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�No DiZd �oN Z/Ai t <br /> CHEMICAL OPERATING CONCENTRATIONS <br /> TANK DIMENSIONS VOLUME <br /> (GAL) <br /> DRAGOUT TANKS 25" W X 30" L X 36 " H 97.4 <br /> ANODIZING TANKS 36" W X 30" L X 36 " H 140.3 <br /> COUNTERFLOW TANKS 25" W X 30" L X 36 " H 97. 4 <br /> CHEMICAL TANKS 24" W X 30" L X 36 " H 93 . 5 <br /> OPERATING LEVEL 6" BELOW TOP <br /> CHEMICALS USED <br /> INITIAL OPERATING OPERATING <br /> CONC. CONC. CONC. <br /> ANODIZING SOLUTION WT. $ WT. $ GPL <br /> SULFOSALICYLIC ACID 6. 00 60.00 <br /> SULFURIC ACID 0.35 3 .50 <br /> SOLUTION CONC. 30.00 <br /> SOLUTION DENSITY (ASSUMPTION) 1.000 <br /> INITIAL OPERATING OPERATING <br /> CONC. CONC. CONC. <br /> DEGREASER SOLUTION WT. % WT. $ GPL <br /> SODIUM NITRITE 5.00 0.30 3.00 <br /> pH 9-10 <br /> SOLUTION CONC. 6.00 <br /> SOLUTION DENSITY (ASSUMPTION) 1.000 <br /> INITIAL OPERATING OPERATING <br /> CONC. CONC. CONC. <br /> MICRO ETCH WT. % WT. $ GPL <br /> PHOSPHORIC ACID 65.00 19.50 218.40 <br /> ETHYLENE GLYCOL N-BUTYL ETHER 20.00 6. 00 67.20 <br /> SOLUTION CONC. 30. 00 <br /> SOLUTION DENSITY 1. 120 <br /> INITIAL OPERATING OPERATING <br /> CONC. CONC. CONC. <br /> DESMUT WT. % WT. $ GPL <br /> FERRIC SULFATE 90. 00 31.50 364.77 <br /> SODIUM BIFLUORIDE 5.00 1.75 20.26 <br /> SULFURIC ACID 2.00 0.70 8. 11 <br /> SOLUTION CONC. 35. 00 <br />