KR101058965B1 - How to suppress grain boundary corrosion on metal surfaces - Google Patents
How to suppress grain boundary corrosion on metal surfaces Download PDFInfo
- Publication number
- KR101058965B1 KR101058965B1 KR1020057007590A KR20057007590A KR101058965B1 KR 101058965 B1 KR101058965 B1 KR 101058965B1 KR 1020057007590 A KR1020057007590 A KR 1020057007590A KR 20057007590 A KR20057007590 A KR 20057007590A KR 101058965 B1 KR101058965 B1 KR 101058965B1
- Authority
- KR
- South Korea
- Prior art keywords
- corrosion
- sprayed water
- reaction product
- water
- delete
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/12—Accessories for subsequent treating or working cast stock in situ
- B22D11/124—Accessories for subsequent treating or working cast stock in situ for cooling
- B22D11/1245—Accessories for subsequent treating or working cast stock in situ for cooling using specific cooling agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/12—Accessories for subsequent treating or working cast stock in situ
- B22D11/124—Accessories for subsequent treating or working cast stock in situ for cooling
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
- C23F11/14—Nitrogen-containing compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
본 발명은, 표면이 분무수 또는 응축물과 접촉하는 산업용수 및 공정 시스템에서 상기 금속 표면의 입계 부식을 억제하기 위한 알카인다이올 및 폴리알킬렌의 반응 생성물의 용도에 관한 것이다. The present invention relates to the use of the reaction product of alkyindiol and polyalkylene for inhibiting intergranular corrosion of the metal surface in industrial water and process systems where the surface is in contact with sprayed water or condensate.
금속 및 합금의 미세구조는 결정 경계선(grain boundary)에 의해 분리되는 결정으로 이루어진다. 입계 부식은 결정 경계선에 따른 국소화된 공격 또는 결정 경계선에 바로 근접한 국소화된 공격으로서 정의될 수 있다. 이러한 침전으로 인해 가까운 주변에서 부식 저항성이 저하된 대역이 발생할 수 있다. The microstructures of metals and alloys consist of crystals separated by grain boundaries. The grain boundary corrosion can be defined as a localized attack along the crystal boundary or a localized attack immediately near the crystal boundary. This precipitation can result in zones of reduced corrosion resistance in the immediate vicinity.
입계 부식의 예로는 스테인레스 강 또는 용접 부식의 증감을 들 수 있다. 크롬이 풍부한 결정 경계선 침전물은 이들 침전물에 인접하는 Cr 국소 고갈을 야기하고, 이로 인해 상기 영역은 부식 공격에 대해 공격받기 쉬워진다. Examples of grain boundary corrosion include increase and decrease of stainless steel or weld corrosion. Chromium-rich crystal boundary precipitates result in local depletion of Cr adjacent to these precipitates, thereby making the region vulnerable to corrosion attack.
박리 부식은 입계 부식의 구체적인 형태이다. 박리 또는 박편은 표면을 따르는 결정 경계선을 따라 나타나는 층에서 금속의 손실로서 나타난다. 주조물에서 의 박리는, 예를 들어 직접적인 분무수 접촉이 발생하지 않는 보다 적은 단편의 비-습윤 구조에서 발생한다. 강철은 표면이 분무수 미스트 또는 응축물에 의해서만 습윤되는 고온의 습윤 환경에 노출된다. 부식은 강철 표면을 따라 급속하게 퍼져서 2차 지지 구조의 구조적 보전성의 손실을 야기한다.Peel corrosion is a specific form of intergranular corrosion. Peeling or flakes appear as a loss of metal in the layer along the crystal boundary along the surface. Peeling from the casting occurs, for example, in less fragments of non-wet structure in which no direct spray water contact occurs. Steel is exposed to a high temperature wet environment where the surface is wetted only by sprayed water mist or condensate. Corrosion spreads rapidly along the steel surface, causing a loss of structural integrity of the secondary support structure.
박리 부식에 대한 기작은 분무수 중의 클로라이드 존재와 관련된다. 미스트(증기)는 분무수 시스템에 사용되는 경우 증기 챔버를 통해 이동하며 강철 표면 상에서 응축된다. 열 및 습기가 이러한 강철 표면으로부터 물을 증발시키고, 이로 인해 농축된 클로라이드 이온이 남겨진다. 이러한 공정이 계속되어 박리가 발생하는 시점까지 보다 많은 클로라이드 이온을 농축시킨다.The mechanism for exfoliation corrosion is related to the presence of chloride in the spray water. Mist (vapor), when used in spray water systems, moves through the vapor chamber and condenses on steel surfaces. Heat and moisture evaporate water from this steel surface, which leaves concentrated chloride ions. This process continues, concentrating more chloride ions until the point at which exfoliation occurs.
쿠폰 분석을 통해 부식 기작이 다음과 같이 발생함이 밝혀진다: 금속 표면 상에 침착된 클로라이드 이온이 부식 생성물/생성된 침착물의 부서지기 쉬운 층을 통해 이동한다. 침착물 밑에 일시적인 염화철 염이 생성된다. 이 염은 흡습성(습기를 흡수한다)이고, 가수분해시 산 클로라이드 조건을 생성한다. 산성 부식이 금속 표면에서 보다 깊이 진행됨에 따라 추가의 철 옥사이드 부식 생성물이 남게 된다. Coupon analysis reveals that the corrosion mechanism occurs as follows: chloride ions deposited on the metal surface migrate through the brittle layers of the corrosion product / generated deposits. A temporary iron chloride salt is formed under the deposit. This salt is hygroscopic (absorbs moisture) and produces acid chloride conditions upon hydrolysis. As acidic corrosion proceeds deeper at the metal surface, additional iron oxide corrosion products remain.
전술한 바와 같이, 당분야에서는 산업 공정 시스템에 존재하는 박리 부식을 제거하기 위한 기술 및 억제제가 요구되고 있다.As mentioned above, there is a need in the art for techniques and inhibitors to remove exfoliation corrosion present in industrial process systems.
본 발명은, 산업 공정 시스템, 예를 들어 증기 및 냉각수 시스템에서 분무수 또는 응축물과 접촉하는 금속 표면의 입계 부식을 억제하는 방법으로서, 알카인다이올 및 폴리알킬렌 폴리아민의 반응 생성물을 부식을 억제하기에 충분한 양으로 상기 분무수에 첨가하는 단계를 포함하는 방법에 관한 것이다.The present invention is a method of inhibiting intergranular corrosion of metal surfaces in contact with sprayed water or condensate in industrial process systems, such as steam and cooling water systems, wherein the reaction products of alkyidadiol and polyalkylene polyamine It relates to a method comprising the step of adding to the spray water in an amount sufficient to inhibit.
반응 생성물이 형성되는 조건은 본원에서 이의 전체 내용을 참조로서 인용하는 미국 특허 제 3,211,667 호에 개시되어 있다.The conditions under which the reaction product is formed are disclosed in US Pat. No. 3,211,667, which is incorporated herein by reference in its entirety.
반응 생성물의 제조에 효과적일 것으로 생각되는 알카인다이올 및 알켄다이올은 4 내지 12의 탄소원자를 함유하는 것이다. 바람직하게는, 알카인다이올의 탄소수는 4이다. 알카인다이올의 예로는 뷰타인다이올을 들 수 있다.Alkydinadiols and alkenediols which are considered to be effective in the preparation of the reaction products are those containing from 4 to 12 carbon atoms. Preferably, the carbon number of the alkyindadiol is four. An example of an alkyindiol is butydinol.
반응 생성물을 제조하는데 효과적인 것으로 교시된 폴리알킬렌 폴리아민 화합물은 2 내지 10개의 아민 기, 바람직하게는 3 내지 7개의 아민 기를 포함하는 것이다. 이들 아민 기는 치환되거나 또는 치환되지 않을 수 있고, 각각 탄소수 1 내지 6, 바람직하게는 탄소수 2 내지 4의 알킬렌 기에 의해 분리된다. 대표적인 폴리아민은 에틸렌 다이아민, 다이에틸렌 트라이아민, 펜타에틸렌 헥스아민, 펜타프로필렌 헥스아민, 트라이헵틸렌 다이아민 등을 포함한다.Polyalkylene polyamine compounds taught to be effective in preparing reaction products are those comprising from 2 to 10 amine groups, preferably from 3 to 7 amine groups. These amine groups may be substituted or unsubstituted, and are each separated by alkylene groups having 1 to 6 carbon atoms, preferably 2 to 4 carbon atoms. Representative polyamines include ethylene diamine, diethylene triamine, pentaethylene hexamine, pentapropylene hexamine, triheptylene diamine, and the like.
반응물의 중량비는, 각각의 성분의 완전한 반응이 수득되게 하는 것으로서, 아민 대 다이올의 중량비는 4:1 내지 1:1, 바람직하게는 3:1이다. 이온화가능한 구리 화합물, 예컨대 구리 아세테이트가 촉매량으로 본 반응에서 사용된다.The weight ratio of the reactants is such that a complete reaction of each component is obtained, with the weight ratio of amine to diol being 4: 1 to 1: 1, preferably 3: 1. Ionizable copper compounds such as copper acetate are used in this reaction in catalytic amounts.
본 발명의 반응 생성물은 금속 표면의 부식을 억제하기에 충분한 양으로 분무수에 첨가될 수 있다. 반응 생성물은 공급 라인 중에 존재하는 물의 0.5 내지 약 500ppm의 양으로 공급 라인에 첨가될 수 있다. 바람직하게는, 약 1 내지 100ppm, 특히 바람직하게는 5 내지 10ppm의 물이 첨가된다.The reaction product of the present invention may be added to the sprayed water in an amount sufficient to inhibit corrosion of the metal surface. The reaction product may be added to the feed line in an amount of 0.5 to about 500 ppm of water present in the feed line. Preferably, about 1 to 100 ppm, particularly preferably 5 to 10 ppm of water is added.
본 발명의 반응 생성물은 용매중에 포함되거나 순 형태로 공급 라인에 공급된다. 바람직하게는, 반응 생성물은 수성 용매, 예를 들어 물에 첨가된다. 이 반응 생성물은 다른 적당한 성분, 예컨대 소포제, 부식 억제제 등과 함께 분무수에 첨가될 수 있다. 전형적으로, 처리되는 시스템에서의 분무수의 온도는 약 110 내지 180℉이다.The reaction product of the present invention is included in the solvent or fed to the feed line in net form. Preferably, the reaction product is added to an aqueous solvent, for example water. This reaction product can be added to the sprayed water together with other suitable components such as antifoaming agents, corrosion inhibitors and the like. Typically, the temperature of the spray water in the system to be treated is about 110 to 180 degrees Fahrenheit.
하기 데이터는 본 발명의 용도에서의 예상치 못한 결과를 증명한다. 하기 실시예는 본 발명의 예시로서, 본 발명의 범주를 제한하고자 함이 아니다. The following data demonstrates unexpected results in the use of the present invention. The following examples are illustrative of the invention and are not intended to limit the scope of the invention.
금속 표면에서 발생하는 부식 기작을 억제하기 위해서, 물 및 클로라이드로부터 표면을 분리시키는 필름 물질을 첨가하였다. 2-뷰타인-1, 4-다이올-폴리에틸렌폴리아민(생성물 A)의 첨가는 강철의 부식 속도를 현저하게 감소시켰다(표 1 및 2 참조). 모든 시험에서는, 분무 챔버내에 다양한 부식 쿠폰을 배치하기 위해 쿠폰 트리를 구성하였다. 이 용액을 주조 분무로의 공급 라인으로 주입하였다. 분무 챔버를 통해 물질을 분포시켰다.In order to suppress the corrosion mechanism occurring on the metal surface, a film material was added which separates the surface from water and chloride. The addition of 2-butyne-1, 4-diol-polyethylenepolyamine (Product A) significantly reduced the corrosion rate of steel (see Tables 1 and 2). In all tests, a coupon tree was constructed to place various corrosion coupons in the spray chamber. This solution was injected into the feed line to the casting spray furnace. The material was distributed through the spray chamber.
침착물에서의 철 수준이 크게 감소되었다. Iron levels in the deposits were greatly reduced.
상기 결과를 통해, 클로라이드 농도는 처리되지 않은 면(5%) 및 처리된 면(6%)에서 모두 유사한 반면, 다른 성분은 크게 상이함을 알 수 있다. 처리되지 않은 면의 철 수준은 88%이고; 박리 수준 또한 유의하다. 처리된 면에서, 철 수준은 단지 23%이었으며, 박리는 발생하지 않았다. 처리된 면의 칼슘 함량은 52%이었고, 이는 부식이 억제되었음을 의미한다. The results show that the chloride concentrations are similar in both untreated (5%) and treated (6%), while the other components are significantly different. The iron level of untreated cotton is 88%; Peel levels are also significant. In terms of treatment, the iron level was only 23% and no delamination occurred. The calcium content of the treated cotton was 52%, which meant that corrosion was suppressed.
추가의 시험에서, 부식 쿠폰을 생성물 A 중에 침지시키고, 이를 처리된 스트렌드 및 처리되지 않은 스트랜드 모두에서 처리되지 않은 쿠폰 다음에 배치하였다. 처리되지 않은 스트랜드에서, 침지된 쿠폰은 거의 부식되지 않은 반면, 처리되지 않은 쿠폰은 박리되었다. 처리된 스트랜드에서는, 쿠폰에 비해 부식 제어에서 상당한 개선이 있었다. In a further test, the corrosion coupon was immersed in Product A and placed after the untreated coupon in both treated and untreated strands. In the untreated strands, the soaked coupons were hardly corroded while the untreated coupons were peeled off. In the treated strands, there was a significant improvement in corrosion control over coupons.
본 발명의 다른 시험에서는, 다른 쿠폰 트리를 구성하였다. 시험된 쿠폰은 연강, 스테인레스 강, 구리 및 피복된 연강을 포함하였다.In another test of the present invention, another coupon tree was constructed. Coupons tested included mild steel, stainless steel, copper and coated mild steel.
개시 점검으로서 8일 후에 연강 쿠폰의 단일 세트를 제거하였다. 쿠폰 결과를 하기 표 3에 제시한다. 2번 스트랜드로부터의 쿠폰은 박리를 나타낸 반면, 1번 스트랜드로부터의 쿠폰은 단지 일반적 부식 기작을 나타냈다. After 8 days as a start-up check, a single set of mild steel coupons was removed. Coupon results are shown in Table 3 below. Coupons from strand 2 showed delamination, while coupons from strand 1 only showed a general corrosion mechanism.
하기 표 4에서 추가로 제시된 바와 같이, 생성물 A가 주입된 1번 스트랜드에서는 부식 쿠폰 트리상의 부식률이 크게 감소되었다. 생성물 A는 시스템을 통해 15ppm으로 공급되었다. 연강 부식률은 대부분의 위치에서 약 50 내지 80% 감소하였다. 전술한 바와 같이, 2번 스트랜드로부터의 쿠폰은 박리를 나타내는 반면, 1번 스트랜드 1로부터의 쿠폰은 단지 일반적인 부식 기작을 나타냈다(박리되지 않았다). As further shown in Table 4 below, the corrosion rate on the corrosion coupon tree was significantly reduced in strand 1 into which product A was injected. Product A was supplied at 15 ppm through the system. Mild steel corrosion rate was reduced by about 50 to 80% at most locations. As noted above, coupons from strand 2 exhibited delamination, while coupons from strand 1 exhibited only general corrosion mechanisms (not peeled).
나머지 쿠폰은 모두 스테인레스 강 또는 코팅된 쿠폰이 아니며, 이들 쿠폰중 어느 것에서도 심각한 부식이 발견되지 않았음을 주목한다. 또한, 본 발명의 처리는 분무수 시스템의 충격 노즐 성능에 불리한 영향을 미치지 않았다. Note that the remaining coupons are not all stainless steel or coated coupons, and no serious corrosion was found in any of these coupons. In addition, the treatment of the present invention did not adversely affect the impact nozzle performance of the spray water system.
본 발명은 특정 실시양태를 참조로 기술되었으나, 당분야의 숙련자들에게는 본 발명의 다수의 기타 형태 또는 개질물이 명백할 것이다. 첨부된 청구범위 및 본 발명은 일반적으로 본 발명의 진의 및 범주에 벗어나지 않는 한 상기 명백한 형태 및 개질물을 포함하는 것으로 이해되어야 한다. While the invention has been described with reference to specific embodiments, many other forms or modifications of the invention will be apparent to those skilled in the art. It is to be understood that the appended claims and the invention generally include the above obvious forms and modifications without departing from the spirit and scope of the invention.
Claims (15)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/283,457 US20040086419A1 (en) | 2002-10-30 | 2002-10-30 | Methods for inhibiting intergranular corrosion of metal surfaces |
US10/283,457 | 2002-10-30 | ||
PCT/US2003/028266 WO2004042115A1 (en) | 2002-10-30 | 2003-09-10 | Methods for inhibiting intergranular corrosion of metal surfaces |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20050083872A KR20050083872A (en) | 2005-08-26 |
KR101058965B1 true KR101058965B1 (en) | 2011-08-23 |
Family
ID=32174660
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020057007590A KR101058965B1 (en) | 2002-10-30 | 2003-09-10 | How to suppress grain boundary corrosion on metal surfaces |
Country Status (17)
Country | Link |
---|---|
US (1) | US20040086419A1 (en) |
EP (1) | EP1558787B1 (en) |
JP (1) | JP4424671B2 (en) |
KR (1) | KR101058965B1 (en) |
CN (1) | CN100425735C (en) |
AT (1) | ATE355402T1 (en) |
AU (1) | AU2003267075B2 (en) |
BR (1) | BR0315190B1 (en) |
CA (1) | CA2504421A1 (en) |
DE (1) | DE60312202T2 (en) |
ES (1) | ES2282654T3 (en) |
NZ (1) | NZ540134A (en) |
PL (1) | PL376482A1 (en) |
RU (1) | RU2320778C2 (en) |
UA (1) | UA80451C2 (en) |
WO (1) | WO2004042115A1 (en) |
ZA (1) | ZA200503934B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
MD307Z (en) * | 2010-04-27 | 2011-07-31 | Институт Прикладной Физики Академии Наук Молдовы | Inhibitor of steel corrosion in the water |
RU2754319C1 (en) * | 2020-12-14 | 2021-09-01 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Башкирский государственный университет" | Method for obtaining corrosion inhibitors based on tetrapropylene pentamines for oilfield equipment and pipelines |
RU2754326C1 (en) * | 2020-12-14 | 2021-09-01 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Башкирский государственный университет" | Method for producing bis-imidazolines and their derivatives based on pentaethylene hexamines for corrosion protection of oilfield equipment and pipelines |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3113113A (en) | 1958-11-07 | 1963-12-03 | Armour & Co | Corrosion inhibitor compositions |
US3152187A (en) | 1960-04-13 | 1964-10-06 | Continental Oil Co | Condensation product of unsaturated diols and polyalkylene polyamines and method of preparation thereof |
US3211667A (en) | 1960-04-13 | 1965-10-12 | Continental Oil Co | Corrosion inhibition |
US3320318A (en) | 1963-08-19 | 1967-05-16 | Continental Oil Co | Thiobenzene-diol-polyamine corrosion inhibiting composition |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2923599A (en) * | 1958-03-26 | 1960-02-02 | Universal Oil Prod Co | Water-soluble corrosion inhibitors |
GB894386A (en) * | 1959-04-20 | 1962-04-18 | Continental Oil Co | Polyamine-diol reaction products and corrosion inhibiting compositions containing same |
FR2477923A1 (en) * | 1980-03-11 | 1981-09-18 | Compiegne Universite Technolog | Water spray cooling process, esp. in continuous casting - with addn. of ions to water to reduce wear of rolls |
DE3317126C2 (en) * | 1983-05-06 | 1986-07-24 | Mannesmann AG, 4000 Düsseldorf | Process to avoid acid corrosion on continuous casting plants |
US5173213A (en) * | 1991-11-08 | 1992-12-22 | Baker Hughes Incorporated | Corrosion and anti-foulant composition and method of use |
US5311925A (en) * | 1993-11-12 | 1994-05-17 | Nalco Chemical Company | Magnesium hydroxide to prevent corrosion caused by water spray in continuous casting |
CA2123936C (en) * | 1994-04-06 | 2005-12-27 | Bruno E. Morin | Methods of inhibiting water corrosion in crude oil pipelines |
-
2002
- 2002-10-30 US US10/283,457 patent/US20040086419A1/en not_active Abandoned
-
2003
- 2003-09-10 AU AU2003267075A patent/AU2003267075B2/en not_active Expired
- 2003-09-10 ES ES03749550T patent/ES2282654T3/en not_active Expired - Lifetime
- 2003-09-10 DE DE60312202T patent/DE60312202T2/en not_active Expired - Lifetime
- 2003-09-10 CN CNB038256347A patent/CN100425735C/en not_active Expired - Lifetime
- 2003-09-10 NZ NZ540134A patent/NZ540134A/en not_active IP Right Cessation
- 2003-09-10 BR BRPI0315190-5A patent/BR0315190B1/en active IP Right Grant
- 2003-09-10 CA CA002504421A patent/CA2504421A1/en not_active Abandoned
- 2003-09-10 WO PCT/US2003/028266 patent/WO2004042115A1/en active IP Right Grant
- 2003-09-10 PL PL03376482A patent/PL376482A1/en unknown
- 2003-09-10 AT AT03749550T patent/ATE355402T1/en not_active IP Right Cessation
- 2003-09-10 JP JP2004549947A patent/JP4424671B2/en not_active Expired - Fee Related
- 2003-09-10 RU RU2005116268/02A patent/RU2320778C2/en not_active IP Right Cessation
- 2003-09-10 EP EP03749550A patent/EP1558787B1/en not_active Expired - Lifetime
- 2003-09-10 KR KR1020057007590A patent/KR101058965B1/en active IP Right Grant
- 2003-10-09 UA UAA200505034A patent/UA80451C2/en unknown
-
2005
- 2005-05-16 ZA ZA200503934A patent/ZA200503934B/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3113113A (en) | 1958-11-07 | 1963-12-03 | Armour & Co | Corrosion inhibitor compositions |
US3152187A (en) | 1960-04-13 | 1964-10-06 | Continental Oil Co | Condensation product of unsaturated diols and polyalkylene polyamines and method of preparation thereof |
US3211667A (en) | 1960-04-13 | 1965-10-12 | Continental Oil Co | Corrosion inhibition |
US3320318A (en) | 1963-08-19 | 1967-05-16 | Continental Oil Co | Thiobenzene-diol-polyamine corrosion inhibiting composition |
Also Published As
Publication number | Publication date |
---|---|
RU2005116268A (en) | 2006-02-10 |
CN1714173A (en) | 2005-12-28 |
KR20050083872A (en) | 2005-08-26 |
ATE355402T1 (en) | 2006-03-15 |
BR0315190B1 (en) | 2013-02-05 |
NZ540134A (en) | 2006-10-27 |
DE60312202D1 (en) | 2007-04-12 |
DE60312202T2 (en) | 2007-10-31 |
CA2504421A1 (en) | 2004-05-21 |
WO2004042115A1 (en) | 2004-05-21 |
EP1558787A1 (en) | 2005-08-03 |
RU2320778C2 (en) | 2008-03-27 |
CN100425735C (en) | 2008-10-15 |
ES2282654T3 (en) | 2007-10-16 |
ZA200503934B (en) | 2006-08-30 |
PL376482A1 (en) | 2005-12-27 |
JP2006504870A (en) | 2006-02-09 |
EP1558787B1 (en) | 2007-02-28 |
US20040086419A1 (en) | 2004-05-06 |
AU2003267075B2 (en) | 2009-06-25 |
AU2003267075A1 (en) | 2004-06-07 |
BR0315190A (en) | 2005-08-23 |
UA80451C2 (en) | 2007-09-25 |
JP4424671B2 (en) | 2010-03-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2205943C (en) | Corrosion inhibitor | |
US4045253A (en) | Passivating metal surfaces | |
EP0512689B1 (en) | Prevention of formation of fouling deposits on metallic surfaces | |
KR101058965B1 (en) | How to suppress grain boundary corrosion on metal surfaces | |
US4595723A (en) | Corrosion inhibitors for alkanolamines | |
RU2334689C2 (en) | Composition for corrosion and salt deposition prevention | |
US4596849A (en) | Corrosion inhibitors for alkanolamines | |
US9382629B2 (en) | Preventing equipment fouling via corrosion reduction | |
KR100421410B1 (en) | 2-Amino-1-Methoxypropane as a Neutralizing Amine in Refinery Processes | |
US3152187A (en) | Condensation product of unsaturated diols and polyalkylene polyamines and method of preparation thereof | |
US3211667A (en) | Corrosion inhibition | |
KR20100051702A (en) | Method for inhibiting corrosion of metal in distillation units caused by organic acids | |
US4873014A (en) | Polyamine-polyglycol inhibitor for steel pickling | |
WO2020008477A1 (en) | A neutralizing amine formulation and process of preparation thereof | |
WO1993010877A1 (en) | 1,1-dichloro-1-fluoroethane dewatering systems | |
EP1115907A1 (en) | Inhibition of corrosion in aqueous systems | |
US4004055A (en) | Inhibiting stress cracking | |
JP2006504870A5 (en) | ||
EP0565371A2 (en) | Boiler double buffers | |
Sherstobitova et al. | Influence of inhibitor PGU-2 on acid pickling and hydrogen absorption of steels. | |
WO2016093952A1 (en) | Inhibiting toxicity of acid systems used for treating metals | |
TH44099A (en) | An improved method for this practice is to use a grinder of sheet metal and sheet metal prepared products. |
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: 20140805 Year of fee payment: 4 |
|
FPAY | Annual fee payment |
Payment date: 20150805 Year of fee payment: 5 |
|
FPAY | Annual fee payment |
Payment date: 20160805 Year of fee payment: 6 |
|
FPAY | Annual fee payment |
Payment date: 20170808 Year of fee payment: 7 |
|
FPAY | Annual fee payment |
Payment date: 20180807 Year of fee payment: 8 |
|
FPAY | Annual fee payment |
Payment date: 20190806 Year of fee payment: 9 |