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Iron recovery

In a modification the conversion process, the jarosite residue is hydrothermaHy decomposed to hematite by autoclaving at 220—250°C. This solubilizes zinc and other metal values and the hematite has a potential for iron recovery. Hematite stockpiles are less of a problem than jarosite because hematite is denser and holds up less of the soluble metals. [Pg.402]

Ferro-heme-MHBP] —> Heme Oxygenase (catabolism, iron recovery)... [Pg.234]

If the zinc and lead levels of the metal dust are relatively low, return of the dust to the furnace for iron recovery is feasible. This method is often employed with dusts generated by the production of stainless or alloy steels but is mostly impractical for handling dusts associated with carbon steel production. Because of the use of galvanized metal scrap in the production of carbon steels, these dusts tend to be high in zinc. [Pg.24]

The metallurgy industry requires about 12 reactors for direct iron recovery on the basis of MHR-T with steam methane reforming. Therefore, not less than 150 MHR-T shall be deployed in Russian energy-consuming industries in a medium-term perspective, till 2040-2050 whereby saving over 80 bln.m3 of natural gas. MHR-T-based complexes will increase competitiveness of energy-consuming industries on the world market despite the decision on transition to world prices of natural gas supply to the Russian consumers since 2011. [Pg.74]

Allan (A7) during his studies of ashed plant materials also investigated interferences. Using an air-acetylene flame, sodium, potassium, calcium, magnesium, and phosphate had no effect. In the air-coal gas flame, as employed by Elwell and Gidley (E2), recoveries of iron were only 80-90% when the test solutions contained an excess of calcium, copper, aluminum, titanium, and zirconium. With silicon added, iron recovery was 26%. Owing to incomplete vaporization of iron in the flame, sensitivities attained are higher in the air-acetylene flame and lower in the air-coal gas flame. Since iron is subject to oxidation in the flame, fuel-rich flames are preferable. [Pg.50]

After the plastic has been removed, the batteries are charged into a cadmium furnace and the cadmium is distilled off at high temperatures and collected. Negative cadmium plates from industrial batteries are also charged into the cadmium furnace for distillation of the cadmium. Carbon is added as a reductant. The charge is heated and the cadmium distilled, then collected in a water bath. The final cadmium product is in shot form. The cadmium shot is drummed, weighed, assayed, and shipped to the customer. The residue from the cadmium furnace, mostly iron and nickel, is shredded and fed to the nickel plant for nickel and iron recovery. [Pg.117]

Oakland-Emeryville Industrial Complex. In the heavily industrialized area in Emeryville at the east end of the San Francisco Bay Bridge, pockets of metallic mercury vapor were detected at various locations on three separate visits (Figure 4). These clouds varied in concentration from 0 to 688 ng/meter. It was not possible to identify the source or sources of this mercury possible local sources include a paint plant, a chemical plant, and a scrap iron recovery facility. [Pg.87]

It is common practice to add the etheramines, which are partly neutralised (5-30%) with acetic acid, direct to the mineral slurry. As in all flotation operations, the collector is sensitive to slime in iron ore applications, and in particular for haematite, a lot of fine material is produced during the grinding process. The presence of slime will increase the collector consumption drastically, and give poor silica reduction and decrease the iron recovery. Therefore, a de-sliming stage is often used prior to flotation. In this, the iron oxide particles are depressed with starch or dextrin alkalized com starch is also commonly used. The depressant is added in a conditioner formulation before the collector is added. The pH varies between 8 to 10.5 in haematite flotation, with 10.5 being the common pH used, while magnetite flotation often takes place at pH levels of 8 to 10. [Pg.345]

High iron recoveries up to 99.5 % are obtained. The hematite produced is used as a red pigment. [Pg.194]

Time/min Yield TFe TMn Iron recovery TFe TMn Manganese recovery... [Pg.372]

STUDY ON IRON RECOVERY AND DESULFURIZATION OF PYRTTE CINDER... [Pg.553]

Study on Iron Recovery and Desulfurization of Pyrite Cinder.553... [Pg.695]


See other pages where Iron recovery is mentioned: [Pg.408]    [Pg.327]    [Pg.190]    [Pg.191]    [Pg.193]    [Pg.193]    [Pg.195]    [Pg.195]    [Pg.115]    [Pg.763]    [Pg.765]    [Pg.770]    [Pg.777]    [Pg.293]    [Pg.304]    [Pg.371]    [Pg.371]    [Pg.372]    [Pg.553]    [Pg.555]    [Pg.558]   
See also in sourсe #XX -- [ Pg.763 ]




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