Atmospheric leaching characteristics of nickel and iron in limonitic laterite with sulfuric acid in the presence of sodium sulfite

2015 ◽  
Vol 78 ◽  
pp. 38-44 ◽  
Author(s):  
Jun Luo ◽  
Guanghui Li ◽  
Mingjun Rao ◽  
Zhiwei Peng ◽  
Yuanbo Zhang ◽  
...  
Ni-Co 2013 ◽  
2013 ◽  
pp. 117-124
Author(s):  
Guanghui Li ◽  
Wen Cai ◽  
Mingjun Rao ◽  
Qian Zhi ◽  
Tao Jiang

2021 ◽  
Vol 03 (03) ◽  
pp. 13-21
Author(s):  
Markhamat Akramovna Mutalova ◽  
◽  
Nargiza Abdurasulovna Abdurakhmanova ◽  

Currently, sulfoxide methods are of greatest interest for the practice of separation of lead-copper concentrates. The selection processes based on the use of sulfoxides such as sulfuric acid, sulfite salts, etc. should be included in this subgroup.d. Typically, these reagents are used in combination with other depressors [3]. The main advantage of sulfoxide methods is the lack of dissolution of noble metals and higher efficiency compared to many known methods. The subgroup under consideration includes a method using sodium sulfite, iron vitriol and sulfuric acid for halenite depression Currently, about thirty methods of flotation separation of lead-copper concentrates are known.


2014 ◽  
Vol 14 ◽  
pp. 57-60
Author(s):  
B Bayarmaa ◽  
D Otgonsuren ◽  
P Odonmajig

Have been obtained 2-aminoethanesulfonic acid (taurine) from ethanolamine, sulfuric acid and sodium sulfite during the synthesis in laboratory condition. The process involves two steps of reactions, the first was esterification of ethanolamine with sulfuric acid to produce the intermediate product of 2-aminoethyl ester which than was extended to the second step by sulfonation with sodium sulfite to produce 2-aminoethanesulfonic acid. Resulting product was analyzed using 1H-NMR, IR, FAB-MS analysis and examined purity characterizations of the synthesized products. DOI: http://dx.doi.org/10.5564/mjc.v14i0.200 Mongolian Journal of Chemistry 14 (40), 2013, p57-60


Tehnika ◽  
2020 ◽  
Vol 75 (2) ◽  
pp. 172-175
Author(s):  
Milisav Ranitović ◽  
Željko Kamberović ◽  
Marija Korać ◽  
Dragana Radovanović ◽  
Miroslav Sokić

2021 ◽  
Vol 173 ◽  
pp. 107212
Author(s):  
Qinghua Tian ◽  
Bo Dong ◽  
Xueyi Guo ◽  
Zhipeng Xu ◽  
Qingao Wang ◽  
...  

2015 ◽  
Vol 56 (2) ◽  
pp. 127-133 ◽  
Author(s):  
Yijie Wang ◽  
Shuming Wen ◽  
Qicheng Feng ◽  
Yongjun Xian ◽  
Dan Liu

Author(s):  
A. N. Zagorodnyaya ◽  
◽  
A. S. Sharipova ◽  
X. A. Linnik ◽  
G. S. Ruzakhunova ◽  
...  

The article presents the results of large-scale laboratory tests of obtaining selenium concentrate from the slime of the sulfuric acid workshop (hereinafter: slime) of the Balkhash copper smelting plant and the extraction of selenium from it into solution. This slime, in contrast to similar slime from non-ferrous metallurgy plants, significantly differs in chemical and material compositions, especially in the selenium content (4.6 - 12.5 wt.%). Involving it in the production sphere will increase the production of selenium by more than 20% from that obtained by the plant from copper electrolyte slime. The slime is washed with water to remove sulfuric acid, dried at 105 ° C. Selenium concentrate was obtained by sequential leaching of slime with solutions of sodium carbonate and nitric acid, selenium from the concentrate was leached with solutions of sodium sulfite (atmospheric pressure) and sodium hydroxide (high pressure, autoclave leaching). Slime, concentrate, cakes, precipitates isolated from solutions, and solutions were analyzed using modern devices of a new generation: An Optima-8300 inductively coupled plasma spectrometer, an Axios X-ray fluorescence spectrometer, an Optima 2000 atomic emission spectroscope, a D8 Advance diffractometer, a D8 Advance infrared spectrometer Avatar 370. From the slime containing, wt. %: 51.2 Pb, 12.5 Se, 3.21 Hg and other elements, a selenium concentrate was obtained with the composition, wt. %: 0.41 Pb, 59.16 Se, 15.4 Hg. The technological indicators for obtaining a concentrate are given, %: concentrate yield - 20.74, Pb recovery - 0.81, Se - 98.23, Hg - 99.50. According to XRD and IR spectroscopy, the concentrate contains elemental selenium and mercury selenide from 10 selenium substances contained in the slime (given in the article). The extraction of selenium from the concentrate into the solution was, %: sodium sulfite - 76.84, sodium hydroxide - 89.65. The pulp from opening the concentrate with sodium hydroxide solution was filtered very poorly. The filtrates contained a colloidal suspension, which could not be filtered off either under vacuum or centrifugation. Therefore, to determine the qualitative and material composition of the filtrates, salts were obtained by evaporating a certain and then neutralized volume to dryness. It was found that only elemental selenium is leached from the concentrate by solutions of both reagents, while mercury selenide remains in the cakes. Moreover, over time, elemental selenium partially precipitated again from selenium-containing sodium sulfite solutions; the salts contain only elemental selenium. An explanation is given for the transition of soluble selenium salts to its elemental state. Despite the higher recovery of selenium from the concentrate by leaching in autoclaves, taking into account the equipment, the complexity of its maintenance, filtration of the pulp and the chemical composition of the filtrate, it is preferable to use the method of leaching with sodium sulfite.


Ni-Co 2013 ◽  
2013 ◽  
pp. 117-124
Author(s):  
Guanghui Li ◽  
Wen Cai ◽  
Mingjun Rao ◽  
Qian Zhi ◽  
Tao Jiang

2018 ◽  
Vol 7 (4) ◽  
pp. 334-343 ◽  
Author(s):  
Yuanbiao Qiao ◽  
Wenhao Qin ◽  
Qingshan Li

Abstract A sealed wet curing design on sulfating Sorghum vinegar residue waste is drilled with sulfo/sulfoalkyl chemicals. Sulfation degrees in the case of reactions with sulfuric acid, sodium sulfite, sulfamic acid, benzenesulfonic acid, p-toluenesulfonic acid and sodium laurilsulfate range from 14.7 to 36.9 mg sulfo per gram waste. The C–O–S formation gives rise to accessional noncrystallinity and mesoporosity of morphology, a character for potential alternatives in catalysis. Waste sulfates are employed as candidates in catalyzing the condensation of α-glycolic acid and urea substitutes for yielding imidazolidine-2,4-dione derivatives. Catalytic and specific activities in terms of derivative productions are 2.6–34.3 (×103 U) and 0.8–5.4 U/mg sulfo, together with the maximal yields of 49.4%–97.6%. Chemical linkage of sulfo/sulfoalkyl groups manifests synergism with intrinsic acidity of waste with respect to catalysis. A rational design of green chemistry is guaranteed by no excess of chemicals and easy recyclability of catalysts.


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