Recovering molybdenite from ultrafine waste tailings by oil agglomerate flotation

被引:73
作者
Fu Jiangang [1 ]
Chen Kaida [1 ]
Hui, Wang [1 ]
Chao, Guo [1 ]
Wei, Liang [1 ]
机构
[1] Cent S Univ, Minist Educ, Key Lab Resources Chem Nonferrous Met, Sch Chem & Chem Engn, Changsha 410083, Hunan, Peoples R China
关键词
Oil agglomerate flotation (OAF); Molybdenite; Waste tailings; Recovery; CRITICAL SURFACE-TENSION; FINE PARTICLES; COAL; FLOATABILITY; SEPARATION;
D O I
10.1016/j.mineng.2012.07.006
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
Neutral oils like kerosene, diesel, transformer and rapeseed oil were used as collectors or bridging reagents in conventional flotation and oil agglomeration flotation (OAF) process, and a promising OAF process has been developed for the recycling of ultrafine molybdenite resources from the waste tailings. The average size of collected particles (d(50)(p)), agglomerates (d(50)(a)) and their distribution of the froth concentrate were determined by laser particle size analyzer or sieve analysis. Conventional flotation froth cannot catch the ultrafine particles, so it is an ineffective process to recover molybdenum metal in the waste tailings, while OAF has some advantages to recover fine minerals. And the best result was obtained from transformer oil due to its appropriate length of carbon chain, kinematic viscosity and cyclical structure. The oil amount plays a very important role on average size of the particles, with the increase of transformer oil from 2.0 to 13.8 kg/t, d(50)(d) increases from 0.15 to 0.68 mm and d(50)(p) decreases from 9.06 to 2.05 mu m. This finding suggests the bigger the d(50)(a), the smaller the d(50)(p), and the higher the recovery of molybdenite. The appropriate conditions for recovering ultrafine molybdenite were determined as follows: dosage of frother: 0.5 kg/t, natural pH: 6.2, stirring time: 3 min, and stirring intensity:400-600 r/min. Lastly, the closed cycle test and industrial application in the producing scale of 500 t/d were carried out, and result shows 95% molybdenum was recovered with a satisfied grade of 22.62%. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:133 / 139
页数:7
相关论文
共 39 条
[1]
Some factors affecting spherical oil agglomeration performance of coal fines [J].
Aktas, Z .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 2002, 65 (3-4) :177-190
[2]
Coal recovery from fines cleaning wastes by agglomeration with colza oil:: a contribution to the environment and energy preservation [J].
Alonso, MI ;
Valdés, AF ;
Martínez-Tarazona, RM ;
Garcia, AB .
FUEL PROCESSING TECHNOLOGY, 2002, 75 (02) :85-95
[3]
Floatability of chalcopyrite and molybdenite in the presence of lignosulfonates. Part II. Hallimond tube flotation [J].
Ansari, Anita ;
Pawlik, Marek .
MINERALS ENGINEERING, 2007, 20 (06) :609-616
[4]
Azevedo MAD, 2000, TAPPI J, V83, P66
[5]
Application of the Box-Wilson experimental design method for the spherical oil agglomeration of coal [J].
Cebeci, Y ;
Sönmez, I .
FUEL, 2006, 85 (03) :289-297
[6]
A study on the relationship between critical surface tension of wetting and oil agglomeration recovery of calcite [J].
Cebeci, Y ;
Sönmez, I .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2004, 273 (01) :300-305
[7]
Investigation of spherical oil agglomeration properties of celestite [J].
Cebeci, Y ;
Sönmez, I .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2004, 273 (01) :198-204
[8]
Investigation of kinetics of agglomerate growth in oil agglomeration process [J].
Cebeci, Y .
FUEL, 2003, 82 (13) :1645-1651
[9]
The investigation of coal-pyrite/lignite concentration and their separation in the artificial mixture by oil agglomeration [J].
Cebeci, Y ;
Sönmez, I .
FUEL, 2002, 81 (09) :1139-1146
[10]
INFLUENCE OF AIR ON OIL AGGLOMERATION OF CARBONACEOUS SOLIDS IN AQUEOUS SUSPENSION [J].
DRZYMALA, J ;
MARKUSZEWSKI, R ;
WHEELOCK, TD .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 1986, 18 (3-4) :277-286