TW200927999A - Acid solution and magnesium alloy phosphating method using the same - Google Patents

Acid solution and magnesium alloy phosphating method using the same Download PDF

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TW200927999A
TW200927999A TW96151313A TW96151313A TW200927999A TW 200927999 A TW200927999 A TW 200927999A TW 96151313 A TW96151313 A TW 96151313A TW 96151313 A TW96151313 A TW 96151313A TW 200927999 A TW200927999 A TW 200927999A
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magnesium alloy
concentration
solution
pickling
phosphating
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TW96151313A
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Chinese (zh)
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TWI359211B (en
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Sheng-En Hsu
Yong Liu
Fei-Xiang Li
Zhao Jin
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Hon Hai Prec Ind Co Ltd
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Abstract

The present invention relates to an acid solution used in a magnesium alloy phosphating method. The acid solution includes citric acid and no-silicon water-solubility surfactant. The concentration of the citric acid is in a range from 5 g/L to 30 g/L in the acid solution, the concentration of no-silicon water-solubility surfactant is in a range from 1. 5 g/L to 6 g/L in the acid solution. A method of magnesium alloy phosphating using the acid solution is also provided. Ash generated on surfaces of the magnesium alloy perform can be removed or reduced when the magnesium alloy perform is processed in the acid solution.

Description

200927999 九、發明說明: 【發明所屬之技術領域】 * 本發明涉及一種鎂合金磷化方法及其酸洗溶液。 【先前技術】 鎂合金輕材料因為比重低、強度高且適合回收使用而 廣泛應用於汽車及電器設備。,准,由於鎮合金化學性質較 為活潑,耐腐蝕性能較差,故鎂合金工件於使用前一般需 ❹要於其表面形成抗腐⑽,該抗腐㈣需具有良好之^ 霧性能、較高之附著力及較小之表面阻抗。 習知技術中,一般藉由磷化方法於鎂合金工件表面形 成一層緻密之磷化膜,以提高其抗腐蝕性。一種習知之鎂 合金磷化方法,包括酸洗之工藝步驟’酸洗之主要作用係 除去鎂合金工件表面之氧化物及壓鑄成型時喷塗之離型 劑,增加鎮合金工件表面粗链度 '然,習知之酸洗工藝中, 於鎂合金工件表面易產生黑灰物質(主要成分為鋁與^), 〇而黑灰物質於後續鹼洗工藝時不易全部去除,故會導致後 續生成之磷化膜出現顏色不均勻、局部顏色發黑甚至鎮合 金工件表面有浮灰等缺陷。 【發明内容】 鑒於上述狀況,有必要提供一種可避免或減少於鎂合 金工件表面形成黑灰物質之鎮合金磷化方法及其酸洗= 液。 ' 一種用於鎮合金魏卫藝之酸洗溶液,其包括摔樣酸 與無矽水溶性表面活性劑,其中檸檬酸於該酸洗溶液中之 200927999 濃度為5至3G克/升’無石夕水溶性表面活性劑於該酸洗溶 液中之濃度為1.5至6克/升。 ' 種鎂°金磷化方法’依次包括酸洗、驗洗及化成形 成填化膜之工藝步驟,其中於酸洗步驟採用一酸洗溶液, 該酸洗溶液包括檸檬酸與無石夕水溶性表面活性劑,摔樣酸 於該酸洗溶液中之濃度為5至3G七升,無料溶性表面 活性劑於該酸洗溶液中之濃度為15至6克/升。 上述鎮合金磷化方法中,藉由控制酸洗溶液之組成, ❹使得鎮合金卫件表面之氧化物及離型劑得以完全去除之同 時’還可避免或減少於該鎮合金工件表面形成黑灰物質。 【實施方式】 下面將結合附圖及實施例對本發明鎂合金工件及鎂 合金填化方法做進一步詳細說明。 請參見圖1 ’所示為本發明較佳實施方式之鎂合金磷 化方法之流程圖,其包括以下步驟: _ 步驟10,提供一鎂合金預基材; 步驟20,脫脂,用除油溶液去除該鎂合金預基材表面 之油污; 步驟30,酸洗,用酸洗溶液去除該鎂合金預基材表面 之氧化物與離型劑; 步驟40’鹼洗,用鹼洗溶液去除該鎂合金預基材表面 之黑灰物質; 步驟50’化成,用化成溶液於該鎂合金預基材表面形 成碟化臈。 200927999 步驟20中,脫脂時間可控制於4至8分鐘,脫脂溫 : 度可控制於55至65°C。該除油溶液可為氳氧化鈉(NaOH) - 或磷酸鈉(Na3P04)之水溶液。脫脂過程主要係用於去除該 鎂合金預基材表面之機油、切削油等有機油。可以理解, 於該鎂合金預基材先經過喷砂等方式處理後,鎂合金預基 材表面沒有油污,則該步驟20可省略。 步驟30中,酸洗時間可控制於3至5分鐘,酸洗溫 度可控制於35至45°C。本實施例中,該酸洗溶液包括濃 ®度為 5 至 30 克/升之檸檬酸(工業級) (HOOCCH2C(OH)(COOH)CH2COOH)與濃度為 1.5 至 6 克/ 升之無砍水溶性表面活性劑(工業級)。 擰檬酸可與鎂合金預基材表面之氧化物及壓鑄成型 時喷塗之離型劑反應,以去除該氧化物及離型劑。其可除 去之氧化物包括氧化鎂(MgO)、氧化鋁(Al2〇3)以及氧化鋅 (ZnO)等;其可除去之離型劑包括高矽脂有機物 ❹((CH2)m-CH(Si)n-COOR),其中R為曱基等官能團。擰檬酸 於該酸洗溶液中可同時避免或減少於該鎂合金預基材表面 形成黑灰物質。檸檬酸於該酸洗溶液之濃度優選為8至15 克/升。於酸洗步驟中,檸檬酸主要發生以下化學反應:200927999 IX. Description of the invention: [Technical field to which the invention pertains] * The present invention relates to a magnesium alloy phosphating method and an acid washing solution thereof. [Prior Art] Magnesium alloy light materials are widely used in automobiles and electrical equipment because of their low specific gravity, high strength and suitable for recycling. , quasi-, because the town alloy chemical properties are more active, corrosion resistance is poor, so magnesium alloy parts generally need to form anti-corrosion on the surface before use (10), the anti-corrosion (four) needs to have good fog performance, higher Adhesion and small surface impedance. In the prior art, a dense phosphating film is generally formed on the surface of a magnesium alloy workpiece by a phosphating method to improve its corrosion resistance. A conventional magnesium alloy phosphating method, including the pickling process step 'the main function of the pickling is to remove the oxide on the surface of the magnesium alloy workpiece and the release agent sprayed during the die casting, and increase the surface roughness of the alloy workpiece surface' However, in the conventional pickling process, black ash substances (main components are aluminum and ^) are easily generated on the surface of the magnesium alloy workpiece, and the black ash material is not easily removed in the subsequent alkali washing process, so that the subsequent phosphorus is formed. The film has uneven color, black color of the local color, and even defects such as floating ash on the surface of the alloy workpiece. SUMMARY OF THE INVENTION In view of the above circumstances, it is necessary to provide a town alloy phosphating method and a pickling liquid which can avoid or reduce the formation of a black ash substance on the surface of a magnesium alloy workpiece. A pickling solution for Zhenwei Weiweiyi, which comprises a splashing acid and a flawless water-soluble surfactant, wherein the concentration of citric acid in the pickling solution is 5 to 3 g/liter in the 200927999 solution. The concentration of the surfactant in the pickling solution is from 1.5 to 6 g/liter. The 'magnesium-gold phosphating method' comprises the steps of pickling, washing and forming into a filled film, wherein the pickling step uses an acid washing solution comprising citric acid and no water-soluble liquid. The surfactant, the concentration of the falling acid in the pickling solution is 5 to 3 G seven liters, and the concentration of the non-soluble surfactant in the pickling solution is 15 to 6 g/liter. In the above-mentioned town alloy phosphating method, by controlling the composition of the pickling solution, the cerium can completely remove the oxide and the releasing agent on the surface of the alloy alloy member, and can also avoid or reduce the formation of black on the surface of the alloy workpiece. Gray matter. [Embodiment] Hereinafter, a magnesium alloy workpiece and a magnesium alloy filling method of the present invention will be further described in detail with reference to the accompanying drawings and embodiments. 1 is a flow chart showing a magnesium alloy phosphating method according to a preferred embodiment of the present invention, which comprises the following steps: _ Step 10, providing a magnesium alloy pre-substrate; Step 20, degreasing, using a degreasing solution Removing the oil stain on the surface of the magnesium alloy pre-substrate; Step 30, pickling, removing the oxide and release agent on the surface of the magnesium alloy pre-substrate with an acid pick-up solution; Step 40' alkaline washing, removing the magnesium with an alkali washing solution The black ash material on the surface of the alloy pre-substrate; the step 50' is formed, and a bismuth is formed on the surface of the magnesium alloy pre-substrate by using a chemical conversion solution. 200927999 In step 20, the degreasing time can be controlled from 4 to 8 minutes, and the degreasing temperature can be controlled from 55 to 65 °C. The degreasing solution may be an aqueous solution of sodium cerium oxide (NaOH) or sodium phosphate (Na3P04). The degreasing process is mainly used to remove organic oil such as engine oil and cutting oil on the surface of the pre-base of the magnesium alloy. It can be understood that the step 20 can be omitted after the magnesium alloy pre-substrate is treated by sand blasting or the like, and the surface of the magnesium alloy pre-base is free of oil. In step 30, the pickling time can be controlled from 3 to 5 minutes, and the pickling temperature can be controlled from 35 to 45 °C. In this embodiment, the pickling solution comprises citric acid (industrial grade) (HOOCCH2C(OH)(COOH)CH2COOH) having a concentration of 5 to 30 g/l and a non-cutting water concentration of 1.5 to 6 g/l. Surfactant (industrial grade). The citric acid can be reacted with the oxide of the surface of the magnesium alloy pre-substrate and the release agent sprayed during the die-casting to remove the oxide and the release agent. The oxides which can be removed include magnesium oxide (MgO), aluminum oxide (Al2〇3), and zinc oxide (ZnO), etc.; the removable release agent includes sorghum organic matter (((CH2)m-CH(Si) n-COOR), wherein R is a functional group such as a thiol group. The citric acid in the pickling solution can simultaneously avoid or reduce the formation of black ash material on the surface of the magnesium alloy pre-substrate. The concentration of citric acid in the pickling solution is preferably from 8 to 15 g/l. In the pickling step, citric acid mainly undergoes the following chemical reactions:

Mg0 + 2H+=Mg2+ + H20 ; Α12〇3 + 6Η+=2Α13+ + 3Η20 ;Mg0 + 2H+=Mg2+ + H20; Α12〇3 + 6Η+=2Α13+ + 3Η20;

Zn0 + 2H+ = Zn2++H20 ;Zn0 + 2H+ = Zn2++H20 ;

Mg + 2H+=Mg2++H2 ; 200927999 無矽水溶性表面活性劑用於使鎂合金工件表面反應 更加均勻,同時降低反應速度,使擰檬酸發生之反應更易 控制,從而進一步避免或減少酸洗過程中於鎂合金工件表 面發生過度腐钱而生成黑灰物質。該無矽水溶:表面活性 劑為低泡無矽水溶性非離子型表面活性劑,其親水基主要 係羥基。該無矽水溶性表面活性劑可為多元醇,例二聚乙 二醇、甘油、季戊四醇、蔗糖、葡萄糖、 反應更均勻及避免浪費’無石夕水溶性表面 Ο 液中之濃度優選為3至4克/升。 山梨醇等。為使 活性劑於酸洗溶 於步驟40中,鹼洗之時間可為3至5分鐘,鹼洗之 溫度可為60至80〇C。該鹼洗溶液中之鹼可為氫氧化鉀 (KOH)或氫氧化鈉(NaOH)。 鹼洗用於與鎂合金預基材表面之黑灰物質反應,用以 除去黑灰物質,使鎂合金基材暴露出來。若採用工業級之 氫氧化鉀,其於該鹼洗溶液中之濃度可為6〇至18〇克/升; 〇為使黑灰物質完全除去及避免後續磷化膜表面局部發黑及 避免後續生成之填化膜之表面阻抗偏大,氫氧化鉀於該驗 洗;谷液中之/農度優選為1〇〇至150克/升。氫氧化卸主要發 生以下化學反應: 6ΚΟΗ+2Α1=2Κ3Α1〇3 + 3Η2 ; 2K0H+Zn=K2Zn02+H2。 於步驟50中’化成之時間可為3〇至50秒,化成之 溫度可為35至45。(:。化成形成於該鎂合金預基材表面之 填化膜居度可為5至30微米,該鎂合金預基材之表面阻抗 200927999 可小於2歐姆。該化成溶液可包括2.89 5 主8.67克/升之鱗 .•酸(H3P04)(工業級)、0.3至!克/升之尿素(分析純)、Q 39 -至⑽克/升之石請(HN〇3)(工業級)、6 i 3〇克/升之碌酸 二氫錳(Mr^HJO4)2)(工業級)及〇·2至〇·6克/升之單寧酸 (C76H52〇46)(分析純)。 磷酸之主要作用係提供形成魏膜所需要之碟酸根 離子。磷酸於該化成溶液中之濃度優選為4 34至65克/ 升。 θ 尿素之主要作用係使形成之磷化膜更均勻。尿素於該 化成溶液中濃度優選為〇·4至0.6克/升。 硝酸之主要作用係提供遊離氫離子,以調整化成溶液 之PH值,使該化成溶液之pH值於6·5至9 5之間。為使 磷化膜具有較佳之抗鹽霧性能及較低之表面阻抗,硝酸於 該化成溶液中濃度優選為0.62至〇 94克/升。 磷酸一氫錳之主要作用係提供錳離子、磷酸根離子及 ❹遊離氫離子。磷酸二氫錳於該化成溶液中濃度優選為丄〇 至18克/升。 單平SiL之主要作用係增加鱗化膜與後續塗裝於構化 膜上之油漆層之間之附著力。單寧酸於該化成溶液中優選 為0.4至0.55克/升。 形成磷化膜之時間可為30秒至50秒。形成之磷化膜 之主要成分為磷酸鎂(Mg3(p〇4)2)、磷酸錳(Mn3(p〇4)2)等複 合磷酸鹽,其中主要化學反應方程式如下:Mg + 2H+=Mg2++H2 ; 200927999 The flawless water-soluble surfactant is used to make the surface reaction of magnesium alloy workpiece more uniform, and at the same time reduce the reaction speed, so that the reaction of citric acid is easier to control, thereby further avoiding or reducing pickling. During the process, excessive corrosion occurs on the surface of the magnesium alloy workpiece to form a black ash substance. The water-free solution: the surfactant is a low-foaming, water-free, nonionic surfactant whose hydrophilic group is mainly a hydroxyl group. The flawless water-soluble surfactant may be a polyol, such as diethylene glycol, glycerin, pentaerythritol, sucrose, glucose, more uniform reaction and avoiding waste. The concentration in the water-free surface sputum is preferably 3 to 4 g / liter. Sorbitol and the like. In order to dissolve the active agent in the acid wash in step 40, the alkali washing time may be 3 to 5 minutes, and the alkali washing temperature may be 60 to 80 °C. The base in the caustic wash solution may be potassium hydroxide (KOH) or sodium hydroxide (NaOH). Alkaline washing is used to react with the black ash material on the surface of the magnesium alloy pre-base to remove the black ash material and expose the magnesium alloy substrate. If industrial grade potassium hydroxide is used, the concentration in the alkali washing solution may be 6 〇 to 18 克 / liter; 〇 is to completely remove the black ash material and avoid local blackening of the surface of the subsequent phosphating film and avoid subsequent The surface of the resulting filled film has a large surface impedance, and potassium hydroxide is used for the washing; the degree of agronomy in the grain liquid is preferably from 1 to 150 g/liter. The following chemical reactions occur mainly in the hydration: 6ΚΟΗ+2Α1=2Κ3Α1〇3 + 3Η2 ; 2K0H+Zn=K2Zn02+H2. The time of formation in step 50 can be from 3 to 50 seconds, and the formation temperature can be from 35 to 45. (: The filling film formed on the surface of the magnesium alloy pre-substrate may be 5 to 30 microns, and the surface resistance of the magnesium alloy pre-substrate may be less than 2 ohms. The chemical solution may include 2.89 5 main 8.67 Gram / liter scale. • Acid (H3P04) (industrial grade), 0.3 to! g / liter of urea (analytical grade), Q 39 - to (10) g / liter of stone (HN 〇 3) (industrial grade), 6 i 3 g/L of dihydromanganese (Mr^HJO4) 2) (industrial grade) and 〇·2 to 〇·6 g/l of tannic acid (C76H52〇46) (analytical grade). The main role of phosphoric acid is to provide the acid ion ions needed to form the Wei film. The concentration of phosphoric acid in the formation solution is preferably from 4 34 to 65 g / liter. The main role of θ urea is to make the formed phosphating film more uniform. The concentration of urea in the chemical solution is preferably from 4 to 0.6 g/liter. The main function of nitric acid is to provide free hydrogen ions to adjust the pH of the solution to a pH of between 6.5 and 9.5. In order for the phosphating film to have better salt spray resistance and lower surface resistance, the concentration of nitric acid in the forming solution is preferably from 0.62 to 9.4 g/l. The main function of manganese monomanganese phosphate is to provide manganese ions, phosphate ions and ruthenium free hydrogen ions. The concentration of manganese dihydrogen phosphate in the formation solution is preferably from 丄〇 to 18 g/liter. The primary function of the monolithic SiL is to increase the adhesion between the squamous film and the subsequently applied paint layer on the structured film. The tannic acid is preferably from 0.4 to 0.55 g/liter in the formation solution. The time for forming the phosphating film may be from 30 seconds to 50 seconds. The main components of the formed phosphating film are complex phosphates such as magnesium phosphate (Mg3(p〇4)2) and manganese phosphate (Mn3(p〇4)2), and the main chemical reaction equations are as follows:

Mg+2H+=Mg2++H2 ; 200927999 3Mg2+ + 2P〇43 =Mg3(P〇4)2 ; 3Mn2++2P043_=Mn3(P04)2。 複合磷酸鹽其化學代表式可為: (Mg2+)A(Mn2+)B(N〇3 )c(Zn2+)D(P043 )E…。 可以理解’於步驟2〇、步驟30、步驟40及步驟50 後還可分別進行至少一次水洗步驟,以及於步驟5 〇後還可 對該鎂合金工件進行烘烤處理,其中烘烤之時間為3〇至 7〇分鐘’烘烤之溫度為11()至i50°c。 為進一步對上述鎂合金磷化方法進行說明,以下將以 具體實施例說明。 €>Mg+2H+=Mg2++H2; 200927999 3Mg2+ + 2P〇43 =Mg3(P〇4)2; 3Mn2++2P043_=Mn3(P04)2. The chemical formula of the composite phosphate may be: (Mg2+)A(Mn2+)B(N〇3)c(Zn2+)D(P043)E.... It can be understood that the at least one water washing step can be separately performed after the step 2, the step 30, the step 40 and the step 50, and the magnesium alloy workpiece can be baked after the step 5, wherein the baking time is 3〇 to 7〇 minutes' baking temperature is 11 () to i50 °c. In order to further explain the above-described magnesium alloy phosphating method, the following will be described by way of specific examples. €>

提供三組(第一組、第二組與第三組)鎂合 該鎮合金預基材之材質均為AZ91D龍合金,制如圖: 所示之工藝流程及參數,對該三域合金預基材進行鱗化 處理;且於魏處理過程中,第―組、第二組盘第三關 合金預基材於脫脂、酸洗、鹼洗及化成工藝中所採用之溶 =應之組分濃度分別如MkAme 列所不。 P 磷化處理後之三組鎂合金工 口 OB,, ^ ® 1于谷抽樣檢測三個樣 口口測试結果如圖4所示。其中,醆露制钟认碰命 行,使用5%之氯化納溶液·>派/ ;Ja"霧箱中進 愈禊斜m “ 抗測試使用微歐姆計 興探針,附者力係於鎮合仝生 ^〇τ 百格刀測試。 ♦增便,使用 級 從圖4中可以看出, ’表面阻抗均小於2歐姆 二組樣品之鹽霧測試均超過8 ,附著力均大於3β。可見,採Provide three groups (the first group, the second group and the third group). The alloy pre-base material of the town is AZ91D dragon alloy. The process and parameters shown in the figure are as shown in the figure. The substrate is subjected to squaring treatment; and in the process of Wei treatment, the components of the first group and the second group of the third off alloy pre-substrate are used in the degreasing, pickling, caustic washing and chemical conversion processes. The concentrations are not as listed in the MkAme column. The results of the three sample mouth tests of the three groups of magnesium alloys OB, ^ ® 1 after P phosphating are shown in Fig. 4. Among them, the 醆 制 制 认 , , , , , , , , , , , , 使用 使用 使用 ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; In the town contract contract ^ 〇 τ 100 grid knife test. ♦ Increased, the use level can be seen from Figure 4, 'the surface impedance is less than 2 ohms. The salt spray test of both sets of samples exceeds 8 and the adhesion is greater than 3β. Visible

11 (S 200927999 用本發明之鎂合金磷化方法處理之鎂合金工件具有良好之 •耐鹽霧性能、較高之附著力及較小之表面阻抗。'當^鎂合 -金工件應用於可攜式電子裝置時,可確保該可攜式電子裝 置具有較強之電磁波遮罩能力。 綜上所述,本發明符合發明專利要件,爰依法提出專 利申請。惟,以上所述者僅為本發明之較佳實施方式,本 發明之範圍並不以上述實施方式為限,舉凡熟悉本案技藝 ❹之人士’於援依本案發明精神所作之等效修飾或變化,皆 應包含於以下之申請專利範圍内。 【圖式簡單說明】 圖1係本發明較佳實施方式之鎂合金磷化方法之流程 圖。 圖2鎂合金磷化工藝流程及參數圖。 圖3磷化過程中脫脂、酸洗、鹼洗及化成步驟之溶液 配方。 © 圖4樣品測試結果圖。 【主要元件符號說明】 無11 (S 200927999 The magnesium alloy workpiece treated by the magnesium alloy phosphating method of the invention has good salt spray resistance, high adhesion and small surface resistance. 'When the magnesium-gold workpiece is applied In the case of the portable electronic device, the portable electronic device can ensure a strong electromagnetic wave shielding capability. In summary, the present invention complies with the invention patent requirements, and the patent application is filed according to law. The invention is not limited to the above-described embodiments, and any equivalent modifications or variations made by those skilled in the art to the present invention should be included in the following patent applications. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a flow chart of a magnesium alloy phosphating method according to a preferred embodiment of the present invention. Fig. 2 Magnesium alloy phosphating process flow and parameter diagram Fig. 3 Degreasing and pickling during phosphating Solution formula for alkaline washing and chemical conversion steps. Figure 4 Sample test results. [Main component symbol description]

1212

Claims (1)

200927999 . 十、申請專利範圍 1. 一種用於鎂合金磷化工藝之酸洗溶液,其包括檸檬酸與 ' 無矽水溶性表面活性劑,其中檸檬酸在該酸洗溶液中之 濃度為5至30克/升,無矽水溶性表面活性劑在該酸洗 溶液中之濃度為1.5至6克/升。 2. 如申請專利範圍第1項所述之用於鎂合金磷化工藝之酸 洗溶液,其中該檸檬酸在該酸洗溶液中之濃度為8至15 克/升。 ❹ 上 3. 如申請專利範圍第1項所述之用於鎂合金磷化工藝之酸 洗溶液,其中該無矽水溶性表面活性劑在該酸洗溶液中 之濃度為3至4克/升。 4. 如申明專利範圍第丨項所述之用於鎂合金墙化工藝之酸 洗溶液,其中該無矽水溶性表面活性劑為多元醇。 5. 如申明專利範圍第4項所述之用於鎂合金鱗化工藝之酸 先洛液其中該多元醇為聚乙二醇、甘油、季戊四醇、 〇 蔗糖、葡萄糖及山梨醇之一或其組合物。 6·-種鎂合金璘化方法,依次包括酸洗、驗洗及化成形成 磷化膜之工藝步驟,其中在酸洗步驟採用一酸洗溶液, 該酸洗溶液包括檸檬酸與無矽水溶性表面活性劑,其中 =檬酸在該酸洗溶液中之濃度為5至3〇克/升,無矽水 /奋性表面活性劑在該酸洗溶液中之濃度為至6克/升。 7.如申請專利範圍第6項所述之鎂合金璘化方法,其中轉 檬酸在該酸洗溶液中之濃度為8至15克/升。 8·如申請專利範圍第6項所述之鎂合金磷化方法,其中無 13 < S 200927999 矽水溶性表面活性劑在該酸洗溶液t之濃度為 升。 9. 如申請專利範圍第6項所述之鎂合金磷化方法其中無 矽水溶性表面活性劑為多元醇。 、…' 10. 如申明專利範圍第9項所述之鎂合金磷化方法其中該 多70醇為聚乙二醇、甘油、季戊四醇、Μ糖、葡萄糖及 山梨醇之一或其組合物。 ❹200927999 . X. Patent Application Range 1. A pickling solution for magnesium alloy phosphating process, comprising citric acid and 'no water-soluble surfactant, wherein the concentration of citric acid in the pickling solution is 5 to 30 g / liter, the concentration of the water-free surfactant in the pickling solution is 1.5 to 6 g / liter. 2. The pickling solution for magnesium alloy phosphating process according to claim 1, wherein the concentration of the citric acid in the pickling solution is 8 to 15 g/l. 3. The pickling solution for magnesium alloy phosphating process according to claim 1, wherein the concentration of the water-free surfactant in the pickling solution is 3 to 4 g/liter. . 4. The acid washing solution for magnesium alloy walling process according to the above-mentioned claim, wherein the water-free surfactant is a polyol. 5. The acid sirloin solution for magnesium alloy sizing process according to claim 4, wherein the polyol is one of polyethylene glycol, glycerin, pentaerythritol, sucrose, glucose and sorbitol or a combination thereof. Things. 6·- magnesium alloy deuteration method, which comprises the steps of pickling, washing and forming into a phosphating film, wherein an acid washing solution comprising citric acid and water-free water is used in the pickling step. A surfactant wherein the concentration of citric acid in the pickling solution is 5 to 3 g/l and the concentration of the non-hydrophobic/exciting surfactant in the pickling solution is 6 g/l. 7. The magnesium alloy deuteration method according to claim 6, wherein the concentration of the citric acid in the pickling solution is from 8 to 15 g/l. 8. The method of phosphating a magnesium alloy according to claim 6, wherein the concentration of the water-soluble surfactant in the pickling solution is liter. 9. The magnesium alloy phosphating method according to claim 6, wherein the water-free surfactant is a polyol. 10. The magnesium alloy phosphating method according to claim 9, wherein the polyhydric alcohol is one of polyethylene glycol, glycerin, pentaerythritol, sucrose, glucose, and sorbitol or a combination thereof. ❹ 1414
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