BENEFICIATION STUDY OF OXIDE PRIMARY TIN ORE FROM BATUBESI BELITUNG USING FLOTATION PROCESS
The mining and processing of secondary tin ore by PT Timah Tbk. has been going on for more than half a century, resulting in depleted secondary tin ore reserves. The utilization of primary tin deposits needs to be carried out by PT Timah Tbk. to maintain the sustainability of tin metal production...
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Format: | Final Project |
Language: | Indonesia |
Online Access: | https://digilib.itb.ac.id/gdl/view/72824 |
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Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | The mining and processing of secondary tin ore by PT Timah Tbk. has been going on for more
than half a century, resulting in depleted secondary tin ore reserves. The utilization of primary
tin deposits needs to be carried out by PT Timah Tbk. to maintain the sustainability of tin metal
production. One of the areas where there are primary tin deposits is the Batubesi area, Damar
District, East Belitung Regency with iron-bearing minerals as the main mineral. To increase
tin grade, a flotation process can be carried out, so it is necessary to see the response of tin
levels and recovery.
Primary tin ore flotation concentration experiments were conducted using a Denver flotation
cell at feed P80 sizes of 38, 75, 105, and 149 microns. The collectors used were all three
sulfosinnamate-based, viz: DP-OMC-1167, and DP-OMC-1474 from BASF, and AERO 845
Promoter from Solvay. The regulator used in the DP-OMC-1167 and DP-OMC-1474 collectors
is H2SiF6, while the AERO 845 Promoter collector uses Na2SiF6. The first variation starts by
determining the best Sn content and recovery at feed sizes with P80: 149 ?m, 105 ?m, 75?m,
and 38 ?m using DP-OMC-1167 and DP-OMC-1474 collectors at pH 3.5 with a collector dose
of 200 g/ton, and AERO 845 Promoter collector and pH 5 and with a collector dose of 500
g/ton. After obtaining concentrate and tailings from the experiment, the results were analyzed
using XRF-Benchtop. The experiment continued by determining the best pH from several pH
variations, namely: 2.7, 2.9, and 3.5 for DP-OMC-1167 and DP-OMC-1474, and pH 3, 5, 7, 9
for the Solvay collector. After obtaining the optimum variables of feed P80 size and pH of each
collector, the experiment was continued to determine the best collector dosage of 100, 200,
300, 400 g/ton for DP-OMC-1167 and DP-OMC-1474 collectors, and collector dosage of 300,
400, 500, 600 g/ton for AERO 845 Promoter collector. The product of flotation concentration
was analyzed using XRF-Benchtop to see the tin content in each product.
The initial Sn content in oxide type primary tin ore is 0.29%. In the flotation concentration of
oxide type primary tin ore, Sn recovery tends to increase with the fineness of the feed P80 size
while the highest content is at -105 +75 ?m size. In the pH variation, the more acidic the
flotation atmosphere, the better the Sn content and recovery. The collector dosage used in the
experiment gave the results that the higher collector dosage generally increased Sn recovery
but decreased Sn content. The optimum variable for collector dosage was 400 g/ton for DPOMC-
1167, 300g/ton for DP-OMC-1474 collectors, and 500 g/ton for AERO 845 Promoter
collectors. The final yield obtained in this study was 0.62% Sn with a yield of 35.60%Sn. |
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