CN1442508A - Surface anticorrusion method of submarine - Google Patents
Surface anticorrusion method of submarine Download PDFInfo
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- CN1442508A CN1442508A CN 02146400 CN02146400A CN1442508A CN 1442508 A CN1442508 A CN 1442508A CN 02146400 CN02146400 CN 02146400 CN 02146400 A CN02146400 A CN 02146400A CN 1442508 A CN1442508 A CN 1442508A
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- submarine
- plating bath
- container
- plating
- coating
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Abstract
An anticorrosion technology for the surface of submarine features that the surface of submarine is integrally treated, and includes such steps as chemically plating a copper layer with 3-5 microns of thickness, and chemically plating a Ni-W-P layer with 50-80 microns of thickness. Its advantages are high resistance to seawater corrosion, high hardness and strength, and high antiwear nature.
Description
Technical field: the effect in modernized war of conventionally-powered submarine and nuclear-powered submarine increases day by day, and especially modern war makes submarine become the indispensable equipment of modernized naval, also is the symbol of a national naval military strength.This project belongs to modernization of national defense field.
Background technology: because submarine slips into b.s.l. work for a long time.The submarine surface is subjected to the parasitic erosion of corrosion and ocean of seawater for a long time, the submarine shell mostly is high-quality alloy steel and is welded, the submarine surface is easy to be corroded under the acting in conjunction of surface stress, composition difference, seawater, ocean parasite and huge sea pressure, influence submarine work-ing life even the safety that directly jeopardizes submarine.The surface anticorrosion of submarine becomes the manufacturing problem of being badly in need of solution of countries in the world submarine for this reason.The leader of General Armament Department of PLA also pays much attention to the anticorrosion research on submarine surface.Because the curved transition of submarine profile is big, the surface anticorrosion of submarine substantially all is the method that adopts topcoating both at home and abroad.Though different types of coating has improved the antiseptic power on submarine surface, also differ greatly with the requirement for anticorrosion on submarine surface.
Summary of the invention: the present invention proposes the new processing method of a kind of submarine surface anticorrosive.The object of the present invention is achieved like this, and the first step adopts the method for electroless plating to plate the metallic copper that a layer thickness is 3~5 μ m at the submarine integral surface.Second step was the nickel-tungsten-phosphorus composite bed that plates one deck 50~80 μ m on copper plate with the method for electroless plating, well-known metallic nickel is the best metallic substance of anti-seawater corrosion, the anti-seawater corrosion ability that any chemical coating all is not so good as metallic nickel is strong, for improving intensity, hardness, the resistance to corrosion of nickel layer, adopt the method for the compound plating of Ni-W-P, at the Ni-W-P composite bed of submarine integral surface plating one deck 0.02~0.2mm, its resistance to corrosion greatly strengthens.
Specific implementation method is:
1) build a 2-3 doubly to the closed container of submarine, inner surface of container is industrial enamel or stainless steel, and container places the vessel space middle part with four submarines of naming a person for a particular job, and around the container several shower nozzles is arranged, and can spray into liquid and high-pressure hydraulic pump is housed and fluid circulation system.
2) will simulate the submarine surface and make processing of rust removing, the dilute hydrochloric acid solution with 10% removes corrosion.
3) be that the sand grains of 2-3mm carries out sandblasting with granularity, further remove corrosion, the stain of submarine.
4) preparation copper facing liquid, concrete composition is:
(1)CuSO
4·5H
2O?????????????????10~15%;
(2) Tartaric acid potassium sodium NaKC4H4Oi4H
2O 10~20%;
(3) the BDTA disodium salt 25~40%;
(4)NaOH???????????????????????????7~15%;
(5) formaldehyde HCHO37% 10~15%;
(6) a, a
1-dipyridyl 0.05~0.1%;
(7) yellow prussiate of potash K
4(Fe (CN)
6) 20~30%.
PH value is transferred to 12.5 with NaOH, bath temperature is risen to 40-50 ℃.
With water pump plating bath is sprayed to submarine from different perspectives, make plating bath be full of container, under the effect of spraying, plating bath is in the submarine surface flow.According to the thickness requirement controlled liq spraying cycle mobile time of coating, perhaps calculate the thickness of coating on submarine surface according to the change in concentration of plating bath, the copper at submarine surface plating one deck 3~5 μ m stops to spray, and plating bath is emitted from container.Till being neutrality with pure water rinsing submarine surface to effusive water.Treat the compound plating processing of step nickel-tungsten-phosphorus down of the air-dry laggard row in submarine surface.
5) preparation Ni-W-P composite plating bath body, concrete composition is:
(1)NiSO
4·6H
2O???????????20%;
(2)WSO
4·4H
2O????????????15%;
(3)NaH
2PO
2·H
2O?????????25%;
(4)Na
3C
6H
6O
7???????????20%;
(5)NaC
2H
3O
2?????????????10%;
(6)〔CH
2(NH
2)COOH〕??????10%。
With pure water pH value is transferred to 3.8, bath temperature is risen to 80-85 ℃.
With water pump plating bath is sprayed to submarine from different perspectives, make plating bath be full of container, under the effect of spraying, plating bath is in the submarine surface flow.According to the thickness requirement controlled liq spraying cycle mobile time of coating, perhaps go out the thickness of coating on submarine surface according to the nickel ion concentration change calculations of plating bath, when reaching thickness requirement, stop to spray, plating bath is emitted from container.
6) the Ni-W-P composite bed thickness on measurement submarine surface, and P content requires between the 7-11%, and optimum value is 9%, and containing the W amount is 3~5%, and optimum value is 4%, and all the other are Ni.
7) to the compound plating of submarine the time, put a test block identical with the submarine surfacing, the test block overlay coating is carried out physics, the anti-rotten experiment of chemistry, to infer the compound plating effect on submarine surface.
We have done the compound plating experiment of surperficial Ni-W-P to four kinds of high-quality steel, prove its anti-seawater corrosion effect splendid (seeing Table 1).
Table 1: the corrosion situation of four kinds of steel in different media, 63%H
2SO
4Solution, 5 moles of KOH solution were put in seawater 90 days.
Material | Highquality carbon steel | Structural alloy steel | High-quality alloy steel | Manganese steel |
??H 2SO | Extremely serious | Extremely serious | Extremely serious | Extremely serious |
??KOH | Extremely serious | Extremely serious | Extremely serious | Extremely serious |
Seawater | Corrosion is arranged | Corrosion is arranged | Corrosion is arranged | Corrosion is arranged |
Table 2: after four kinds of steel pass through the compound plating of Ni-W-P in the table 1, the anticorrosive situation in different media
Material | ????H 2SO | ????KOH | Seawater |
The compound plating of Ni-W-P | Good | Good | Extremely strong |
Neutral salt spray test shows that the plating of carbon steel surface is the N-W-P composite bed of 30 μ m, and wherein P content 9%, W content 3.6%, and Ni content 87.4% is not seen corrosion through 3000 hours surfaces.
Embodiment 1:
The simulation submarine is carried out surperficial corrosion-resistant treatments; (1) simulation submarine volume 1m
3(2) simulation submarine enclosure material: 40CrMnTi; (3) simulation submarine enclosure material thickness and locate 8mm, modifier treatment; (4) surface treatment container, volume 3m
3, stainless steel is made, and is provided with 36 nozzles in container.(5) simulation submarine surface treatment (simulation submarine profile is identical with the submarine profile); 1. rust cleaning is removed the alloy material surface corrosion with dilute hydrochloric acid; 2. carry out sandblasting with sand grains and further eliminate rust, remove stain.(6) copper-plated composition is formulated as: 1. CuSO
45H
2O 18g/L;
2. Tartaric acid potassium sodium NaKC4H4Oi4H
2O 16g/L%;
3. BDTA disodium salt 20g/L;
④NaOH??????????????????????????14g/L;
5. formaldehyde HCHO37% 16ml/L;
6. a, a
1-dipyridyl 20ml/L;
7. yellow prussiate of potash K
4(Fe (CN)
6) 10mg/L.
PH value is transferred to 12.5 with NaOH, bath temperature is risen to 46 ℃.
8. will simulate submarine and prop to container central authorities, place some of test blocks simultaneously with four fulcrums.
9. ON cycle water pump, plating bath sprays from nozzle, be full of container after, water pump continues operation, plating bath circulates in container.
Thickness of coated copper layer is controlled at 3.2~3.6 μ m.
(7) composition of plating Ni-W-P layer is formulated as:
1. select analytical pure NiSO46H for use
2O 2kg;
2. select analytical pure WSO for use
44H
2O 1.5kg;
3. select analytical pure NaH for use
2PO
2H
2O 2.5kg;
4. select analytical pure Na for use
3C
6H
6O
72kg;
5. select analytical pure NaC for use
2H
3O
21kg;
⑥(CH
2(NH
2)COOH〕??????????1kg。
With pure water above-mentioned 10kg compound is transferred to pH value 3.8 for extremely, in the plating bath pond plating bath is heated, temperature rises to 82 ℃.
(8) will simulate submarine and prop to container central authorities, place some of test blocks simultaneously with four fulcrums.
(9) ON cycle water pump, plating bath sprays from nozzle, be full of container after, water pump continues operation, plating
(10) through 30 minutes, 1h, 1.5h, 2h ... take out test block respectively, measure thickness of coating, get about 30 μ m, stopped reaction is emitted plating bath.
(11) test block and simulation submarine overlay coating are analyzed, the result is as follows:
1. thickness of coating 30 μ m;
2. the coating P content 9.2%;
3. coating contains W amount 3.6%;
4. coating density 7.92g/cm
3
5. fusing point is 890 ℃;
6. coating hardness HV520.
Test block is heated for 380 ℃, handle through 6h, hardness value reaches more than the HV1000.
7. coating corrosion resistance test:
In neutral salt spray 3000 hours, do not find corrosion.
Claims (2)
1, the present invention proposes the processing method that a kind of submarine surface anticorrosion is handled.Its characteristic is:
1) build a 2-3 doubly to the closed container of submarine, inner surface of container is industrial enamel or stainless steel, and container places the vessel space middle part with four submarines of naming a person for a particular job, and around the container several shower nozzles is arranged, and can spray into liquid and high-pressure hydraulic pump is housed and fluid circulation system.
2) processing of rust removing is made on the submarine surface, available 10% dilute hydrochloric acid solution removes corrosion.
3) be that the sand grains of 2-3mm carries out sandblasting with granularity, further remove corrosion, the stain of submarine.
4) preparation copper facing liquid, concrete composition is:
(1)CuSO
4·5H
2O???????????????10~15%;
(2) Tartaric acid potassium sodium NaKC4H4Oi4H
2O 10~20%;
(3) the BDTA disodium salt 25~40%;
(4)NaOH?????????????????????????7~15%;
(5) formaldehyde HCHO37% 10~15%;
(6) a, a
1-dipyridyl 0.05~0.1%;
(7) yellow prussiate of potash K
4(Fe (CN)
6) 20~30%.
PH value is transferred to 12.5 with NaOH, bath temperature is risen to 40-50 ℃.
With water pump plating bath is sprayed to submarine from different perspectives, make plating bath be full of container, under the effect of spraying, plating bath is in the submarine surface flow.According to the thickness requirement controlled liq spraying cycle mobile time of coating, perhaps calculate the thickness of coating on submarine surface according to the change in concentration of plating bath, the copper at submarine surface plating one deck 3~5 μ m stops to spray, and plating bath is emitted from container.Till being neutrality with pure water rinsing submarine surface to effusive water.Treat the compound plating processing of step nickel-tungsten-phosphorus down of the air-dry laggard row in submarine surface.
5) preparation Ni-W-P composite plating bath body, concrete composition is:
(1)NiSO
4·6H
2O????????????20%;
(2)WSO
4·4H
2O?????????????15%;
(3)NaH
2PO
2·H
2O??????????25%;
(4)Na
3C
6H
6O
7????????????20%;
(5)NaC
2H
3O
2??????????????10%;
(6)〔CH
2(NH
2)COOH〕???????10%。
With pure water pH value is transferred to 3.8, bath temperature is risen to 80-85 ℃.
With water pump plating bath is sprayed to submarine from different perspectives, make plating bath be full of container, under the effect of spraying, plating bath is in the submarine surface flow.According to the thickness requirement controlled liq spraying cycle mobile time of coating, perhaps go out the thickness of coating on submarine surface according to the nickel ion concentration change calculations of plating bath, when reaching thickness requirement, stop to spray, plating bath is emitted from container.
6) the Ni-W-P composite bed thickness on measurement submarine surface, and P content requires between the 7-11%, and optimum value is 9%, and containing the W amount is 3~5%, and optimum value is 4%, and all the other are Ni.
7) to the compound plating of submarine the time, put a test block identical with the submarine surfacing, the test block overlay coating is carried out physics, the anti-rotten experiment of chemistry, to infer the compound plating effect on submarine surface.
2, the processing method of handling according to claims 1 described submarine surface anticorrosion, its characteristic is:
1) build a 2-3 doubly to the closed container of submarine, inner surface of container is industrial enamel or stainless steel, and container places the vessel space middle part with four submarines of naming a person for a particular job, and around the container several shower nozzles is arranged, and can spray into liquid and high-pressure hydraulic pump is housed and fluid circulation system.
2) processing of rust removing is made on the submarine surface, available 10% dilute hydrochloric acid solution removes corrosion.
3) be that the sand grains of 2-3mm carries out sandblasting with granularity, further remove corrosion, the stain of submarine.
4) preparation copper facing liquid, concrete composition is:
(1)CuSO
4·5H
2O?????????????????15%;
(2) Tartaric acid potassium sodium NaKC4H4Oi4H
2O 10%;
(3) the BDTA disodium salt 29.9%;
(4)NaOH??????????????????????????15%;
(5) formaldehyde HCHO37% 15%;
(6) a, a
1-dipyridyl 0.1%;
(7) yellow prussiate of potash K
4(Fe (CN)
6) 15%.
PH value is transferred to 12.5 with NaOH, bath temperature is risen to 45 ℃.
With water pump plating bath is sprayed to submarine from different perspectives, make plating bath be full of container, under the effect of spraying, plating bath is in the submarine surface flow.According to the thickness requirement controlled liq spraying cycle mobile time of coating, perhaps calculate the thickness of coating on submarine surface according to the change in concentration of plating bath, the copper at submarine surface plating one deck 3.6 μ m stops to spray, and plating bath is emitted from container.Till being neutrality with pure water rinsing submarine surface to effusive water.Treat the compound plating processing of step nickel-tungsten-phosphorus down of the air-dry laggard row in submarine surface.
5) preparation Ni-W-P composite plating bath body, concrete composition is:
(1)NiSO
4·6H
2O?????????20%;
(2)WSO
4·4H
2O??????????15%;
(3)NaH
2PO
2·H
2O???????25%;
(4)Na
3C
6H
6O
7?????????20%;
(5)NaC
2H
3O
2???????????10%;
(6)〔CH
2(NH
2)COOH〕????10%。
With pure water pH value is transferred to 3.8, bath temperature is risen to 80-85 ℃.
With water pump plating bath is sprayed to submarine from different perspectives, make plating bath be full of container, under the effect of spraying, plating bath is in the submarine surface flow.According to the thickness requirement controlled liq spraying cycle mobile time of coating, perhaps go out the thickness of coating on submarine surface according to the nickel ion concentration change calculations of plating bath, when reaching thickness requirement, stop to spray, plating bath is emitted from container.
6) the Ni-W-P composite bed thickness on measurement submarine surface, and P content requires between the 7-11%, and optimum value is 9%, and containing the W amount is 3~5%, and optimum value is 4%, and all the other are Ni.
7) to the compound plating of submarine the time, put a test block identical with the submarine surfacing, the test block overlay coating is carried out physics, the anti-rotten experiment of chemistry, to infer the compound plating effect on submarine surface.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02146400 CN1287006C (en) | 2002-10-30 | 2002-10-30 | Surface anticorrusion method of submarine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02146400 CN1287006C (en) | 2002-10-30 | 2002-10-30 | Surface anticorrusion method of submarine |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1442508A true CN1442508A (en) | 2003-09-17 |
CN1287006C CN1287006C (en) | 2006-11-29 |
Family
ID=27793431
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 02146400 Expired - Fee Related CN1287006C (en) | 2002-10-30 | 2002-10-30 | Surface anticorrusion method of submarine |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1287006C (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102330077A (en) * | 2011-09-13 | 2012-01-25 | 南京航空航天大学 | Processing method and device of multilayer film by jet chemical plating |
CN102330126A (en) * | 2011-09-13 | 2012-01-25 | 南京航空航天大学 | Method and device for machining multilayer film by using multiple jet-electrodeposition |
CN104379817A (en) * | 2012-04-12 | 2015-02-25 | 诺沃皮尼奥内股份有限公司 | Method for preventing corrosion and component obtained by means of such |
-
2002
- 2002-10-30 CN CN 02146400 patent/CN1287006C/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102330077A (en) * | 2011-09-13 | 2012-01-25 | 南京航空航天大学 | Processing method and device of multilayer film by jet chemical plating |
CN102330126A (en) * | 2011-09-13 | 2012-01-25 | 南京航空航天大学 | Method and device for machining multilayer film by using multiple jet-electrodeposition |
CN104379817A (en) * | 2012-04-12 | 2015-02-25 | 诺沃皮尼奥内股份有限公司 | Method for preventing corrosion and component obtained by means of such |
US10161413B2 (en) | 2012-04-12 | 2018-12-25 | Nuovo Pignone Srl | Method for preventing corrosion and component obtained by means of such |
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Publication number | Publication date |
---|---|
CN1287006C (en) | 2006-11-29 |
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Granted publication date: 20061129 Termination date: 20091130 |