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Anodes galvanic

These three passive systems are important in the technique of anodic protection (see Chapter 21). The kinetics of the cathodic partial reaction and therefore curves of type I, II or III depend on the material and the particular medium. Case III can be achieved by alloying additions of cathodically acting elements such as Pt, Pd, Ag, and Cu. In principle, this is a case of galvanic anodic protection by cathodic constituents of the microstructure [50]. [Pg.61]

Galvanic anodes should exhibit as low a polarizability as possible. The extent of their polarization is important in practice for their current output. A further anode... [Pg.179]

The cathodic protection of plain carbon and low-alloy steels can be achieved with galvanic anodes of zinc, aluminum or magnesium. For materials with relatively more positive protection potentials (e.g., stainless steels, copper, nickel or tin alloys), galvanic anodes of iron or of activated lead can be used. [Pg.180]

The current-density-potential graph for a working galvanic anode is given by Eq. (6-8) in which the polarization resistance /j, is dependent on loading ... [Pg.183]

Fig. 6-1 Characteristic J U ) and resistance straight lines of a galvanic anode. Slope of the resistance lines tan a = + / )]. Slope of the... Fig. 6-1 Characteristic J U ) and resistance straight lines of a galvanic anode. Slope of the resistance lines tan a = + / )]. Slope of the...
This value can be considerably smaller. It corresponds in Fig. 6-1 to the ordinate of the intersection of the resistance graph of slope cCq with a 7(f/-r) curve that deviates markedly to the left of that plotted. The maximum current density is an important quantity for the setting up of cathodic protection with galvanic anodes and is dependent on the anode geometry and conductivity of the medium. [Pg.185]

Galvanic anodes of cast iron were already in use in 1824 for protecting the copper cladding on wooden ships (see Section 1.3). Even today iron anodes are still used for objects with a relatively positive protection potential, especially if only a small reduction in potential is desired, e.g., by the presence of limiting values U" (see Section 2.4). In such cases, anodes of pure iron (Armco iron) are mostly used. The most important data are shown in Table 6-1. [Pg.185]

In spite of a low driving voltage of about 0.2 V, about 90% of all galvanic anodes for the external protection of seagoing ships are zinc anodes (see Section 17.3.2). Zinc alloys are the only anode materials permitted without restrictions for the internal protection of exchange tanks on tankers [16] (see Section 17.4). [Pg.188]

Pure aluminum cannot be used as an anode material on account of its easy passivatability. For galvanic anodes, aluminum alloys are employed that contain activating alloying elements that hinder or prevent the formation of surface films. These are usually up to 8% Zn and/or 5% Mg. In addition, metals such as Cd, Ga, In, Hg and T1 are added as so-called lattice expanders, these maintain the longterm activity of the anode. Activation naturally also encourages self-corrosion of the anode. In order to optimize the current yield, so-called lattice contractors are added that include Mn, Si and Ti. [Pg.188]

Oxide, hydroxide and basic salts of aluminum are less soluble at pH values of about 7 than those of zinc [17], which explains the easy passivatability. Galvanic anodes of aluminum alloys are primarily employed in the area of offshore technology. The anodes work in relatively pure seawater flowing with a high velocity so that by using suitable alloys, passivation phenomena are rare. Their low weight is particularly favorable in view of a service time of 20 to 30 years. [Pg.191]

Magnesium anodes usually consist of alloys with additions of Al, Zn and Mn. The content of Ni, Fe and Cu must be kept very low because they favor selfcorrosion. Ni contents of >0.001% impair properties and should not be exceeded. The influence of Cu is not clear. Cu certainly increases self-corrosion but amounts up to 0.05% are not detrimental if the Mn content is over 0.3%. Amounts of Fe up to about 0.01% do not influence self-corrosion if the Mn content is above 0.3%. With additions of Mn, Fe is precipitated from the melt which on solidification is rendered harmless by the formation of Fe crystals with a coating of manganese. The addition of zinc renders the corrosive attack uniform. In addition, the sensitivity to other impurities is depressed. The most important magnesium alloy for galvanic anodes is AZ63, which corresponds to the claims in Ref. 22. Alloys AZ31 and M2 are still used. The most important properties of these alloys are... [Pg.191]

Fig. 6-7 Rest potentials of various galvanic anodes as a function of the salt content of the medium at 20°C. Fig. 6-7 Rest potentials of various galvanic anodes as a function of the salt content of the medium at 20°C.
Fig. 6-9 (above) Apparatus for determining the weight loss of galvanic anodes by measuring hydrogen evolution. [Pg.195]

Galvanic anodes must not be backfilled with coke as with impressed current anodes. A strong corrosion cell would arise from the potential difference between the anode and the coke, which would lead to rapid destruction of the anode. In addition, the driving voltage would immediately collapse and finally the protected object would be seriously damaged by corrosion through the formation of a cell between it and the coke. [Pg.198]

The quality control of galvanic anodes is reduced mainly to the analytical control of the chemical composition of the alloy, to the quality and coating of the support, to an adequate joint between support and anode material, as well as to restricting the weight and size of the anode. The standards in Refs. 6, 7, 22, 27, 31 refer to magnesium and zinc anodes. Corresponding specifications for aluminum anodes do not exist. In addition, the lowest values of the rest potentials are also given [16]. The analytical data represent the minimum requirements, which are usually exceeded. [Pg.203]

In poorly conducting media or soils, however, the low driving voltage can limit the use of galvanic anodes. Raising the current delivery, which becomes necessary in service, is only practically possible with the help of an additional external voltage. In special cases this is used if an installed galvanic system is overstretched or if the reaction products take over additional functions (see Section 7.1). [Pg.205]

No damaging interference to foreign objects has to be considered in cathodic protection with galvanic anodes because of the small current densities in soil and the lower anode voltages. [Pg.258]

The current output of galvanic anodes depends on the specific soil resistivity in the installation area and can only be used in low-resistivity soils for pipelines with a low protection current requirement because of the low driving voltage. Impressed current anode installations can be used in soils with higher specific soil resistivities and where large protection currents are needed because of their variable output voltage. [Pg.278]

Examples of the Design of Protective Installations 11.3.3.1 Equipment Using Galvanic Anodes... [Pg.296]

Protection with impressed current, with galvanic anodes, and a combination of both processes is used for marine structures and offshore pipelines. Their properties, as well as their advantages and disadvantages, are given in Table 16-1. The protective measures must be optimized for every structure. In the impressed current protection of offshore platforms, for example, the difficulties of maintenance and repair will be of major importance, whereas in harbor installations these problems can be... [Pg.367]

The difficulties of such operations on the research platform Nordsee are described in Ref. 9. The Murchison platform was provided with a combination of impressed current protection and galvanic anodes because there was a limit to the load to be transported [12]. The anodes for platforms are installed and provided with cables at the yard. They are installed with redundancy and excess capacity so that no repairs are necessary if there is a breakdown. The lower part of the platform up to the splash zone is usually placed in position in the designated location at least 1 year before the erection of the deck structure so that impressed current protection cannot initially be put in operation. This requires cathodic protection with galvanic anodes for this period. This also means that the impressed current protection is more expensive than the galvanic anodes. [Pg.375]


See other pages where Anodes galvanic is mentioned: [Pg.174]    [Pg.179]    [Pg.180]    [Pg.183]    [Pg.191]    [Pg.198]    [Pg.199]    [Pg.199]    [Pg.204]    [Pg.204]    [Pg.207]    [Pg.263]    [Pg.278]    [Pg.279]    [Pg.295]    [Pg.297]    [Pg.305]    [Pg.343]    [Pg.368]    [Pg.369]    [Pg.372]    [Pg.372]    [Pg.373]    [Pg.374]    [Pg.374]    [Pg.376]    [Pg.377]    [Pg.379]    [Pg.379]    [Pg.384]   
See also in sourсe #XX -- [ Pg.270 ]

See also in sourсe #XX -- [ Pg.553 ]




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Advantages and Disadvantages of Galvanic Anodes

Anode/cathode area ratio, galvanic

Anode/cathode area ratio, galvanic corrosion

Anodes area effect, galvanic corrosion

Anodic polarization curves galvanic couple

Capacity of Galvanic Anodes

Cathode:anode ratio galvanic corrosion

Current Capacity of Galvanic Anodes

Discharge from Galvanic Anodes

Equipment Using Galvanic Anodes

Galvanic (Sacrificial) Anodes

Galvanic anode system

Galvanic anode system advantages

Galvanic anode system installation

Galvanic anodes aluminum

Galvanic anodes current capacity

Galvanic anodes current discharge from

Galvanic anodes forms

Galvanic anodes magnesium

Galvanic anodes offshore

Galvanic anodes pipeline protection

Galvanic anodes power cables

Galvanic anodes pure metals

Galvanic anodes storage tanks

Galvanic anodes supports

Galvanic anodes surface films

Galvanic anodes testing

Galvanic anodes tubes

Galvanic corrosion coupled anodic surface

Protection by Galvanic Anodes

Protection with Galvanic Anodes

Sacrificial anode galvanic corrosion

Surface films zinc galvanic anodes

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