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Rudarstvo 2011 / Mining 2011H 9 C 4H 9 C 4S||P — S -1 Na ++C —C C| || |C C— C — N = C – S -1+Na 2 S+RR⁄⁄NH — C\SS -1U vezi sa ovim proizilazi da je primenjen reţim reagenasa sa AP 3404 bolje prilagoĊen mineraloškimkarakteristikama rude, protoku masa i po obimu instaliranim jedinicama. Pri tome, veća efikasnost,primenjenog kolektora za flotacijsku koncentraciju bakra i plemenitih metala, izraţena je njegovomhemijskom prirodom, što je opet posledica od primenjene vrste i naĉina rasporeda atoma koji ga grade.Zbog toga su, za intenzivniju promenu naelektrisanja površina minerala bakra i plemenitih metala,primenom AP 3404 naroĉito znaĉajne ĉetiri sintetizovane specifiĉne molekulske strukture. Njihovproizvod reakcije u flotacijskoj koncentraciji: Cu, Au i Ag, je abstrakcija mineralnih zrna mase 3 : 1molg u odnosu na ksantate. Jer, više molekulska struktura, zbog izraţajnijeg afiniteta, dovodi do većenjihove migracije na površine minerala. Sam mehanizam atsorpcije se dešava uz prisustvomolekulskih struktura, koje su pomoćne u strukturi kolektora. One pomaţu jaĉe izraţenoj atsorciji napovršine Cu, Au i Ag. Iz razloga, što površine ovih minerala, postaju jaĉe hidrofilne za višemolekulsku strukturu kolektora AP 3404, nego u svom prirodnom stanju i sa ksantatima . Zbog tihsvojstava, adsorcija kolektora iz grupe ditiofofinata AP 3404 na površine minerala Cu, Au i Ag,ispitatna je sa eksperimentalnim dizajnom, slike 2 i 3, od niţih koncentracija u pulpi do optimalnetehnološke vrednosti. S obzirom da selektivniji i aktivniji kolektori utiĉu na tok masa u procesudomeljavanja i preĉišćavanja, znatno većom koncentracijom korisnih komponenata u grubomkoncentratu, koji, zbog toga, po svojoj manjoj masi, omogućuje potpunije mlevenje do graniĉnekrupnoće koju iziskuje proces koncentracije u preĉišćavanju. Zbog toga je, u procesu domeljavanja ipreĉišćavanja, potrebno tehniĉko – tehnološko usklaĊivanje proizvodnih faktora, na bazi rezultatadobijenih primenom kolektora sa sloţenijim molekulskim strukturama.U tom cilju, zapoĉeto je optimiziranje dopunskog ciklusa mlevenja i klasiranja u flotaciji Majdanpek.363
ala flotiranjaHala mlevenjaiz postr. za pr. reag.Postrojenje za pripremu irastvaranje reagenasa ikreĉaRudarstvo 2011 / Mining 2011Slika 1: TEHNOLOŠKA ŠEMA PRIPREME I RAZVODA REAGENASA I KREĈA FLOTACIJI IIIAP3404Z11A76REAGENSNI RADNI REŢIM:PERIOD I II IIIIVod14.10.20101 NaPX 24g/t 30g/t 24g/t 20g/tZ11dnevnirezervoari2 AP3404 - 5g/t 8g/t 12g/t3 A76 9g/t 9g/t 9g/t 9g/t4 SKIK-BZ 2020 14g/t - - -dnevni rezervoariA76AP3404 Z11IXVIII54XI55XFLOTACIJA IIIA76A76AP3404AP3404Z11A242364dopunski mlinovi I i II
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Rudarstvo 2011 / Mining 2011proizvo
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stanje i perspektive u rudarstvu i odrÅ£ivi razvoj mining present state ...

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