for stainless steel and descaling method of stainless steel using the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008137796A1 (en) * 2007-05-04 2008-11-13 Ecolab Inc. Mg++chemistry and method for fouling inhibition in heat processing of liquid foods and industrial processes
US8143204B2 (en) 2007-05-04 2012-03-27 Ecolab Usa Inc. Mg++ chemistry and method for fouling inhibition in heat processing of liquid foods and industrial processes
US8247363B2 (en) 2007-05-04 2012-08-21 Ecolab Usa Inc. MG++ chemistry and method for fouling inhibition in heat processing of liquid foods and industrial processes
KR101327187B1 (en) * 2013-07-24 2013-11-06 손경업 Descaling and passive state processing composition for stainless steel and descaling method of stainless steel using the same

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