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Mild anodization

Reactions different from those listed above may simultaneously contribute to a minor extent. Thus, the characterization of the GaAs electrode by XPS has demonstrated a significant enrichment in As at the surface after mild anodization [45]. Also by in-situ ellipsometric measurements, combined with ex-situ surface analysis by SEM, Auger spectroscopy and X-ray diffraction, it has recently been... [Pg.10]

MC 1 pm thin (200-800 nm grains) 1020-1021 O.lVs-1 As grown (NDCh,gh) Mild anodic (NDC, ) Severe anodic... [Pg.188]

Although both of the previously mentioned methods yield high-quality polyparaphenylene films, polyparaphenylene can also be formed electrochemically from biphenyl (Fig. 21c) dissolved in acetonitrile under similar mild anodic conditions [367]. The electropolymerization of biphenyl may be advantageous in that the toxicity of biphenyl is lower than that of benzene. Furthermore, the resulting films are reported to have longer chain lengths and less cross-linking than the films synthesized directly from benzene [368]. [Pg.803]

Simonet, J. The mild anodic oxidation of platinum in organic solvents of low acidity. J. Electroanal. Chem. 578 (2005) 79. [Pg.168]

United States, LaSalle, IH. 1918 continuous Hquid-phase oxidation (since ca 1961) K MnO separation from Hquid phase is without prior dilution continuous electrolysis of filtered electrolyte in bipolar ceUs Monel anodes, mild steel cathodes, vacuum crystallization 14,000 ... [Pg.519]

The reaction mixture is filtered. The soHds containing K MnO are leached, filtered, and the filtrate composition adjusted for electrolysis. The soHds are gangue. The Cams Chemical Co. electrolyzes a solution containing 120—150 g/L KOH and 50—60 g/L K MnO. The cells are bipolar (68). The anode side is monel and the cathode mild steel. The cathode consists of small protmsions from the bipolar unit. The base of the cathode is coated with a corrosion-resistant plastic such that the ratio of active cathode area to anode area is about 1 to 140. Cells operate at 1.2—1.4 kA. Anode and cathode current densities are about 85—100 A/m and 13—15 kA/m, respectively. The small cathode areas and large anode areas are used to minimize the reduction of permanganate at the cathode (69). Potassium permanganate is continuously crystallized from cell Hquors. The caustic mother Hquors are evaporated and returned to the cell feed preparation system. [Pg.78]

Both cell types utilize 5—25 g/L Cr at a pH = 2.3-40 and a temperature from 20—50°C under mild air agitation. Current densities mn from 430—1600 A/m, the rectifier voltage is from 4—15 V, and the anode to cathode ratio is 2 1. [Pg.156]

The assessment for nonalloyed ferrous materials (e.g., mild steel, cast iron) can also be applied generally to hot-dipped galvanized steel. Surface films of corrosion products act favorably in limiting corrosion of the zinc. This strongly retards the development of anodic areas. Surface film formation can also be assessed from the sum of rating numbers [3, 14]. [Pg.148]

As in the case of corrosion at the insulating connection due to different potentials caused by cathodic protection of the pipeline, there is a danger if the insulating connection is fitted between two sections of a pipeline with different materials, e.g., mild and stainless steel. The difference between the external pipe/soil potential is changed by cell currents so that the difference between the internal pipe/ medium potential has the same value, i.e., both potential differences become equal. If the latter is lower than the former for the case of free corrosion, the part of the pipe with the material that has the more positive rest potential in the soil is polarized anodically on the inner surface. The danger increases with external cathodic protection in the part of the pipeline made of mild steel. [Pg.282]

Modem cells employ arrays of anodes (Ti02 coated with a noble metal) and cathodes (mild steel) spaced 3 mm apart and carrying current at 2700Am into brine (80-100gl ) at 60-80°C. Under these conditions current efficiency can reach 93% and 1 tonne of NaC103 can be obtained from 565 kg NaCl and 4535 kWh of electricity. The off-gas H2 is also collected. [Pg.862]

The use of anodic films on aluminum alloys is only applicable to some mildly corrosive environments, including architectural purposes and where abrasion resistance is required. [Pg.906]

It also follows that if the solution is stirred the rate of arrival of oxygen at the cathode will be increased. This will result in a corresponding increase in the rate of bimetallic corrosion as is shown in Fig. 1.63 for the aluminium-mild steel couple in stirred 1 - On NaCl solution . The increase in galvanic corrosion rate will be in the inverse relation to the slope of the anodic polarisation curve of the more negative metal, provided that the cathodic reaction is not totally diffusion controlled. [Pg.222]

Fig. 1.67 Effect of mild-steel cathode on the weight loss of aluminium and zinc anodes (100 cm area) and on the number of coulombs flowing in the aluminium-mild steel and zinc-mild steel couples over a 96 h period in 1 -0 n NaCl at 25°C (after Pryor and Keir )... Fig. 1.67 Effect of mild-steel cathode on the weight loss of aluminium and zinc anodes (100 cm area) and on the number of coulombs flowing in the aluminium-mild steel and zinc-mild steel couples over a 96 h period in 1 -0 n NaCl at 25°C (after Pryor and Keir )...
In pure dry air at normal temperatures a thin protective oxide film forms on the surface of polished mild steel. Unlike that formed on stainless steels it is not protective in the presence of electrolytes and usually breaks down in air, water and soil. The anodic reaction is ... [Pg.487]

Contact of brass, bronze, copper or the more resistant stainless steels with the 13% Cr steels in sea-water can lead to accelerated corrosion of the latter. Galvanic contact effects on metals coupled to the austenitic types are only slight with brass, bronze and copper, but with cadmium, zinc, aluminium and magnesium alloys, insulation or protective measures are necessary to avoid serious attack on the non-ferrous material. Mild steel and the 13% chromium types are also liable to accelerated attack from contact with the chromium-nickel grades. The austenitic materials do not themselves suffer anodic attack in sea-water from contact with any of the usual materials of construction. [Pg.545]

An unacceptable situation because of the large anode to cathode ratio The reverse situation may be acceptable under mild corrosive conditions... [Pg.86]


See other pages where Mild anodization is mentioned: [Pg.188]    [Pg.115]    [Pg.360]    [Pg.129]    [Pg.131]    [Pg.203]    [Pg.897]    [Pg.188]    [Pg.115]    [Pg.360]    [Pg.129]    [Pg.131]    [Pg.203]    [Pg.897]    [Pg.489]    [Pg.519]    [Pg.520]    [Pg.520]    [Pg.520]    [Pg.196]    [Pg.77]    [Pg.149]    [Pg.123]    [Pg.148]    [Pg.198]    [Pg.797]    [Pg.1292]    [Pg.154]    [Pg.208]    [Pg.209]    [Pg.225]    [Pg.231]    [Pg.233]    [Pg.237]    [Pg.699]    [Pg.1154]    [Pg.1187]    [Pg.1187]    [Pg.1191]    [Pg.87]   
See also in sourсe #XX -- [ Pg.129 ]




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