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Process for forming a coating on surfaces of metal ferrifeno transformation with control automatic adicao of nitrite in solutions of acid phosphate coating
Process for forming a coating on surfaces of metal ferrifeno transformation with control automatic adicao of nitrite in solutions of acid phosphate coating
In producing phosphate coatings upon a succession of ferrous metal surfaces by contacting them with a nitrite-containing aqueous acidic zinc phosphate solution, the solution is replenished with nitrite ion at a rate governed by the potential measured across a pair of redox electrodes immersed in the solution while contact is maintained between the solution and the surfaces. The solution may also contain calcium phosphate, oxidizing accelerator such as nitrate, non-oxidizing accelerators such as Cu, Ag, Ni and/or Co as well as simple and complex fluorides and salts of polyphosphoric acids. Replenishment with nitrite ion is initiated when the measured potential falls to a pre-selected value and is subsequently discontinued either a) when the measured potential rises above a higher pre-selected value or b) after a pre-selected time interval. Replenishment may be prevented during a further pre-selected time interval occurring immediately after the replenishing time interval. The redox electrodes may comprise a calomel and a Pt electrode. Alternatively Au-calomel or C-calomel systems may be used. The inert one of the pair of redox electrodes may be periodically cleaned by first rendering it anodic relative to a second inert electrode positioned adjacent thereto and subsequently rendering it cathodic relative to the second inert electrode. Fig.1 (not shown) illustrates a line wherein car parts are spray-treated as they are conveyed through a tunnel (4). They are cleaned with an aqueous solution of Na3PO4 or Na2CO3 (at 5), water rinsed (at 6 and 7), phosphate conversion coated (at 8), water rinsed (at 9), acid rinsed (at 10) e.g. with chromic acid to stabilize and passivate the conversion coating and oven dried (at 3) prior to painting. Fig. 2 (not shown) illustrates the spraying of workpieces (19, 20) with the phosphate solution as they move along a conveyer (1) circulation of the solution and addition of phosphate and replenishing NaNO2 from drums (28, 33) to the circulating solution. Fig. 3 (not shown) illustrates calomel and Pt redox electrodes (40, 41) triggering operation of a time switch (T1 or T2) to control a motor (32) which drives a pump (31) to deliver nitrite solution from a drum (33) to the phosphate solution. Switching mechanism controls cleaning of the electrode (41) with the aid of an auxiliary Pt electrode (42).
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机译:在通过使一类黑色金属表面与含亚硝酸盐的酸性磷酸锌水溶液接触而在一系列黑色金属表面上生产磷酸盐涂层时,向溶液中补充亚硝酸根离子的速率取决于浸入溶液中的一对氧化还原电极上测得的电势同时保持溶液与表面之间的接触。该溶液还可以包含磷酸钙,氧化促进剂例如硝酸盐,非氧化促进剂例如Cu,Ag,Ni和/或Co以及简单和复杂的氟化物和多磷酸的盐。当测得的电位下降到预选值时开始进行亚硝酸根离子的补给,然后在a)当测得的电位上升到较高的预选值以上或b)在预选的时间间隔后中止。在补充时间间隔之后立即发生的另外的预选时间间隔期间,可以防止补充。氧化还原电极可以包括甘汞和Pt电极。或者,可以使用Au-calomel或C-calomel系统。可以通过首先相对于与其相邻的第二惰性电极使其呈阳极,然后相对于第二惰性电极使其呈阴极,来定期清洁一对氧化还原电极中的一个。图1(未示出)示出了一条线,其中汽车部件在通过隧道(4)输送时被喷雾处理。它们用Na 3 PO 4或Na 2 CO 3水溶液(在5)清洗,用水漂洗(在6和7),用磷酸盐转化膜涂覆(在8),用水漂洗(在9),用酸漂洗(在10)。用铬酸稳定和钝化转化膜,并在涂漆前用烘箱干燥(3)。图2(未示出)示出了当工件(19、20)沿着输送机(1)移动时,用磷酸盐溶液喷涂工件(19、20),溶液的循环以及磷酸盐的添加以及从鼓(28、33)向其补充的NaNO2。循环溶液。图3(未示出)示出了甘汞和Pt氧化还原电极(40、41),其触发时间开关(T1或T2)的操作,以控制驱动泵(31)以从滚筒输送亚硝酸盐溶液的电动机(32)。 (33)去磷酸盐溶液。切换机构借助于辅助Pt电极(42)控制电极(41)的清洁。
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