519 - 532 |
Biological treatment of precious metal refinery wastewater: A review Dobson RS, Burgess JE |
533 - 540 |
Interactions between sulphides and manganese dioxide in thiosulphate leaching of gold ores Feng D, van Deventer JSJ |
541 - 551 |
Application of a cellular automata based simulation model of size reduction in mineral processing Guimaraes C, Durao F |
552 - 558 |
New basis for adsorption of ionic pollutants onto modified zeolites Oliveira CR, Rubio J |
559 - 565 |
Leaching and CIL processes in gold recovery from refractory ore with thiourea solutions Gonen N, Korpe E, Yildirim ME, Selengil U |
566 - 573 |
Fundamental study on talc-ink adhesion for talc-assisted flotation deinking of wastepaper Liu J, Vandenberghe J, Masliyah J, Xu Z, Yordan J |
574 - 580 |
Fundamentals on the spigot capacity of dense medium cyclones Magwai MK, Bosman J |
581 - 590 |
Gold cementation from thiocyanate solutions by iron powder Wang ZK, Chen DH, Chen L |
591 - 599 |
Bioleaching and chemical leaching as an integrated process in the zinc industry de Souza AD, Pina PS, Leao VA |
600 - 608 |
Floatability of chalcopyrite and molybdenite in the presence of lignosulfonates. Part I. Adsorption studies Ansari A, Pawlik M |
609 - 616 |
Floatability of chalcopyrite and molybdenite in the presence of lignosulfonates. Part II. Hallimond tube flotation Ansari A, Pawlik M |
617 - 620 |
Comparison of biological ammonium removal from synthetic metal refinery wastewater using three different types of reactor Manipura A, Barbosa VL, Burgess JE |
621 - 624 |
Physicochemical studies of smithsonite flotation using mixed anionic/cationic collector Hosseini SH, Forssberg E |
625 - 628 |
Boundary conditions for gas rate and bubble size at the pulp-froth interface in flotation equipment Yianatos JB, Henriquez F |