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Chemical corrosives

The chemical corrosion resistance of Zr 704 is slightly less than that of Zr 702 in some environments but Zr 704 is superior in high temperature, high pressure water, and steam. A softer version of Zr 705 is Zr 706, developed specifically for severe forming appUcations such as panel-type heat exchangers. [Pg.431]

To reduce the amount of dust produced, water can be added to the abrasive from a circular water sprayer around the no22le. Chemical corrosion inhibitors must be dissolved in the water to prevent flash msting of the steel. Newer methods to reduce dust include the use of ice, soHd carbon dioxide (dry ice), or plastic beads as abrasives. Blasting with dry ice is inexpensive and effective, but the accumulation of carbon dioxide must be avoided in enclosures. Plastic beads are inexpensive, but the cutting efficiency is low and paint removal is slow the beads can be cleaned of paint particles and reused. [Pg.364]

Evaporative condensers are used quite extensively. In most cases commercial evaporative condensers are not totally suitable for chemical plants due to the hostile atmosphere which usually abounds in vapor and dusts which can cause either chemical (corrosion) or mechanical problems (phigging of spray nozzles). [Pg.1114]

Ammonia Used in refrigeration, chemical processes such as dye making, explosives, lacquer, fertilizer Textiles, chemicals Corrosive to copper, brass, aluminum, and zinc high concentration producing chemical burns on wet sldn... [Pg.2174]

Removing suspended solids, decreasing cycles of concentration, and clarification all may be beneficial in reducing deposits. Biodispersants and biocides should be used in biofouled systems. Simple pH adjustment may lessen precipitation of certain chemical species. The judicious use of chemical corrosion inhibitors has reduced virtually all forms of aqueous corrosion, including underdeposit corrosion. Of course, the cleaner the metal surface, the more effective most chemical inhibition will be. Process leaks must be identified and eliminated. [Pg.83]

Chemical corrosion inhibition can reduce all forms of corrosion including dealloying. In particular, filmers such as tolyltriazole are effective in reducing corrosion of yellow metals. [Pg.303]

This type of pump is used to handle abrasive, chemically corrosive, and oxidizing liquids, where conventional pumps would require exotic alloys. The wet end of these pumps is non-metallic or lined and coated, sealing and isolating any metal component. The power end is normal. [Pg.61]

The bitumens have a good order of chemical corrosion resistance, have reasonably good electrical insulation properties and are very cheap. Their main disadvantages are their black colour and their somewhat brittle nature. [Pg.872]

Chemical (and Water) Tank and Pump. The pump injects water, liquid foamers and chemical corrosion inhibitors into the high-pressure air (or gas) line after compression of the air and prior to the standpipe. [Pg.845]

Sealing rings that are inert to most chemical corrosives and solvents are usually manufactured from PTFE or one of the synthetic elastomers. [Pg.883]

Most organic solvents, except for alcohol, have reasonably low ionic conductivity and hence do not support electro-chemically corrosion to any significant extent. Steel is commonly used except in systems in which water can separate and where the conductivity is sufficient to permit the flow of ionic current. [Pg.899]

The fluidised bed coating technique is used extensively for wirework items such as dish drainer racks, vegetable racks, office trays etc. The technique is also widely used for street furniture e.g. metal lampposts, signposts and balustrading, and for metal office furniture and domestic garden furniture. It also provides chemical corrosion resistance on valves, pipes, couplings etc. [Pg.748]

The main metallic impurities that contaminate the primary powder, due to chemical corrosion of the retort and other metal parts of the reactor, are Fe, Ni and Cr. From this point of view, reactors that are equipped with larger retorts usually provide better purity due to a relatively low ratio between the internal surface of the wet metal parts of the reactor and the total volume of the melt. Recent investigations on the decreasing of Fe, Ni and Cr impurities during the sodium reduction process were performed by Li [591]. It was shown that one of the most effective ways to reduce contamination of the product is to reduce the duration of time K2TaF7 is present in the reactor. [Pg.333]

MRR increases continuously during the entire testing oxidizer concentration as shown in Fig. 36(c), which is consentaneous with the Stein s results [ 106], and this may be due to the stronger chemical corrosion effect at high oxidizer concentration. In addition, it should be noticed that varia-... [Pg.254]

We conclude this review with an example of the application of SPFM to corrosion studies. Atmospheric chemical corrosion constitutes a severe threat to the structural integrity of... [Pg.281]

Besides pure chemical corrosion, solid products of corrosion in the system will give rise to erosive corrosion, in which the particles moving with the fluid will impact onto the surfaces and can remove protective surface layers. Such corrosion effects are most pronounced in regions of high fluid-stream velocity. [Pg.188]

Why does the amount of acid in paper make such a difference Acids are corrosive chemicals. Corrosive chemicals can destroy material or living tissue on contact. Paper does not contain enough acid to burn skin, but over time the paper becomes stiff and brittle and eventually falls apart. As a result, precious personal memories or important historical documents that were written on acidic paper can be lost. Acid-containing paper can also transfer the acid to other objects in a process called acid migration. The acid can weaken or destroy the fibers in fabrics. It can also ruin photographs. Therefore, to preserve those irreplaceable memories, be sure to use paper that is acid-free. [Pg.6]

Chemical conversion processes, for high purity gases, 13 457 Chemical corrosion, of magnesium... [Pg.166]

Corrosion can be divided into two parts, chemical corrosion and electrochemical corrosion. Chemical corrosion is a direct reaction between the medium and the materials, while electrochemical corrosion is an electron transformation on different surfaces of the metal because of conductivity. In this chapter, all corrosions are referred as electrochemical corrosions. [Pg.168]

Various ceramic membranes, for example, possess differing degrees of acid/base resistance, depending on the pH value, particular phase of the membrane material, porosity, contact time and temperature. However, no quantitative data are available on the kinetics of chemical dissolution of ceramic membranes as a guide for chemical corrosion considerations. [Pg.84]


See other pages where Chemical corrosives is mentioned: [Pg.382]    [Pg.301]    [Pg.310]    [Pg.11]    [Pg.323]    [Pg.431]    [Pg.460]    [Pg.1685]    [Pg.297]    [Pg.58]    [Pg.69]    [Pg.663]    [Pg.825]    [Pg.167]    [Pg.295]    [Pg.76]    [Pg.158]    [Pg.175]    [Pg.89]    [Pg.166]    [Pg.389]    [Pg.452]    [Pg.257]    [Pg.322]    [Pg.327]    [Pg.86]    [Pg.98]    [Pg.69]    [Pg.173]   
See also in sourсe #XX -- [ Pg.12 , Pg.71 , Pg.73 , Pg.157 ]

See also in sourсe #XX -- [ Pg.55 , Pg.62 ]

See also in sourсe #XX -- [ Pg.55 , Pg.62 ]

See also in sourсe #XX -- [ Pg.55 , Pg.62 ]

See also in sourсe #XX -- [ Pg.393 ]




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