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Corrosion Forecast

Equation (2-38) is valid for every region of the surface. In this case only weight loss corrosion is possible and not localized corrosion. Figure 2-5 shows total and partial current densities of a mixed electrode. In free corrosion 7 = 0. The free corrosion potential lies between the equilibrium potentials of the partial reactions and U Q, and corresponds in this case to the rest potential. Deviations from the rest potential are called polarization voltage or polarization. At the rest potential = ly l, which is the corrosion rate in free corrosion. With anodic polarization resulting from positive total current densities, the potential becomes more positive and the corrosion rate greater. This effect is known as anodic enhancement of corrosion. For a quantitative view, it is unfortunately often overlooked that neither the corrosion rate nor its increase corresponds to anodic total current density unless the cathodic partial current is negligibly small. Quantitative forecasts are possible only if the Jq U) curve is known. [Pg.44]

However, the published corrosion rates of Ru from oxygen evolution are not reliable, as they forecast [50] Ru losses as high as 40 g cm-2 h, which is inconsistent with the anode lifetimes observed in commercial chlor-alkali cells. [Pg.87]

The ERICE system Knowledge Base is composed at top-level by a parent unit (CORROSION) as shown in Figure 1 and by three descendant units (FORECAST, CHECK and DIAGNOSIS). The CORROSION unit has the goal to perform a complete cognitive process relative to forecasting and checking the correct/incorrect corrosion rate. [Pg.153]

Then, utilizing these data, the FORECAST unit is instantiated to evaluate the forecasting range of corrosion rate values. [Pg.155]

Obviously the forecasting corrosion rate value will be different if the plant was operated in normal or anomalous chemical conditions the two different evaluations are executed by the units NORMAL CONDITION and ANOMALOUS CONDITION respectively. [Pg.155]

After the forecasting process the CHECK unit is istantiated to compare the estimated corrosion rate values with the measured one if a match of the values occours the current goal of the system is reached and the expert system waits until a new corrosion rate value is available. Otherwise the DIAGNOSIS units is istantiated. [Pg.155]

The forecast of RubCon chemical resistance coefficient for x = 10 years of operation in corrosive environments has been carried out by [21,24] according to these formulas ... [Pg.81]

Analysis of metal artefacts tells us about their state of preservation, and analysis of any covering corrosion products informs us about the post-depositional corrosion processes and their thermodynamic stability. This in turn enables us to forecast the changes in the environment that may be detrimental to their future preservation. [Pg.323]

Sea-dumped CW should be examined for corrosion to predict more realistically the impact of the sea environment on munition shells and to forecast possible major releases of chemical warfare agents in the future. [Pg.65]

Ru02 losses can occur via the dissolution of the intermediates in the above reactions. However, the published corrosion data for Ru from O2 evolution are not reliable as the data forecast Ru losses as high as 40gm hr [80], which are inconsistent with the observations in diaphragm chlor-alkali cell operations. [Pg.230]

CGC IV Accurate forecasting of remaining service time until major repair, replacement, or overhaul becomes necessary—i.e., corrosion prognosis. [Pg.22]

Because of such complexity, there are scientific barriers to the advancement of lifetime prediction models that forecast damage accumulation, as well as barriers to computational design of materials for obtaining desired corrosion properties and to achieving, at the engineering level, a prognosis of future damage on the basis of physics at the materials science scale. These barriers present opportunities for improvement that include, but are not limited to ... [Pg.89]

Corrosion grand challenge IV addresses the critical need for better methods to monitor the actual deterioration of a component once it is placed in service in a corrosive environment, analyze that information, and, based on decision-making algorithms (or reasoners ), provide a reasonable forecast of the time remaining before maintenance or replacement becomes necessary. [Pg.100]

The physicochemical hazard assessment must consider the potential threats from combustion, explosiveness, oxidizability, and metal corrosion. The human health risk assessment must qualitatively rank the hazard presented by the new substance, and the submitter must provide "the doses (concentration) of the new chemical substance. .. to match its no-hazard or minimum hazard status," akin to a DNEL as described in Chapter 2. The environmental hazard assessment must qualify the hazard level as severe, medium, or mild and a concentration akin to the PNEC, as discussed in Chapter 2, derived. The exposure assessment comprises two parts a simple exposure forecast and assessment and a detailed exposure forecast and assessment. The latter includes a material balance on manufacturing or processing, and exposure scenarios for different exposure routes that describe the extent, range, and frequency of exposures. The results of the hazard... [Pg.112]

Pourbaix diagrams Thermodynamically, one may forecast or predict whether certain reactions can occur however, this does not mean that the reaction in question will occur. Thermodynamics can tell us about the tendency of corrosion to happen, and it is by using Pourbaix diagrams that one can thermodynamically predict whether certain reactions will occur. [Pg.6]

In this chapter, we very briefly touched on some important theoretical elements of electrochemical corrosion such as how corrosion can be forecast (by using Pour-baix diagrams) and how fast it can happen (by using anodic and cathodic polarisation curves). [Pg.9]

Adhesive bonds are degraded by various chemical reactions, notably hydrolysis, corrosion, and dissolution at the interface. Although primers and inhibitors minimize these effects, their role is not well understood. It is obvious that any systematic improvement in our present ability to forecast the service life of bonds will require a greater understanding of the processes involved in bond deterioration. [Pg.69]


See other pages where Corrosion Forecast is mentioned: [Pg.154]    [Pg.6]    [Pg.6]    [Pg.8]    [Pg.154]    [Pg.6]    [Pg.6]    [Pg.8]    [Pg.189]    [Pg.326]    [Pg.326]    [Pg.189]    [Pg.189]    [Pg.4]    [Pg.350]    [Pg.542]    [Pg.542]    [Pg.33]    [Pg.2040]    [Pg.65]    [Pg.70]    [Pg.166]    [Pg.179]    [Pg.676]    [Pg.114]    [Pg.49]    [Pg.170]    [Pg.277]    [Pg.279]    [Pg.896]   


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