Abstract: A fluid treatment plant has a filter module including at least a first filter and a second filter connected in series and connectable to a supply of fluid. A pump is fluidly connected to the filter module and a controller with a fluid quality sensor is connected to detect a quality of the fluid between the first filter and the second filter. A filter module detector is connected to the controller configured to uniquely detect a filter module connected to the pump, and the controller is controls the pump responsively to a signal from the fluid quality sensor and the module detector. The controller is configured to continue pumping based on output of the quality sensor and/or based on output from the filter module detector.

Abstract: A method for separating gold and/or silver from copper or other contaminant metals is provided in which a suitable filter membrane (64), particularly a nanofilter, is used to form a retentate (134) containing most of the multivalent metal cyanide complexes and a permeate (135) containing most of the precious metal cyanide complexes. The process is particularly applicable to the recovery of gold and/or silver from ores containing these metals and one or more contaminant metals. The precious metal can thereafter be recovered from the permeate (135) and the metal in the multivalent metal cyanide complex from the retentate (134).

Abstract: A method for removing solid wastes from an organic extractant-based SX/EW copper processing system. A lixivant is initially applied to copper ore, followed by mixing of the copper-containing lixivant product with an organic extractant. The organic extractant (which contains extracted copper ions) is then contacted with an electrolyte solution. At least part of the remaining organic fraction after electrolyte contact is passed through a filtration membrane (either an ultrafiltration or microfiltration membrane) to remove solid wastes. The filtered organic fraction is then reused within the system, followed by electrowinning of the copper-containing electrolyte to recover purified copper. Alternatively, the organic extractant may be membrane-filtered after initial contact with the copper-containing lixivant product to remove solid wastes from the organic extractant.

Abstract: The present invention is directed to a process for removing various contaminants (e.g., organic collectors, contaminant metals or spectator ions, and/or suspended and colloidal solids) from process streams in leaching processes. The contaminant removal is performed by one or more membrane filtration systems (e.g., nanofilters, ultrafilters, and/or microfilters) treating process streams including, the pregnant leaching solution, the barren raffinate, and the lean and rich electrolytes.

Abstract: A method for separating gold from copper in a gold ore processing system. Gold ore containing elemental gold and elemental copper is treated with an aqueous cyanide solution to produce a liquid product containing a gold-cyanide complex and a copper-cyanide complex. The liquid product is then delivered to a nanofiltration membrane which prevents the copper-cyanide complex from passing therethrough while allowing passage of the gold-cyanide complex. Nanofiltration of the liquid product specifically produces (1) a retentate which contains the copper-cyanide complex; and (2) a permeate which contains the gold-cyanide complex. In this manner, the gold-cyanide complex is effectively separated from the copper-cyanide complex. The permeate is then treated (e.g. with activated carbon or elemental zinc) to ultimately obtain elemental gold therefrom. The copper-cyanide complex may either be discarded or treated to recover elemental copper from the complex.

Abstract: A method for removing solid wastes from an organic extractant-based SX/EW copper processing system. A lixivant is initially applied to copper ore, followed by mixing of the copper-containing lixivant product with an organic extractant. The organic extractant (which contains extracted copper ions) is then contacted with an electrolyte solution. At least part of the remaining organic fraction after electrolyte contact is passed through a filtration membrane (either an ultrafiltration or microfiltration membrane) to remove solid wastes. The filtered organic fraction is then reused within the system, followed by electrowinning of the copper-containing electrolyte to recover purified copper. Alternatively, the organic extractant may be membrane-filtered after initial contact with the copper-containing lixivant product to remove solid wastes from the organic extractant.

Abstract: A treatment system for removing metal ions from liquids. A metal ion-containing liquid (e.g. water or an acidic mining leachate) is first passed through a nanofiltration membrane system to produce a metal ion-rich retentate and a permeate. The retentate may be saved for metal recovery or discarded. To purify the permeate and remove residual metal ions therefrom, it may thereafter be passed through one or more columns containing metal ion-extracting materials. Specifically, the permeate is passed through at least one and preferably multiple columns filled with porous polymer beads having metal ion extracting agents therein (e.g. biomass materials). As a result, purified liquid is produced. When saturated with metal ions, each bead-containing column is successively cleaned with acid solutions.

Abstract: A treatment system for removing metal ions from water. Contaminated water is first passed through a nanofiltration membrane system, and then through one or more columns having ion-extracting materials therein. The nanofiltration membrane system involves at least one and preferably multiple nanofiltration membrane units which are capable of removing metal ions from water. To remove any residual metal ions from the permeate generated by the nanofiltration membrane system, the permeate is passed through at least one and preferably multiple columns filled with porous polymer beads having metal ion extracting agents therein (e.g. biomass materials). As a result, highly purified water is produced. When saturated with ions, each bead-containing column is successively cleaned with acid solutions.

Abstract: A treatment system for removing metal ions from water and a method for cleaning the system. Contaminated water is passed through a plurality of columns having ion-extracting agents therein. When saturated with ions, each column is successively cleaned with primary and secondary acid solutions from separate vessels. When the primary acid is saturated with ions, it is membrane-filtered to remove ions therefrom. The secondary acid is then directed into the primary acid vessel, with the purified primary acid being routed back into the system (preferably into the second vessel) for reuse. The column is then rinsed with water, washed with an alkali solution (periodically concentrated using a water-permeable membrane), and rinsed again with water. The system preferably uses three columns, all of which are successively cleaned in the manner described above.

Abstract: An ACM removal assembly is disclosed, including: a nozzle for directing a pressurized fluid against ACM for dislodging the ACM; a fluid supply reservoir connected to the nozzle; a housing which supports the nozzle and capturingly receives spent fluid and dislodged ACM; and a material handing and separating system which includes coarse separating apparatus for coarsely separating the spent fluid from the dislodged ACM and fluid return conduit for returning coarsely separated fluid to the fluid supply reservoir.