Separator STET pojasa

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ST oprema & Tehnologija LLC (STET) Triboelectrostatic belt separator (Slika 1) ima sposobnost obrade finih čestica iz 1995 separating Unburned carbon from fly ash minerals in coal-fired power plants in North America, Europe and Asia to produce a concrete grade Pozzolan for use as a cement substitute. 1 Kroz testiranje pilot postrojenja, In-plant demonstracioni projekti i/ili komercijalne operacije, STET’s separator has demonstrated Beneficiation of many minerals including potash, barit, calcite, and talc.2

Since the primary interest in this technology has been its ability to process particles less than 0.1 Mm, Ograničenje konvencionalnih separatora slobodnog pada i drum rolla, the upper particle size limit of STET’s current design has not been a focus of the development of the technology in the past. Međutim, efforts are under way to increase it by design changes. STET currently manufactures two sizes with nominal capacities of 40 i 23 metric tonne per hour.

Slika 1: ST oprema & Technology’s Triboelectric Belt Separator

Figure 1: ST Equipment & Technology’s Triboelectric Belt Separator

The principles of operation of the STET separator are illustrated in Figures 2 & 3. Čestice se naelektriziraju triboelektričnim efektom putem sudara čestica do čestica u distributeru zraka i unutar jaza između elektroda.. Primijenjeni napon na elektrodama je između ±4 i ±10kV u odnosu na tlo., davanje totalne razlike u voltaži 8 da 20 kV. Pojas, koja je napravljena od neprovodljive plastike, Veliko je interesovanje za 60% otvoreno podrucje. The particles can easily pass through the openings in the belt.

Slika 2: Schematic of STET Separator

Figure 2: Schematic of STET Separator

Feed Capacity: 40TPH Dimensions: 9.1m L x 1.7m W x 3.2m H

The flow patterns and particle-to-particle contact within the electrode gap that is established by the moving belt are key to the effectiveness of the separator. Po ulasku u jaz između elektroda, negativno naelektrisane čestice privlače sile električnog polja na donje pozitivne elektrode.. Pozitivno naelektrisane čestice privlače negativno naelektrisanu gornju elektrodu.. Brzina kontinuiranog pojasa je promjenljiva od 4 da 20 m/s. The geometry of the belt cross-direction strands serves to sweep the particles of the electrodes moving them towards the proper end of the separator and back into the high shear zone between the oppositely moving sections of the belt. Zato što je gustina broja čestica tako visoka unutar jaza između elektroda. (approximately one-third the volume is occupied by particles) Struja je veoma uznemirena, Postoji mnogo sudara između čestica i optimalno punjenje se odvija kontinuirano u cijeloj zoni razdvajanja.. The counter-current flow induced by the oppositely moving belt sections and the continual re-charging and re-separation creates a countercurrent multistage separation within a single apparatus. This continuous charging and recharging of particles within the separator eliminate the need for any “charger” system prior to introducing material to the separator, thus removing a serious limitation on the capacity of electrostatic separation. Izlaz ovaj razdjelnik je dva potoka, a concentrate, and a residue, bez middlings potok. Efikasnost ovog separatora se pokazala ekvivalentnom približno tri faze odvajanja slobodnog pada sa recikliranjem sredine.

Slika 3: Electrode Gap of STET Belt Separator

Figure 3: Electrode Gap of STET Belt Separator

The STET separator has many process variables that enable optimization of the trade-off between product purity and recovery that is inherent in any Beneficiation process. The coarse adjustment is the feed port through which the feed is introduced to the separation chamber. The port furthest from the discharge hopper of the desired product gives the best grade but at the expense of a lower recovery. A finer adjustment is the speed of the belt. The electrode gap, which is adjustable between 9 i 18 Mm, and the applied voltage (±4 to ±10 kV) are also important variables. The polarity of the electrodes may be changed which aids in the separation of some materials. Pretreatment of feed material by precise control of trace moisture content (as measured by feed relative humidity) is important to achieve optimum separation results. The addition of trace amounts of charge-modifying chemical agents can also aid in optimizing the process.

Kao što je gore navedeno, the initial commercial application of the belt separator has been a separation of coal char from the glassy Aluminosilicate mineral from fly ash from coal-fired power plants. This technology is unique among electrostatic separators in its ability to separate fly ash, which typically has a mean particle size less than 0.02 Mm. The STET separator has also been proven to effectively separate magnesite from talc, halite from kieserite and sylvite, silicates from Bart, and silicates from calcite.3 The mean particle size of all of these feed materials has been in the range of 0.02 and 0.1mm. Examples of separations for several materials are included in Tablica 1.

Tablica 1 – Example Separations

OdvajanjeHranitiProizvodOporavak
Calcium Carbonate - Silikati9.5% Acid Insols<1% A.I.89% CaCO3
Talk - Magnezita58% talk95% talk77% talk
88% talk82% talk
Kierserite + KCl - NaCl11.5% K2O27.1% K2O90% K2O
12.2% kieserite31.8% kieserite94% kieserite
64.3% NaCl14.3% NaCl92% NaCl reject
Fly Ash Mineral - Indigo6.3% carbon1.8% carbon88% mineral
11.2% carbon2.1% carbon84% mineral
19.3% carbon2.9% carbon78% mineral

In theory, since particle charging depends upon the triboelectric effect, any two minerals that are liberated from each other (conductor- conductor or nonconductor-conductor) can be separated by this method. Other potential applications include magnesite-quartz, feldspar-quartz, mineralni pijesak, other potash mineral separations, i
Phosphate-calcite-silica separations.


 

1 Bittner, J.D., Gasiorowski, S.A., Bush, T.W.,, Hrach, F.J., Separation technologies’ automated fly ash beneficiation process selected for new Korean power plant, Proceedings of 2013 World of Coal Ash conference, April 22-25, 2013. 2 Bittner, J.D., Hrach, F.J., Gasiorowski, S.A., Canellopoulus, L.A., Guicherd, H. Triboelectric belt separator for Beneficiation of fine minerals, SYMPHOS 2013 – 2nd International Symposium on Innovation and Technology for the Phosphate Industry. Proceed Engineering, Vol. 83 PP 122-129, 2014. 3 Bittner, J.D., Flynn, K.P., Hrach, F.J., Expanding applications in dry Triboelectric separation of minerals, Proceedings of the XXVII International Mineral Processing Congress – IMPC 2014, Santiago, Čile, Oct 20 – 24, 2014.