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JP5072059B2 - Cleaning method for inner surface of copper tube or copper alloy tube - Google Patents

Cleaning method for inner surface of copper tube or copper alloy tube Download PDF

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JP5072059B2
JP5072059B2 JP2005309765A JP2005309765A JP5072059B2 JP 5072059 B2 JP5072059 B2 JP 5072059B2 JP 2005309765 A JP2005309765 A JP 2005309765A JP 2005309765 A JP2005309765 A JP 2005309765A JP 5072059 B2 JP5072059 B2 JP 5072059B2
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忍 鈴木
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Sumitomo Light Metal Industries Ltd
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Description

本発明は銅管または銅合金管内面の洗浄方法、とくに長尺の銅管または銅合金管コイルの内面に形成されているカーボン皮膜を除去して均一な表面を得るために好適な銅管または銅合金管内面の洗浄方法に関する。   The present invention relates to a method for cleaning an inner surface of a copper tube or a copper alloy tube, particularly a copper tube suitable for obtaining a uniform surface by removing a carbon film formed on the inner surface of a long copper tube or copper alloy tube coil. The present invention relates to a method for cleaning the inner surface of a copper alloy tube.

銅管あるいは銅合金管は、抽伸加工時に潤滑油を使用するが、管内に残存した潤滑油は焼鈍時の加熱によって無機質の炭素質皮膜(以下、カーボン皮膜)となって管内面に残留する。カーボン皮膜の多い銅管を給水、給湯用配管として使用した場合、使用する環境によっては腐食が発生し、銅管に貫通腐食が生じて漏洩事故に至る場合もある。   A copper pipe or a copper alloy pipe uses a lubricating oil at the time of drawing, but the lubricating oil remaining in the pipe becomes an inorganic carbonaceous film (hereinafter referred to as a carbon film) by heating during annealing and remains on the inner surface of the pipe. When a copper pipe with a lot of carbon film is used as piping for water supply or hot water supply, corrosion may occur depending on the environment used, and through corrosion may occur in the copper pipe, leading to a leakage accident.

このような銅管の腐食対策として、銅管の内面にスズめっき皮膜を形成する方法が知られており、特にコイル状の長尺銅管内面にスズめっき皮膜を形成するため、置換型無電解スズめっき液を銅管内部に通液させるめっき処理方法が提案されている(例えば、特許文献1)。   As a countermeasure against corrosion of such copper pipes, a method of forming a tin plating film on the inner surface of the copper pipe is known. In particular, since a tin plating film is formed on the inner surface of a coiled long copper pipe, a substitution type electroless There has been proposed a plating method in which a tin plating solution is passed through a copper tube (for example, Patent Document 1).

良好な耐食性を得るために、密着性に優れたスズめっき皮膜を形成するには、めっきを施す前に管内のカーボン皮膜を除去することが重要であり、その手法として、管内に不活性ガスを流通させて熱処理を行う方法(例えば、特許文献2)が提案されているが、この手法は密着性に優れたスズめっき皮膜を得るためには必ずしも十分ではなく、薬液による化学的処理との併用も検討されている。   In order to form a tin plating film with excellent adhesion in order to obtain good corrosion resistance, it is important to remove the carbon film in the tube before plating. A method of performing heat treatment by distribution (for example, Patent Document 2) has been proposed, but this method is not always sufficient for obtaining a tin plating film having excellent adhesion, and combined with chemical treatment with a chemical solution. Has also been considered.

カーボン皮膜は、管内表面に強固に付着しており、無機質であることから有機系洗浄剤あるいは界面活性剤では除去できないため、管内表層を溶解させてこれと共に除去する方法以外になく、また、銅や銅合金は水素より自然電位が貴であり、硫酸や塩酸のような酸では溶解することができないから、酸化性を有する酸、例えば、硝酸や硫酸に過酸化水素を添加した混酸を使用してカーボン皮膜を除去し、管内表面を活性して金属の活性面を得る方法が試みられている。   Since the carbon film is firmly attached to the inner surface of the tube and is inorganic, it cannot be removed with an organic cleaning agent or surfactant. Therefore, there is no method other than dissolving the inner surface of the tube and removing it together with copper. Since copper and copper alloys have a higher natural potential than hydrogen and cannot be dissolved with acids such as sulfuric acid and hydrochloric acid, use an acid that has an oxidizing property, for example, a mixed acid obtained by adding hydrogen peroxide to nitric acid or sulfuric acid. Attempts have been made to obtain a metal active surface by removing the carbon film and activating the inner surface of the tube.

しかしながら、これらの酸は銅の溶解反応において有害なガスを発生させるため、数百メートルに及ぶ長尺コイルに通液した場合には発生したガスで管内の圧力が上昇して洗浄液通液用に長尺コイル両管端に取り付けた送液管(ホース等)が抜ける懸念があり、作業の安全性に問題があるため、長尺コイル内面の洗浄においては、銅との反応でガスが発生しない組成の洗浄液を用いる必要があった。   However, since these acids generate harmful gases in the copper dissolution reaction, when they are passed through a long coil of several hundred meters, the generated gas increases the pressure in the tube and allows the cleaning liquid to pass. There is a concern that the liquid supply pipes (hose etc.) attached to both ends of the long coil may come off, and there is a problem with the safety of the work. Therefore, no gas is generated by the reaction with copper in cleaning the long coil inner surface. It was necessary to use a cleaning solution having a composition.

一方、硫酸と無水クロム酸からなる洗浄液は銅の洗浄液として知られており、銅との反応においてもガスの発生はなく、洗浄性(カーボン皮膜の除去、表面の均一性)も優れているが、銅との反応では水素イオンが必要となるため、密閉状態で反応が進行する長尺コイル内では洗浄液各成分の補給ができずに長尺コイルの途中で反応が終了する。このため、洗浄可能な長尺コイル長さに限界があり、また、この反応は発熱反応であり洗浄液の流通とともに洗浄液の液温が上昇するから、より早く反応が進行して、長尺コイルの全長を均一に洗浄できないという難点もある。従って、硫酸、無水クロム酸から成る洗浄液を使う場合は、コイルの長さを短くするか、洗浄液の通液方向を逆転させ、且つコイルの温度上昇を抑えるための設備も必要となり実用的ではない。
特開平4-45282号公報 特開平8-81780号公報
On the other hand, a cleaning solution composed of sulfuric acid and chromic anhydride is known as a cleaning solution for copper, and no gas is generated in the reaction with copper, and the cleaning property (removal of carbon film, surface uniformity) is excellent. Since hydrogen ions are required for the reaction with copper, the components of the cleaning solution cannot be replenished in the long coil where the reaction proceeds in a sealed state, and the reaction ends in the middle of the long coil. For this reason, there is a limit to the length of the long coil that can be cleaned, and this reaction is an exothermic reaction, and the temperature of the cleaning liquid rises with the circulation of the cleaning liquid. There is also a drawback that the entire length cannot be cleaned uniformly. Therefore, when using a cleaning solution made of sulfuric acid or chromic anhydride, it is not practical because the length of the coil is shortened or the flow direction of the cleaning solution is reversed and equipment for suppressing the temperature rise of the coil is required. .
Japanese Patent Laid-Open No. 4-45282 JP-A-8-81780

本発明は、銅管または銅合金管内面に形成されたカーボン皮膜を除去する場合における上記従来の問題点を解消するためになされたものであり、その目的は、特別な設備を使用せずに銅管または銅合金管内面のカーボン皮膜を低減させることができ、とくに長尺の銅管または銅合金管コイルの内面に形成されているカーボン皮膜を除去して均一な金属活性面を得るために好適な銅管または銅合金管内面の洗浄方法を提供することにある。当該洗浄方法はまた、銅管または銅合金管内面への無電解スズめっき処理の前処理として有効である。   The present invention has been made to solve the above-mentioned conventional problems in removing the carbon film formed on the inner surface of a copper tube or a copper alloy tube, and the purpose thereof is to use no special equipment. To reduce the carbon film on the inner surface of a copper tube or copper alloy tube, especially to remove the carbon film formed on the inner surface of a long copper tube or copper alloy tube coil to obtain a uniform metal active surface An object of the present invention is to provide a method for cleaning the inner surface of a suitable copper tube or copper alloy tube. The cleaning method is also effective as a pretreatment for electroless tin plating on the inner surface of a copper tube or a copper alloy tube.

上記の目的を達成するための請求項1による銅管または銅合金管内面の洗浄方法は、硫酸と、酸化剤として硫酸第二鉄を含有する洗浄液をコイル状の長尺銅管または銅合金管内に通液させて管内面を洗浄することを特徴とする。 The method for cleaning the inner surface of a copper tube or a copper alloy tube according to claim 1 for achieving the above object is characterized in that a cleaning solution containing sulfuric acid and ferric sulfate as an oxidizing agent is used in a coiled long copper tube or copper alloy tube. It is characterized in that the inner surface of the pipe is washed by letting it pass through.

請求項2による銅管または銅合金管内面の洗浄方法は、硫酸と、酸化剤としてペルオキソ二硫酸ナトリウムを含有する洗浄液をコイル状の長尺銅管または銅合金管内に通液させて管内面を洗浄することを特徴とする。 According to a second aspect of the present invention, there is provided a method for cleaning an inner surface of a copper tube or a copper alloy tube by passing a cleaning solution containing sulfuric acid and sodium peroxodisulfate as an oxidizing agent through a coiled long copper tube or copper alloy tube. It is characterized by washing.

請求項3による銅管または銅合金管内面の洗浄方法は、請求項1または2において、前記洗浄液に界面活性剤が添加されていることを特徴とする。   According to a third aspect of the present invention, there is provided a method for cleaning an inner surface of a copper pipe or a copper alloy pipe according to the first or second aspect, wherein a surfactant is added to the cleaning liquid.

請求項による銅管または銅合金管内面の洗浄方法は、請求項1〜3のいずれかにおいて、銅管または銅合金管内面への無電解スズめっき処理の前処理であることを特徴とする。 A method for cleaning an inner surface of a copper tube or a copper alloy tube according to claim 4 is a pretreatment for electroless tin plating on the inner surface of a copper tube or a copper alloy tube according to any one of claims 1 to 3. .

本発明によれば、特別な設備を使用せずに銅管または銅合金管内面のカーボン皮膜を低減させることができ、とくに長尺の銅管または銅合金管コイルの内面に形成されているカーボン皮膜を除去して均一な金属活性面を得るために好適な銅管または銅合金管内面の洗浄方法が提供される。当該洗浄方法はまた、銅管または銅合金管内面への無電解スズめっき処理の前処理として有効である。   According to the present invention, the carbon film on the inner surface of a copper tube or a copper alloy tube can be reduced without using special equipment, and in particular, the carbon formed on the inner surface of a long copper tube or copper alloy tube coil A method for cleaning the inner surface of a copper tube or copper alloy tube suitable for removing the coating to obtain a uniform metal active surface is provided. The cleaning method is also effective as a pretreatment for electroless tin plating on the inner surface of a copper tube or a copper alloy tube.

第二鉄塩としては、硫酸第二鉄、塩化第二鉄、水酸化第二鉄などが挙げられる。本発明を、銅管または銅合金管内面への無電解スズめっき処理の前処理として適用する場合には、前処理である洗浄工程に続いて実施される無電解置換スズめっき処理のめっき液が、通常、硫酸酸性であるから、めっき液との組み合わせにおいて硫酸第二鉄を使用するのが望ましい。 Examples of the ferric salt include ferric sulfate, ferric chloride, and ferric hydroxide. When the present invention is applied as a pretreatment for electroless tin plating on the inner surface of a copper tube or a copper alloy tube, a plating solution for electroless substitution tin plating that is carried out following the cleaning step that is the pretreatment is provided. Since it is usually sulfuric acid acid, it is desirable to use ferric sulfate in combination with the plating solution.

ペルオキソ二硫酸塩としては、ペルオキソ二硫酸ナトリウム、ペルオキソ二硫酸カリウム、ペルオキソ二硫酸アンモニウムなどが挙げられるが、ペルオキソ二硫酸カリウムは水への溶解度が低く、ペルオキソ二硫酸アンモニウムはアンモニウム塩であり排水処理の観点で窒素源が増して排水処理負荷が増大するという問題があるため、ペルオキソ二硫酸ナトリウムを使用するのがより好ましい。   Examples of peroxodisulfate include sodium peroxodisulfate, potassium peroxodisulfate, and ammonium peroxodisulfate. However, potassium peroxodisulfate has low solubility in water, and ammonium peroxodisulfate is an ammonium salt. Therefore, it is more preferable to use sodium peroxodisulfate because the nitrogen source increases and the wastewater treatment load increases.

硫酸第二鉄、ペルオキソ二硫酸ナトリウムの濃度範囲は、管の長さ、管径および流通用ポンプ能力に基づく流速等によって変わるため、被洗浄管、洗浄設備に適した範囲を適宜選定する。また、各酸化剤および溶解した銅の溶解能を高めるため、硫酸を添加した酸性溶液に上記の酸化剤を添加することが望ましい。 Since the concentration range of ferric sulfate and sodium peroxodisulfate varies depending on the length of the pipe, the pipe diameter, the flow rate based on the flow pump capacity, and the like, a range suitable for the pipe to be cleaned and the cleaning equipment is appropriately selected. Moreover, in order to improve the dissolving ability of each oxidizing agent and dissolved copper, it is desirable to add the above oxidizing agent to an acidic solution to which sulfuric acid has been added.

界面活性剤としては、アニオン系界面活性剤、カチオン系界面活性剤、非イオン系界面活性剤の中で、酸性溶液中でも安定に存在し、且つ汎用的な非イオン系界面活性剤を使用するのが望ましく、その濃度範囲は0.1〜10g/Lが好ましい。金属洗浄時の経験的な適用濃度からみて1g/L程度の濃度での使用が最も適切である。   As the surfactant, an anionic surfactant, a cationic surfactant, and a nonionic surfactant, which is stably present even in an acidic solution, and a general-purpose nonionic surfactant is used. The concentration range is preferably 0.1 to 10 g / L. In view of empirically applied concentration during metal cleaning, use at a concentration of about 1 g / L is most appropriate.

以下、本発明の実施例を比較例と対比して説明し、その効果を実証する。なお、これらの実施例は、本発明の一実施態様を示すものであり、本発明はこれらに限定されるものではない。   Examples of the present invention will be described below in comparison with comparative examples to demonstrate the effects. In addition, these Examples show one embodiment of this invention, and this invention is not limited to these.

実施例1、比較例1
厚さ0.5mm、幅20mm、長さ80mmのリン脱酸銅板を被洗浄材とし、表1に示す各洗浄液(液温:30℃)に100分間浸漬して銅板表面からのガス発生の有無を確認した。結果を表1に示す。
Example 1, Comparative Example 1
A phosphorus deoxidized copper plate with a thickness of 0.5mm, width 20mm, and length 80mm is used as the material to be cleaned, and immersed in each cleaning solution shown in Table 1 (liquid temperature: 30 ° C) for 100 minutes to check for gas generation from the copper plate surface. confirmed. The results are shown in Table 1.

表1に示すように、本発明に従う試験No.1、2においてはいずれもガスの発生が認められなかった。これに対して、硫酸と過酸化水素水からなる洗浄液を用いた試験No.3、硫酸と硝酸からなる洗浄液を用いた試験No.4においてはガスが発生した。   As shown in Table 1, in Test Nos. 1 and 2 according to the present invention, no gas generation was observed. On the other hand, gas was generated in test No. 3 using a cleaning liquid consisting of sulfuric acid and hydrogen peroxide, and in test No. 4 using a cleaning liquid consisting of sulfuric acid and nitric acid.

Figure 0005072059
Figure 0005072059

実施例2
管内に不活性ガスを流通させて熱処理を施すことによりカーボン皮膜を除去した外径15.88mm、肉厚0.71mm、長さ100mのコイル状のリン脱酸銅管を直列に6ヶ接続したものを被処理材とし、被処理材の片管端より、98%硫酸:15g/L、41%硫酸第二鉄溶液:200g/L、界面活性剤:1g/Lからなる洗浄液を20℃に温調して50min間の循環通液を行った。その後、十分に水洗し、管内の水洗水はエアーブローにて排出した。
Example 2
6 pipes connected in series with coiled phosphorous deoxidized copper tubes with an outer diameter of 15.88mm, wall thickness of 0.71mm, and length of 100m, from which an inert gas was circulated and subjected to heat treatment. As the material to be treated, the temperature of the cleaning solution consisting of 98% sulfuric acid: 15 g / L, 41% ferric sulfate solution: 200 g / L, and surfactant: 1 g / L is adjusted to 20 ° C from the end of one tube of the material to be treated. Then, circulation was performed for 50 minutes. Thereafter, it was sufficiently washed with water, and the washing water in the pipe was discharged by air blow.

次いで、市販の置換型無電解スズめっき液(例えば、第一スズ塩:0.1mol/L、有機イオウ化合物:1mol/L、有機カルホン酸塩:0.1mol/L、硫酸:0.5mol/L、芳香族スルホン酸塩:0.2mol/L、非界面活性剤:1g/L)を用いて、液温30℃で30minのめっき処理を施す第1のめっき処理に続き、液温を70℃として100minのめっき処理を施す第2のめっき処理を行ってスズめっき皮膜を形成させた。第2のめっき処理終了後には十分に水洗してエアーブロー乾燥した。   Subsequently, a commercially available substitutional electroless tin plating solution (for example, stannous salt: 0.1 mol / L, organic sulfur compound: 1 mol / L, organic carbonate: 0.1 mol / L, sulfuric acid: 0.5 mol / L, aroma Group sulfonate: 0.2 mol / L, non-surfactant: 1 g / L), followed by the first plating process for 30 minutes at a liquid temperature of 30 ° C, followed by 100 minutes at a liquid temperature of 70 ° C. A tin plating film was formed by performing a second plating process for plating. After the completion of the second plating treatment, it was sufficiently washed with water and air blow dried.

洗浄液の通液中には長尺コイルの洗浄液流出側にて洗浄液の温度を測定し、洗浄が終了して水洗、エアーブローにより管内の水洗水を排出した後には洗浄液のコイル導入側から0m、300m、400m、500m、600m(洗浄液流出側に相当)より抜管して、銅管内面のカーボン皮膜の付着状況を洗浄前の同位置と比較した。   During the flow of the cleaning liquid, measure the temperature of the cleaning liquid at the cleaning liquid outflow side of the long coil.After the cleaning is completed, the water is washed, and after the flushing water in the pipe is discharged by air blow, 0m from the coil introduction side of the cleaning liquid Pipes were removed from 300m, 400m, 500m, and 600m (corresponding to the washing liquid outflow side), and the adhesion of the carbon film on the inner surface of the copper pipe was compared with the same position before washing.

カーボン皮膜の付着状況は次に示す方法にて行った。すなわち、各位置のサンプルを1mに切断し、塩酸、硝酸からなる混酸により管内表面を溶解させると共にカーボン皮膜を除去し、これを捕集して赤外線吸収法によってカーボン量を測定した。洗浄後のカーボン皮膜の付着状況は、洗浄後のカーボン量を洗浄前のカーボン量で徐した残存割合にて確認した。なお、洗浄前の長尺コイル各位置のカーボン皮膜の付着量は2〜4mg/m2であった。 The carbon film was adhered by the following method. That is, the sample at each position was cut to 1 m, the inner surface of the tube was dissolved with a mixed acid composed of hydrochloric acid and nitric acid, the carbon film was removed, and this was collected and the amount of carbon was measured by an infrared absorption method. The adhesion state of the carbon film after the cleaning was confirmed by a residual ratio in which the carbon amount after the cleaning was gradually reduced by the carbon amount before the cleaning. In addition, the adhesion amount of the carbon film at each position of the long coil before cleaning was 2 to 4 mg / m 2 .

スズめっき後、長尺コイルのめっき液導入側から0m、300m、400m、500m、600m(出側に相当)より抜管して、以下に示す方法によりスズめっき皮膜厚さ、ピンホール数の測定を行ない、スズめっき皮膜特性を評価した。結果を表2に示す。   After tin plating, extrude from 0m, 300m, 400m, 500m, 600m (equivalent to the outlet side) from the plating solution introduction side of the long coil, and measure the thickness of tin plating film and the number of pinholes by the following methods The tin plating film characteristics were evaluated. The results are shown in Table 2.

スズめっき皮膜厚さの測定:(株)中央製作所製電解式めっき膜厚測定器TH-10Pを用いて測定した。
ピンホール数測定:28%アンモニア水270mL/L、ペルオキソ二硫酸アンモニウム135g/Lからなる溶液を、スズめっき処理した試験材(長さ10cm)に充填し、室温に1時間放置後、水洗、乾燥した。試験材を長手方向に半割りにした後、スズめっき皮膜をテープ(ニットーNo.31B)で剥離させ、銅の点状露出部分をピンホールとして顕微鏡にて観察し、1cm2当たりでの最多発生数を計数した。
Measurement of tin plating film thickness: It was measured using an electrolytic plating film thickness measuring instrument TH-10P manufactured by Chuo Seisakusho.
Pinhole number measurement: A solution consisting of 270 mL / L of 28% ammonia water and 135 g / L of ammonium peroxodisulfate was filled in a tin-plated test material (length: 10 cm), left at room temperature for 1 hour, washed with water and dried. . After the test material was halved in the longitudinal direction, the tin plating film was peeled off with tape (Nitto No. 31B), and the copper spot-like exposed part was observed with a microscope as a pinhole, and the maximum occurrence per cm 2 Numbers were counted.

表2に示すように、長尺コイルの洗浄液流出側の洗浄液温度は24℃で、外気温(22℃)、送液用のポンプの発熱を勘案すれば、洗浄による発熱はほとんどない。また、洗浄後の長尺コイル各位置のカーボン皮膜除去程度は、長尺コイルの全長にわたり洗浄前の40%以下であり、スズめっきを行うに際して十分なまでに除去された。スズめっき後のスズめっき皮膜のピンホール数はめっき液の導入側から流出側まで皆無であり、密着性に優れたスズめっき皮膜が形成された。   As shown in Table 2, the cleaning solution temperature on the outflow side of the long coil is 24 ° C., and considering the outside air temperature (22 ° C.) and the heat generation of the pump for feeding liquid, there is almost no heat generation due to cleaning. The degree of carbon film removal at each position of the long coil after cleaning was 40% or less before the cleaning over the entire length of the long coil, which was sufficiently removed when tin plating was performed. The number of pinholes in the tin plating film after tin plating was completely absent from the plating solution introduction side to the outflow side, and a tin plating film having excellent adhesion was formed.

なお、洗浄液の主剤として、前記41%硫酸第二鉄溶液に代えて、ペルオキソ二硫酸ナトリウム:100g/Lを用い、前記実施例2と同一条件にて洗浄した後、スズめっきを行ったところ、同様に、洗浄性(洗浄中の温度上昇、カーボン皮膜の除去状況)およびめっき性(スズめっき皮膜厚さ、ピンホール数)共に良好な結果が得られた。   In addition, instead of the 41% ferric sulfate solution as the main component of the cleaning solution, sodium peroxodisulfate: 100 g / L was used, and after washing under the same conditions as in Example 2, tin plating was performed. Similarly, good results were obtained for both cleaning properties (temperature rise during cleaning, carbon film removal status) and plating properties (thin plating film thickness, number of pinholes).

Figure 0005072059
Figure 0005072059

比較例2
実施例2と同一条件により製造した外径15.88mm、肉厚0.71mm、長さ600mのコイル状のリン脱酸銅管に、98%硫酸15g/L、無水クロム酸50g/Lからなる洗浄液を、実施例2と同じ条件にて循環通液した。洗浄後、実施例2と同じめっき液、条件にてスズめっき処理を行った後、実施例2と同様の方法で、洗浄中の長尺コイル洗浄液流出側の洗浄液温度、洗浄後のカーボン皮膜除去状況を確認し、めっき後にはスズ皮膜厚さ、ピンホール数を測定した。結果を表3に示す。
Comparative Example 2
A coiled phosphorous deoxidized copper tube with an outer diameter of 15.88 mm, a wall thickness of 0.71 mm, and a length of 600 m manufactured under the same conditions as in Example 2 was washed with a cleaning solution consisting of 98% sulfuric acid 15 g / L and chromic anhydride 50 g / L. The liquid was circulated under the same conditions as in Example 2. After cleaning, after performing tin plating treatment with the same plating solution and conditions as in Example 2, the cleaning solution temperature on the outflow side of the long coil cleaning solution during cleaning, removal of the carbon film after cleaning, in the same manner as in Example 2 The situation was confirmed, and after plating, the thickness of the tin film and the number of pinholes were measured. The results are shown in Table 3.

表3に示すように、洗浄中には銅溶解反応によって洗浄液が発熱し、洗浄液流出側にて10℃の温度上昇が認められた。また、カーボン皮膜は、水素イオンの消耗によって銅溶解反応が終了するため、長尺コイルの中央以降ではカーボン皮膜の残存割合が増加した。ピンホール数は、洗浄によってカーボン皮膜の除去が不十分となった長尺コイル中央以降で20個/cm2となり、密着性に乏しいスズめっき皮膜が形成された。 As shown in Table 3, during the cleaning, the cleaning solution generated heat due to the copper dissolution reaction, and a temperature increase of 10 ° C. was observed on the cleaning solution outflow side. In addition, since the copper dissolution reaction of the carbon film was terminated by the consumption of hydrogen ions, the remaining ratio of the carbon film increased after the center of the long coil. The number of pinholes was 20 / cm 2 after the center of the long coil where the carbon film was not sufficiently removed by washing, and a tin plating film with poor adhesion was formed.

Figure 0005072059
Figure 0005072059

Claims (4)

硫酸と、酸化剤として硫酸第二鉄を含有する洗浄液をコイル状の長尺銅管または銅合金管内に通液させて管内面を洗浄することを特徴とする銅管または銅合金管内面の洗浄方法。 Cleaning the inner surface of a copper tube or copper alloy tube, characterized by passing a cleaning solution containing sulfuric acid and ferric sulfate as an oxidizing agent through a coiled long copper tube or copper alloy tube to clean the inner surface of the tube Method. 硫酸と、酸化剤としてペルオキソ二硫酸ナトリウムを含有する洗浄液をコイル状の長尺銅管または銅合金管内に通液させて管内面を洗浄することを特徴とする銅管または銅合金管内面の洗浄方法。 Cleaning of the inner surface of a copper tube or copper alloy tube characterized by passing a cleaning solution containing sulfuric acid and sodium peroxodisulfate as an oxidizing agent through a coiled long copper tube or copper alloy tube to clean the inner surface of the tube Method. 前記洗浄液に界面活性剤が添加されていることを特徴とする請求項1または2に記載の銅管または銅合金管内面の洗浄方法。 The method for cleaning an inner surface of a copper tube or a copper alloy tube according to claim 1, wherein a surfactant is added to the cleaning solution. 銅管または銅合金管内面への無電解スズめっき処理の前処理であることを特徴とする請求項1〜3のいずれかに記載の銅管または銅合金管内面の洗浄方法。 The method for cleaning an inner surface of a copper tube or a copper alloy tube according to any one of claims 1 to 3 , wherein the inner surface of the copper tube or the copper alloy tube is a pretreatment for an electroless tin plating process.
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