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Red Mud Addition in the Raw
Meal for the Production
of
Portland Cement Clinker
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Jarosite-Alunite
Addition in the Raw Meal for the Production
of Portland Cement Clinker
The jarosite–alunite
group of isostructural minerals is described by the general formula M(FexAlyCrz)(SO4)2(OH)6,
in which “M” may be Na+, K+, NH4+
or H3O+ and x+y+z=3. For x=3, the formula
represents jarosite, whereas for y=3 it represents alunite. The precipitate is produced at some stage of a new hydrometallurgical process [1-3], which was developed at the laboratory of Metallurgy of the National Technical University of Athens in order to extract, economically and efficiently, nickel and cobalt from low-grade nickel oxide ores. According to the above process, the ores are subjected to heap leaching with dilute sulfuric acid and the resulting leach liquors, containing nickel, cobalt, iron, aluminum and chromium, are then treated, at atmospheric pressure and at temperatures not exceeding 100oC, to remove iron, aluminum and chromium before nickel and cobalt recovery. The jarosite-alunite precipitation is a hydrolysis reaction and can be represented by the equation:
2[Fe2(SO4)3](aq) + [Al2(SO4)3](aq) +M2SO4 +12H2O ® 2M[Fe2Al(SO4)2(OH)6](s) +6H2SO4
The addition of jarosite-alunite precipitate by 1% in the raw meal did not affect either the sintering or the hydration process during Portland cement production. More specifically, the sample with jarosite-alunite presented the following characteristics:
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Use of Gypsum/Brucite Mixed Precipitate Instead of Gypsum in Portland Cement
The Laboratory of Metallurgy of the National Technical University of Athens has developed a new integrated hydrometallurgical method, suitable to treat, efficiently and economically, low-grade nickel oxide (laterite) ores. It involves heap leaching of the ore by dilute sulphuric acid at ambient temperature, purification of the leach liquor and recovery of nickel and cobalt. A typical composition of the pregnant solution produced from heap leaching of Greek low-grade nickeliferous laterites with sulphuric acid is: Ni2+ = 5.0 mg/l, Co2+ =0.6 g/dm3, Fe3+=22.0 mg/l, Al3+=6.0 mg/l, Cr3+=1.0 mg/l, and Mg2+=8 mg/l. Iron, aluminium and chromium are removed from the leach liquor by hydrolytic precipitation after which nickel and cobalt are recovered from the purified liquor by solvent extraction. The resulting final solution contains only magnesium, which must also be removed in order to:
The precipitation of gypsum/brucite was carried out in 5 dm-3, five-necked, round bottomed split reactors at 25 oC, using 1.1 times the stoichiometric quantity of Ca(OH)2 required to precipitate all of the magnesium. Calcium hydroxide was added in solid form. The reaction time was approximately two hours. Equilibrium pH was around 10.
The precipitate that was obtained composed of well-crystallized gypsum (CaSO4.2H2O) and aggregates of fine crystallites of brucite (Mg(OH)2). The mixture exhibited excellent filtering properties. The addition of the above precipitate, instead of natural gypsum, by 4.1%, 5.2% and 6.3% in clinker did not adversely affect the properties of the cement mixtures produced. More specifically, all the cement mixtures tested presented similar characteristics, such as grindability, compressive strength and expansion, with the reference sample. Regarding the setting times of the mixtures, the replacement of natural gypsum with the gypsum/brucite precipitate accelerated the cement setting, within acceptable limits, a fact which was attributed to the lower solubility of SO3 contained in the precipitate than that in natural gypsum.:
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