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CC PACKET 09251984
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CC PACKET 09251984
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12/30/2015 3:59:52 PM
Creation date
12/30/2015 3:59:16 PM
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SP Box #
16
SP Folder Name
CC PACKETS 1981-1984 & 1987
SP Name
CC PACKET 09251984
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The advantages of.the ion exchange treatment system are: the Activated Carbon Adsorption <br /> water savings are significant; the feedstream can be dilute as <br /> is the case in rinse waters; and the energy consumption is low. The plating baths in electroplating and printed circuit board <br /> The disadvantages are: capital costs are high; chemical, labor manufacturing shops normally become contaminated with a variety <br /> and maintenance costs are high; the equipment is complex; and of substances. The important contaminants of concern to the <br /> the performance of the system depends on the operator. proposed metals recovery system are those that adversely affect <br /> the ion exchange resins. These important contaminants include <br /> strong oxidants that may physically break down the resin, <br /> Electrolytic Recovery chelating agents and oils or other organics that may gradually <br /> k foul the resin and various suspended solids that may foul the <br /> This is a process in which there is an electrochemical i ion exchange column. <br /> reduction of metal ions to elemental metal. In the <br /> electrochemical cell a sufficient level of direct current Therefore, it is essential that these organic contaminants be <br /> voltage is applied across two electrodes, overcoming the removed from the waste water prior to the ion exchange <br /> reversible electromotive force of the cell, causing the metal treatment in order to preserve the longevity of the resins. <br /> ions to plate out at the cathode. The cathode is the electrode Activated carbon performs this required step by the process of <br /> at which electrons are taken up by the metal and reduction adsorption. <br /> occurs. The other electrode is the anode. Oxidation occurs <br /> here and electrons are given up to the electrode. There are three important steps in the process of adsorption of <br /> dissolved organics in the waste water by the granular activated <br /> The electrolytic recovery of metals has been proven technically carbon. First is the transport of the solute through a film on <br /> feasible by the primary and secondary copper industry. Copper the surface of the activated carbon granule to the exterior <br /> is purified using these electrochemical techniques. surface of the carbon. The second step is the diffusion of the <br /> Electrolytic recovery is also used to recover tin, silver, solute through the pores of the carbon to its interior. <br /> copper and other metals from plating and etching drag out Finally, adsorption of the solute occurs on the interior <br /> wastes in some electroplating plants. surfaces of the pore and capillary spaces of the activated <br /> carbon. <br /> Electrolytic recovery was chosen as the metal recovery process <br /> for the copper and cadmium wastes entering the Facility. The effectiveness of adsorption by activated carbon is <br /> Copper will be recovered using a large electrowinning tank dependent upon a number of factors. The physical and chemical <br /> while cadmium recovery will require a smaller plating cell. nature of the solution, the nature of the material to be <br /> adsorped, including its molecular size and polarity, the type <br /> Zinc and nickel waste streams are believed to be contaminated of contacting system (carbon column for example) and its mode <br /> with copper and other metals along with other impurities. The of operation, and the nature of the carbon itself. <br /> electromotive series position of nickel and zinc are higher <br /> than the contaminating metals so their recovery by this Activated carbon canisters would be used at the industrial <br /> electrolytic process is uneconomical. shops as a prefilter to the ion exchange system. At the <br /> Facility there will be two activated carbon columns installed <br /> The important factors which determine the efficiency of in series. At the Facility the main function of the carbon <br /> electrolytic recovery of metals are, water temperature, water would be to trap suspended solids and remove organics from <br /> flow rate, the current density and electrode area of the cell nickel and copper waste waters which arrive at the facility in <br /> (for plating), the type of metal and metal concentration in the bulk shipments. <br /> water, and the types of contaminants and their concentration in <br /> the water. Once the carbon columns have reached their capacity they must <br /> be replaced with fresh activated carbon columns. In order to <br /> There is also a possibility of reusing the spent electrolytic be disposed of they will first be dried and then incinerated. <br /> solutions as a regenerant solution for the ion exchange resins. The ash may then be disposed of in a sanitary landfill. Since <br /> no heavy metals are adsorped by the carbon, none will be <br /> present in the ash. <br /> A-4 A-5 <br />
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