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"Some Studies on the Parameters for the New Bath for Protection of ...

"Some Studies on the Parameters for the New Bath for Protection of ...

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"<str<strong>on</strong>g>Some</str<strong>on</strong>g> <str<strong>on</strong>g>Studies</str<strong>on</strong>g> <strong>on</strong> <strong>the</strong> <strong>Parameters</strong> <strong>for</strong> <strong>the</strong> <strong>New</strong> <strong>Bath</strong> <strong>for</strong> Protecti<strong>on</strong> <strong>of</strong> Steel fromCorrosi<strong>on</strong>"1. Introducti<strong>on</strong>:The corrosi<strong>on</strong> resistance <strong>of</strong> pure zinc deposits is not satisfactory undermore corrosive envir<strong>on</strong>ments, particularly in a very humid atmosphere. Itwas found that additi<strong>on</strong> <strong>of</strong> cobalt to zinc was so effective in <strong>the</strong>improvement <strong>of</strong> <strong>the</strong> corrosi<strong>on</strong> resistance <strong>of</strong> galvanized steel producti<strong>on</strong> (1,2, 3, 4) .Too, <strong>the</strong> zinc and his alloys (4, 5) are characterized by <strong>the</strong>ir high degree <strong>of</strong>corrosi<strong>on</strong> protecti<strong>on</strong> <strong>of</strong> steel in automobile (6, 7, 8) , aerospace (9) , andelectr<strong>on</strong>ic industries (10) . In additi<strong>on</strong>, its possible use as a less pollutingalternative to cadmium coatings (11) .In <strong>the</strong> present study, zinc was electrodeposited <strong>on</strong>to steel substrates fromcitrate baths. Attempts had been d<strong>on</strong>e in order to obtain a sound andsatisfactory deposits from an optimum bath. The effect <strong>of</strong> operatingvariables such as: bath c<strong>on</strong>stituent, c<strong>on</strong>centrati<strong>on</strong>s <strong>of</strong> zinc i<strong>on</strong>s, currentdensity, pH, and temperature <strong>on</strong> <strong>the</strong> electrodepositi<strong>on</strong> <strong>of</strong> zinc wasstudied. In additi<strong>on</strong>, <strong>the</strong> effect <strong>of</strong> some additi<strong>on</strong> agents <strong>on</strong> <strong>the</strong> process <strong>of</strong>zinc electrodepositi<strong>on</strong> from <strong>the</strong>se baths was studied. <strong>Bath</strong>s used <strong>for</strong> <strong>the</strong>electrodepositi<strong>on</strong> <strong>of</strong> zinc are presented in Table 1.2. Experimental workAll <strong>the</strong> plating baths and reagents used were made from annularchemicals and doubly distilled water. The compositi<strong>on</strong>s <strong>of</strong> <strong>the</strong> examinedbaths <strong>for</strong> zinc electrodepositi<strong>on</strong> are given in Table 1. Forelectrodepositi<strong>on</strong>, a steel cathode and platinum sheet anode each <strong>of</strong>dimensi<strong>on</strong>s (2.5 cm x 3.0 cm) was used. The plating cell used was arectangular Perspex trough (10 cm x 3.0 cm) provided with verticalgrooves, <strong>on</strong> each <strong>of</strong> <strong>the</strong> side walls, to fix <strong>the</strong> electrodes. Be<strong>for</strong>e each run,steel cathode was mechanically polished with different grade emerypapers, 600, 800, 1000 and 1500 and <strong>the</strong>n washed with distilled water,rinsed with ethanol and weighed. Direct current (d.c) was supplied byd.c. power supply model (GPS-3030D). The Cathodic currentefficiencies f were determined with <strong>the</strong> help <strong>of</strong> Cu-coulometer, (f =Wt exp ./ Wt <strong>the</strong>o .) where Wt exp is <strong>the</strong> weight <strong>of</strong> <strong>the</strong> deposit obtainedexperimentally and Wt <strong>the</strong>o is <strong>the</strong> weight <strong>of</strong> <strong>the</strong> deposit calculated<strong>the</strong>oretically according to Faraday’s law. Most <strong>of</strong> <strong>the</strong> experiments werecarried out at 25 ± 2 o C. The plating durati<strong>on</strong> was 20 minutes.76

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