Abstract
Process for Ekstraktion gold (Au) and silver (Ag) of ore can use cedimentation system (precipitation) zinc (Zn) powder. But lately the conventional process is already considered almost inefficient and not selective, because metals other than gold and silver are precipitate (Dayton, SH, 1987). The current attention focused on absorption system using activated carbon for the extraction of gold and silver in the processing of mineral called carbon in leach (CIL). Activated carbon is used to process the CIL has its own characteristics. So, activated carbon required a special study to obtain activated carbon according to the characteristics of CIL process and the important think of activated carbon is number of iodine (iodine number) so that could be optimal for absorption process. Activated carbon from coal sub - bituminous PT.BA with activation performed in this study has not been reached in accordance with the required characteristics for CIL process that is supposed to be iodine number of 700 mg / g and only reached a maximum of 493 mg / g. Likewise, the relative ash content that should not meet that 4% to 4.1188% results. While the other parameters have been reached as required. the highest iodine number of 493 mg / g achieved with variable temperature experiments at 900oC with -48 +100 mesh fraction for 1 hour with iodine number of 493 mg / g, and also have a percentage of loss during the activation process smallest 45.15%. Here are the specifications of activated carbon from sub - bituminous coal results and qualified of activation process for the purification process using the CIL: Percent moisture : 2,5187 % (max 5%) Percent ash : 4,1188 % (max 4%) Percent fix carbon : 88,5027 % (min 80 %) Iodin Number : 493 mg/g (min 700 mg/g) Based on the study in making activated carbon using iodine number coalite to obtain up to 1000 mg / g required a specific study using the chemical activation process or physical activation with rotary kiln system.
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