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IMPLEMENTATION OF MATHEMATICAL EQUATION FOR CALCULATING ALUMINA EXTRACTION FROM BAUXITE TAILING DIGESTION Husaini Husaini
Indonesian Mining Journal Vol 19, No 1 (2016): INDONESIAN MINING JOURNAL Vol. 19 No. 1 February 2016
Publisher : Puslitbang tekMIRA

Research on bauxite tailing digestion using pressurized batch reactor at a feed capacity of 86.66 kg had been conducted. Bauxite with -150 mesh of particle size is reacted with 42.15 kg of caustic soda (433.49 g/l) at 140oC for 1.0 to 2.5 hours using steam as heating media. Lime added are varied from 3 to 9 kg. After processing for a certain period of time, slurry product is transfered into a mixer. To evaluate percent extraction of Al2O3 from this process, the height of slurry level in the mixer, densities of the slurry, filtrat, and solid residue are measured and determined. The head sample of bauxite, filtrate and residue are analysed by using wet method to obtain Al2O3 content of each sample taken from the mixer. There are four equations that are used for obtaining the alumina extraction, namely : Vsl=4.176x+15.83 Wsl=(4.176x+15.83)ρsl S=(ρsl - ρl)/ (ρs - ρl) (ρs/ ρsl)*100% E=[10 (4.176x+15.83) [1- (ρsl - ρl)/ (ρs - ρl)]*[cl/FxF]% The calculation results show that by increasing lime added into the slurry, percent yield of alumina extraction tend to decrease from 46.63% for 3 kg of lime to 15.84% by using 9 kg of lime. Whereas by varying reaction time between 1.0-2.5 hours, percent yield of alumina extraction are fluctuation in the range of 42.07-60.54%, and the highest result was obtanined for 1,5 hours of reaction time. By implementing those four equations above for evaluating the data, we do not need to weigh the slurry in the reactor.

UPGRADING OF TAYAN’S CRUDE BAUXITE USING ROTARY DRUM SCRUBBER Husaini Husaini; Stefanus Suryo Cahyono; Retno Damayanti
Indonesian Mining Journal Vol 17, No 1 (2014): INDONESIAN MINING JOURNAL Vol. 17 No. 1 FEBRUARY 2014
Publisher : Puslitbang tekMIRA

Indonesia has abundant bauxite resources at Tayan, West Kalimanatan, where the reserve is relied more than 800 million tons. There were two types of Tayan’s bauxite that have been used in the present research. One contains 34.63 % Al2O3 and 5.20 % reactive SiO2 which is known as low grade ore, while the second type contains 47.30 % Al2O3 and 5.79 % reactive SiO2 which is known as high grade ore. A Rotary Drum Scrubber (diameter 80 cm, length 200 cm, screen opening 2 mm) was applied to upgrade the crude bauxite ores. The research was started by crushing followed by scrubbing and screening. The scrubber is supported by water sprayer to achieve washed bauxite (+2mm of particle sizes) separated from tailing (-2mm of particle size). The researchs were conducted by varying the feed rate (300-2100 kg/hr), solid percentage (14-36%) and water flow rate (35-78 L/minute). The results show that feed rate and solid percentage have high impact to the quality of washed bauxite obtained. The higher is feed rate and solid percentage the lower is alumina content of the washed bauxite produced. An optimum condition is attained at1600 kg/hour of feeding rate, 25% solid and 8 minutes of residence time that is capable to produce washed bauxite with chemical composition of 45.25 % Al2O3 and 3.27 % reactive SiO2 (when the crude bauxite as the feed is low grade type). On the other hand, the washed bauxite obtained with chemical composition of 55.50 % Al2O3, 0.47 % reactive SiO2 and impurities content with particle sizes <2mm is approximately 2,1% (when the crude bauxite as the feed is typically high grade). The average increase of Al2O3 content in the washed bauxite is 6.63% and the average decrease of reactive SiO2 is 2.87%. The washed bauxite produced is reliable as feed material for Bayer process.

UPGRADING OF TAYAN’S CRUDE BAUXITE USING ROTARY DRUM SCRUBBER Husaini Husaini; Stefanus Suryo Cahyono; Retno Damayanti
Indonesian Mining Journal Vol 17 No 1 (2014): INDONESIAN MINING JOURNAL Vol. 17 No. 1 FEBRUARY 2014
Publisher : Balai Besar Pengujian Mineral dan Batubara tekMIRA

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.30556/imj.Vol17.No1.2014.343

Indonesia has abundant bauxite resources at Tayan, West Kalimanatan, where the reserve is relied more than 800 million tons. There were two types of Tayan’s bauxite that have been used in the present research. One contains 34.63 % Al2O3 and 5.20 % reactive SiO2 which is known as low grade ore, while the second type contains 47.30 % Al2O3 and 5.79 % reactive SiO2 which is known as high grade ore. A Rotary Drum Scrubber (diameter 80 cm, length 200 cm, screen opening 2 mm) was applied to upgrade the crude bauxite ores. The research was started by crushing followed by scrubbing and screening. The scrubber is supported by water sprayer to achieve washed bauxite (+2mm of particle sizes) separated from tailing (-2mm of particle size). The researchs were conducted by varying the feed rate (300-2100 kg/hr), solid percentage (14-36%) and water flow rate (35-78 L/minute). The results show that feed rate and solid percentage have high impact to the quality of washed bauxite obtained. The higher is feed rate and solid percentage the lower is alumina content of the washed bauxite produced. An optimum condition is attained at1600 kg/hour of feeding rate, 25% solid and 8 minutes of residence time that is capable to produce washed bauxite with chemical composition of 45.25 % Al2O3 and 3.27 % reactive SiO2 (when the crude bauxite as the feed is low grade type). On the other hand, the washed bauxite obtained with chemical composition of 55.50 % Al2O3, 0.47 % reactive SiO2 and impurities content with particle sizes <2mm is approximately 2,1% (when the crude bauxite as the feed is typically high grade). The average increase of Al2O3 content in the washed bauxite is 6.63% and the average decrease of reactive SiO2 is 2.87%. The washed bauxite produced is reliable as feed material for Bayer process.

IMPLEMENTATION OF MATHEMATICAL EQUATION FOR CALCULATING ALUMINA EXTRACTION FROM BAUXITE TAILING DIGESTION Husaini Husaini
Indonesian Mining Journal Vol 19 No 1 (2016): INDONESIAN MINING JOURNAL Vol. 19 No. 1 February 2016
Publisher : Balai Besar Pengujian Mineral dan Batubara tekMIRA

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.30556/imj.Vol19.No1.2016.363

Research on bauxite tailing digestion using pressurized batch reactor at a feed capacity of 86.66 kg had been conducted. Bauxite with -150 mesh of particle size is reacted with 42.15 kg of caustic soda (433.49 g/l) at 140oC for 1.0 to 2.5 hours using steam as heating media. Lime added are varied from 3 to 9 kg. After processing for a certain period of time, slurry product is transfered into a mixer. To evaluate percent extraction of Al2O3 from this process, the height of slurry level in the mixer, densities of the slurry, filtrat, and solid residue are measured and determined. The head sample of bauxite, filtrate and residue are analysed by using wet method to obtain Al2O3 content of each sample taken from the mixer. There are four equations that are used for obtaining the alumina extraction, namely : Vsl=4.176x+15.83 Wsl=(4.176x+15.83)ρsl S=(ρsl - ρl)/ (ρs - ρl) (ρs/ ρsl)*100% E=[10 (4.176x+15.83) [1- (ρsl - ρl)/ (ρs - ρl)]*[cl/FxF]% The calculation results show that by increasing lime added into the slurry, percent yield of alumina extraction tend to decrease from 46.63% for 3 kg of lime to 15.84% by using 9 kg of lime. Whereas by varying reaction time between 1.0-2.5 hours, percent yield of alumina extraction are fluctuation in the range of 42.07-60.54%, and the highest result was obtanined for 1,5 hours of reaction time. By implementing those four equations above for evaluating the data, we do not need to weigh the slurry in the reactor.

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