scholarly journals Ion exchange treatment of solution produced in acid leaching of uranium ore from the Kitts Property of British Newfoundland Exploration LTD. , Newfoundland sample Nos. 4/58-12, 5/58-4

1958 ◽  
Author(s):  
A J Gilmore ◽  
W A Gow
2015 ◽  
Vol 5 (2) ◽  
pp. 33-38
Author(s):  
Quang Thai Le ◽  
Minh Tuan Pham ◽  
Nguyen Quynh Trinh ◽  
Khac Tuan Vu ◽  
Hong Ha Nguyen ◽  
...  

Ion exchange is one of the most popular techniques for recovery and purification of uranium from sulfuric acid leaching solution, especially for recovery of uranium from a low uranium containing solutions. Resins commonly used are strong base or weak base anion resins with amine functional group. The anionic form of resins may be NO3-, Cl- , SO­42- or OH-. The selection of  a resin depends on the uranium total exchange capacity, selectivity and the cost. The previous studies often use Amberlite IRA-420 for concentration and purification of uranium solution from Pa Lua sandstone ores. This is a good and suitable resin but high price. To diversify the resins and reduce the costs, instead of IRA-420, the authors tested two commercial resins Indion GS300 (India) and Purolite A400 (UK) in the processing of uranium solution from sandstone ores. The results showed that the uranium total exchange capacity of  these resins is only about 80 - 85% over  Amberlite IRA-420, but these resins should be able to be used instead of Amberlite IRA-420 due to their low cost and availability in Vietnam.


2020 ◽  
Vol 12 (21) ◽  
pp. 9086 ◽  
Author(s):  
Chen-Piao Yen ◽  
Song-Yan Zhou ◽  
Yun-Hwei Shen

The treatment and disposal of municipal solid waste incineration (MSWI) fly ash containing significant amounts of dissolvable salts and heavy metals is a seriously challenge. At present, the common treatment method for MSWI fly ash in Taiwan is the cement-based stabilization/solidification (S/S) process. In this work, an integrated hydrometallurgical process for the treatment of MSWI fly ash was evaluated. Ca was first recovered by combining water washing and ion exchange sequentially. Meanwhile, Zn in the water-washed fly ash was recovered by combining acid leaching and ion exchange sequentially. Combining the water washing efficiency of 30% on raw ash and the acid leaching efficiency of 40% on pre-washed ash, a total of 58% mass reduction rate of fly ash was achieved. In addition, an 80% Zn and 58% Ca recovery was achieved.


Catalysts ◽  
2020 ◽  
Vol 10 (12) ◽  
pp. 1398
Author(s):  
Zdeněk Tišler ◽  
Anna Klegová ◽  
Eliška Svobodová ◽  
Jan Šafář ◽  
Kateřina Strejcová ◽  
...  

In this work, we studied the effect of alkali-activated zeolite foams modifications on properties and catalytic activity of cobalt phases in the process of catalytic decomposition of N2O. The zeolite foam supports were prepared by alkali activation of natural zeolite followed by acid leaching and ion exchange. The cobalt catalysts were synthesised by a different deposition technique (direct ion exchange (DIE) and incipient wetness impregnation (IWI) method of cobalt on zeolite foams. For comparison, catalysts on selected supports were prepared and the properties of all were compared in catalytic tests in the pellet form and as crushed catalysts to determine the effect of internal diffusion. The catalysts and supports were in detail characterized by a variety of techniques. The catalyst activity strongly depended on the structure of support and synthesis procedure of a cobalt catalyst. Ion exchange method provided active phase with higher surface areas and sites with better reducibility, both of these factors contributed to higher N2O conversions of more than 80% at 450 °C. A large influence can also be attributed to the presence of alkali metals, in particular, potassium, which resulted in a modification of electronic and acid base properties of the cobalt oxide phase on the catalyst surface. The promotional effect of potassium is better reducibility of cobalt species.


2020 ◽  
Vol 8 (4) ◽  
pp. 103873
Author(s):  
Antoine Leybros ◽  
Jean-Christophe Ruiz ◽  
Thibault D’Halluin ◽  
Egle Ferreri ◽  
Agnès Grandjean

1982 ◽  
Vol 22 (01) ◽  
pp. 132-140 ◽  
Author(s):  
R.S. Schechter ◽  
Paul M. Bommer

Abstract The results of the first restoration effort for a pilot-scale acidic leaching of a uranium ore body in the U.S. are given. The project was performed under a cooperative agreement between the USBM and a joint venture consisting of Rocky Mountain Energy, Mono Power Co., and Halliburton Co. The leaching phase is described only briefly; it was reported earlier by Tweeton et al. Leaching was done with H2SO4 (pH range of 1.6 to 3.9) and H2O2 (80 to 1,000 ppm) over an 11-month period. The restoration phase begun in September 1978 and was completed in 11 months. Water samples were taken from observation wells located between injection and production wells while the leaching solution was decreased in strength. Groundwater quality in the leached ore zone was restored by diluting and neutralizing effects of injecting native groun dwater and treated water produced from recovered solution. Recovered water was purified by a combination of chemical precipitation and reverse osmosis. In-situ measurements of pH, Eh, dissolved oxygen, conductivity, and temperature were made by a downhole probe in one of the wells. Water samples were taken and analyzed for U. V, Na, K, Ca, Mg, SO4, P, Cl, F, Fe, Mn, Si, Zn, As, and Se. Introduction The USBM and the companies listed previously entered into a cooperative agreement aimed at modeling in situ leaching (ISL) of uranium with sulfuric acid at the venture's Nine-Mile Lake test site near Casper. WY (Fig. 1). Acid leaching of uraniferous ores is relatively unproved because most earlier ISL systems involved use of alkaline leachants. This report describes the first restoration of a pilot-scale acidic-leached ore body inthe U.S. The results of an 11-month leaching phase conducted on afive-spot pilot test area (Pattern 2, Fig. 2) were previously reported bythe Bureau of Mines. The study presented here consisted of weekly in-situ determination of water quality parameters within the ore zone being restored plus additional water analysis in the laboratory. Geology The uranium mineralization occurs in Teapot sandstone members of the Upper Creataceous Mesaverde formation. The project site is located approximately 15 km (9 miles) north of Casper in Natrona County. The leached uranium ore (and aquifer) restored to baseline in this study was a bedded deposit ranging from 155 to 165 m (508 to 541 ft) deep. The sandstone contains quartz, feldspar, and minor amounts of mica, black (organic-containing) minerals, glauconite, carbon aceous fragments, blue to earthy clayinclusions, and disseminated argillaceous materials. The deposit isamenable to acidic leaching because of the relatively low carbonate content. The mineralization is typical of a roll-front type deposit. The principal uranium mineral is uraninite (UO2), with minor amounts of coffinite U(SiO4) 1-X (OH) 4X. Further de tails are found in the operators environmental report to the U.S. Nuclear Regulatory Commission (NRC). Hydrology The Teapot sand stone is an artesian aquifer confined by the overlying Lewisshale and the underlying Pumpkin Buttes shale. The formation dips to theeast-northeast at about 7 with ground water movement in that direction at about 4 m/a (14 ft/yr). The aquifer is recharged at the out crop approximately 3 km (2 miles) west of the test area. Groun dwater in the project area is marginally acceptable for live stock watering or industrial use. SPEJ P. 382^


1987 ◽  
Vol 17 (2) ◽  
pp. 229-238 ◽  
Author(s):  
K.E. Haque ◽  
J.J. Laliberté ◽  
J. Pruneau

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