An anionic-cationic flotation of two Egyptian feldspar samples, representing Road Ashaab locality of the Eastern Desert of Egypt, was investigated on both laboratory and pilot plant scales. The pegmatites belong to the alkali feldspar granite type, mostly microcline and orthoclase, KAL Si3O8 coarse grained rocks. Quartz, as the main gangue mineral, occurs in two forms as either free grains or as veins intercalating the feldspar crystals or, sometimes, intermingled with them. Iron, on the other hand, is found in three different forms as free magnetite embedded in the feldspar crystals, as microcrystalline crystals, or as magnetite filling cracks in the feldspar. Dissolution of magnetite to hematite is, sometimes, observed. Grinding of the feldspar samples to less than 0.25 mm followed by desliming was optimized in the laboratory, using a ball mill in closed circuit with the screen. Anionic flotation of the iron oxide impurity from the -0.25 + 0.03 mm ground product was successfully conducted using locally produced dodecyl benzene sulphonic acid—rice bran oil/kerosene promoter at pH 3. Cationic flotation of feldspar from this product was then carried out employing a locally produced quaternary ammonium salt in presence of HF acid, as a silica depressant and a feldspar activator at pH 3. Feldspar final concentrates assaying 80.8% - 89.5% feldspar mineral, 0.119% - 0.127% Fe
2O
3 and 16.84% - 18.65% Al
2O
3, were obtained at the optimum operating conditions that satisfy the requirements of the ceramic industry. Continuous 200 kg/h pilot plant runs were conducted using the appropriate equipment, based upon the laboratory findings to produce feldspar concentrates assaying 16.38% - 18.13% Al
2O
3, and 0.13% - 0.15% Fe
2O
3. Materials’ metallurgical balance and complete chemical analyses were shown.
Na-Feldspar K-Feldspar Flotation Sand Separation Effect of pH1. Introduction
Feldspars are indispensable raw materials for many industries, such as ceramics, glass and fillers for plastics production. Considerable reserves of feldspar varieties are found in the Eastern Desert of Egypt, most of which are used as it is without processing.
The development of a satisfactory concentration process of feldspar depends not only upon its separation but also upon the maintenance of a proper size ratio of feldspar particles that satisfy the trade requirements [1] . The specification of size ranges from as coarse as −0.75 mm + 0.15 mm to a size as fine as −0.075 mm. Various methods of separation, such as differential grinding and sizing, gravity concentration, electrostatic separation and flotation had been developed in the past [1] - [4] . Each process had been partly successful or had failed because of unsuitability of the size range or lack of selectivity.
Recently, the ability to beneficiate feldspar has developed remarkably because flotation techniques proved its viability [2] [4] [5] . It is now possible to free feldspar from all kinds of gangue minerals, e.g. mica, quartz and heavy minerals in addition to separation of both K and Na feldspars from each other [2] - [4] . Cationic flotation of feldspar (amine + HF) in presence of NaCl was conducted by CengizDemir of Turkey in 2010 to separate both Na- and K-feldspar [3] . NaCl addition controls amine adsorption on sodium feldspar through adsorption of Na+ ions onto the mineral surface [3] . The use of NaCl addition in flotation was found to increase the K-feldspar grade in the concentrate.
The flotation behavior of feldspars is essentially determined by their surface condition and thus by the extent of hydrolytic decomposition of feldspar surfaces [6] . The cationic-type collectors, which are most satisfactory for acidic minerals, were used in the flotation of feldspars in the thirties. In 1982, it was found that C6-14 primary amine hydrochloride collectors were used for the flotation of feldspars in presence of HF or a mixture of HF and NaCl. The C10-12 amine gave the best flotation results [7] [8] . The feldspar was activated whereas the quartz was depressed by conditioning with HF. A comprehensive review on flotation of mica, iron oxides, ilmenite and other gangue minerals from feldspar was discussed by Heyes et al. in 2012 [9] .
However, a HF-free flotation process using a mixture of the cationic and anionic collectors for the separation of feldspar from sand was described by Katayanagi [4] and the process was reported to be applied in industrial practice [2] [4] . In an aqueous medium the feldspar surface shows, after a short time, changes which have a negative effect on floatability. Therefore, the residence times during reagent conditioning and during flotation too should be as short as possible [7] [10] . Referring to the fact that in HF-containing pulps, a considerable amount of the Fe ions of the mineral surface dissolves and then forms bond with F ions, so iron-rich minerals should be eliminated as much as possible prior to flotation [11] [12] .
In this respect, the present investigation is a “step-on-the-road” for better quality Egyptian feldspars.
The feldspar samples were crushed in a “Denver” pilot jaw crusher followed by a “Wedag” roller in closed circuit with 3.5 mm screen. The −3.5 mm crushed products were mixed thoroughly, then quartered by a “Jones” sampler to about 3 kg batches. One of these batches was finely ground to 100% less than 74 μm for complete chemical analysis. On the other hand, mineralogical examination of the samples was carried out on hand-picked thin and polished sections.
The flotation feed samples were prepared by grinding the secondary crushed ores to 100% less than 0.25 mm in a rod mill in closed circuit with the screen, under the predetermined optimum conditions. The ground products were then screened on 0.1 mm sieve and the undersize products were deslimed using a “Mozley” portable 3” hydrocyclone to remove the −30 μm slimes at a feed pressure of 20 psi and 15% pulp density. The cyclone underflow products were thoroughly mixed with the −0.25 + 0.1 mm size fraction. The dried products were sampled to 300 g batches for the flotation tests. In this respect, a “Denver D 12” flotation cell was used which is a simulation of the sub-aeration type.
2.2. Reverse Anionic Flotation of Iron Oxides Contaminants
Dodecyl benzene sulphonic acid was used as a collector without or with the addition of rice bran oil as a foam regulator. This is an Egyptian by-product of the rice industry which proved its viability for such purpose. The former was added as a 10% solution and the latter was diluted with kerosene in 1:1 mixture by volume. Factors affecting the process were verified under pH 3 using H2SO4. These included the collector dose, the effect of adding rice bran oil, pulp pH, and the effect of using coarser size flotation feed.
2.3. Direct Cationic Flotation of Feldspar
Locally produced quaternary ammonium salt was used to separate the silica impurities from the previously obtained flotation concentrate. Hydrofluoric acid was added in this circuit as a silica depressant and a feldspar activator as well. Optimization of the process was carried out under the following operating parameters: pH 3, dose of dodecyl benzene sulphonic acid/rice bran oil/kerosene blend of 1.5:0.75:0.75 kg/t.
2.4. Pilot Plant Production of Feldspar Concentrates
Figure 1 depicts the beneficiation flowsheet and layout of equipment. In the first part of the circuit, the −3.5 crushed ore was wet ground to −0.25 mm in a 24 × 16" “Denver” rod mill in a closed circuit with a 9” spiral classifier. A pulp density of 50% solid and a residence time of 12 min. were always maintained in the mill, Figure 1. The classifier overflow product, O.F., was delivered to another spiral classifier for removal of the −0.03 mm slimes whereas the −0.25 + 0.03 mm underflow, U.F., product was directed towards the conditioning tank.
The anionic collector, dodecyl benzene sulphonic acid/rice bran oil in kerosene mixture (1.5:0.75:0.75 kg/t) was added to the tank with close control of the pH at 2.5 - 3 and the pulp density at about 50% solid, and conditioning time 3 min. The conditioned pulp was then directed to a 6-flotation cell bank where roughing and cleaning processes were carried out in the first four units only. The iron oxides froth was sent to dump whereas the sink (feldspar) was pumped to “Denver” attrition scrubber for surface cleaning. De-oiling of the product was then performed in a “Denver” hydrosizer, the O.F. of which was dumped whereas the thickened feldspar pulp was delivered to another conditioning tank for addition of HF acid (0.3 kg/t) as a free silica depressant at pH 2.5 - 3. The conditioned pulp was then delivered to the last two flotation cell units, for direct flotation of feldspar after the addition of the amine cationic collector at a rate of 0.3 kg/t in the rougher cell. The cleaner feldspar concentrate was then collected as the final product from the last flotation cell whereas the depressed free silica was sent to dump.
Continuous pilot plant runs were carried out with both feldspar samples at a feed rate of 200 kg/h with close control of all parameters. Samples were collected periodically from feed and all outlets for metallurgical balance calculations.
The Feldspar beneficiation flow-sheet and equipment layout
3. Results and Discussion3.1. Characterization of the Feldspar Samples
Complete chemical analyses of the feldspar samples, shown in Table 1, indicate that they belong to the alkali-feldspar granite type, highly siliceous, rich in Al2O3 and K2O, but poor in Fe2O3 and MgO.
Mineralogically the pegmatites are coarse grained rocks, crystals may reach one centimeter to decimeter in size. The most abundant feldspar minerals are microcline, KAlSi3O8. It occurs in large crystals showing cross hatching lamellar twinning, Plate 1(a) . Orthoclase is the second feldspar mineral, KAlS3O8 that was identified with its twinned forms, e.g. carlsbad, baveno and manebach, Plate 1(b) . Both minerals are found associated with each other, Plate 1(b) . Quartz occurs in two forms: as free grains, Plate 1(c) and as veins intercalating the feldspar crystals, or sometimes, intermingled with them, Plate 1(d) . Iron, on the other hand, is found in three different forms; in free magnetite crystals embedded in the feldspar as microcrystalline crystals, Plate 1(e) or filling cracks in the feldspar, Plate 1(f) . The size of the different mineral species varies between 1 mm to 3 mm. The pegmatitic rocks form, sometimes, perthitic plates with quartz, a property that may help rock pulverization
and facilitates the degree of minerals liberation.
3.2. Optimization of the Differential Flotation Process
Fine grinding of the pulverized feldspar samples to 100% less than 0.25 mm in the rod mill accompanied with proper desliming was a perquisite to flotation. Results show that only 6.26% by weight of the ground product was lost in the −0.03 mm slimes but it was overloaded with iron oxide reaching about 2%. The accumulation of this iron oxide in the O.F. of the cyclone may be due to the surface coating of the feldspar grains with a ferruginous clayey matrix which was disintegrated by the feed pressure of the hydrocyclone.
3.2.1. Anionic Flotation of Iron Oxides
Results illustrated in Figure 2 show a successive decrease in the % Fe2O3 of the feldspar pre-concentrate from 0.39% to 0.18% by using 9 kg/t of dodecyl benzene sulphonic acid collector. By stepwise addition of the collector in 2 kg/t each, this could be cut down to 7 kg/t only. Nevertheless, this is a rather high consumption of a reagent, in addition to its questionable highly stable form in the flotation cell (specially tailored for the detergency industry.
By addition of rice bran oil as a foam regulator, results shown in Table 2 indicate that in addition to that, a drastic drop in the collector consumption to 1.5 kg/t was achieved by blending with the rice bran oil/kerosene mixture of 0.75 kg/t each. A better quality concentrate was obtained having 0.18% Fe2O3 with a feldspar recovery of 73%. Therefore the dodecyl benzene sulphonic acid/rice bran oil in kerosene blend of 2:1:1 (1.5:0.75:0.75 kg/t) was chosen as the optimum.
The effect of changing pulp pH on the concentrate quality under the predetermined optimum conditions is illustrated in Figure 3. Evidently the best pH is around 3. At pH 4, the grade of the concentrate deteriorates, despite the loss in its weight due to flotation of the feldspar itself by increase in pH.
Although the grain size requirement of feldspar employed in the ceramic industry is 98% by weight less than 74 mm, yet relatively coarser size limits are compelled in the glass industry (up to 0.42 mm). Table 3 shows that by using the −0.417 + 0.02 mm relatively coarse size in feldspar flotation a relative increase in the yield of concentrate from 73% to 79.4% occurs, but this happens on the prejudice of product grade. The Fe2O3 content is
Complete chemical analysis of feldspar samples
Constituent
Sample I %
Sample II %
Total SiO2
72.37
73.50
Al2O3
11.97
12.50
Fe2O3
0.53
0.22
Na2O
2.28
2.13
K2O
8.38
9.30
MgO
0.25
0.23
Effect of dodecyl benzene sulphonicacid dose
Effect of flotation pH on the concentrate quality of the anionic circuit
doubled in this latter case (from 0.12% to 0.242%).
3.2.2. The Cationic Flotation of Feldspar
When the feldspar pre-concentrate obtained under the predetermined optimum conditions was subjected to a differential cationic flotation process using the locally produced amine (0.25 kg/t) in presence of HF acid (1.3 kg/t), the optimum pH was found between 2.5 and 3, Table 4. A concentrate assaying 75.86% feldspar, 15.3% Al2O3 and 0.12% Fe2O3 was obtained with a total % SiO2 of 65.91.
By increasing the dose of the cationic collector under the optimum pH and in presence of HF acid, a relative improvement in the concentrate grade and recovery occurs at 0.291 kg/t of the amine, Table 5. Under such conditions, increasing the HF acid consumption successively leads to a pronounced increase in the concentrate grade in terms of both feldspar and Al2O3 content, Table 6. At a maximum dose of 5.20 kg/t of HF acid, a concentrate assaying 18.65% Al2O3, 0.119% Fe2O3 and 65.3% total SiO2 (89.52% feldspar), Table 6. Complete chemical analysis of the two feldspar samples at optimum flotation conditions are illustrated in Table 7.
Effect of mixing the collector with rice bran oil
Dose, kg/ton
Conc. Wt%
Fe2O3%
Feldspar Rec. %
Sulphonic acid
Rice Bran Oil
Kerosene
3.00
0.00
0.0
80.48
0.262
59.45
3.00
0.25
0.25
77.95
0.240
60.02
3.00
0.5
0.5
70.89
0.166
77.37
3.00
0.75
0.75
65.54
0.170
78.57
1.50
0.75
0.75
72.98
0.120
83.16
3.00
--
1.5
No Froth
Effect of using coarser size fraction feed
Flotation Feed Size, mm
Fe2O3%
Yield %
−0.25 + 0.020
0.120
72.98
−0.417 + 0.02
0.242
79.44
The effect of pH on the cationic flotation process
pH
Total SiO2 %
Al2O3%
Fe2O3%
Feldspar %
2.0
67.62
13.80
0.140
66.24
2.0 - 3.0
65.91
15.30
0.120
75.86
4.0 - 4.5
68.46
12.80
0.145
61.44
Effect of cationic collector dose on the improvement of the flotation process
Dose, Kg/t
Total SiO2%
Al2O3%
Fe2O3%
Feldspar %
0.250
65.91
15.30
0.120
75.86
0.291
65.63
15.92
0.118
76.42
0.332
69.16
15.50
0.123
74.42
0.400
67.08
15.45
0.123
74.14
Effect of HF dose on the Improvement of the flotation process
HF Dose, kg/t
Wt., %
Total SiO2%
Al2O3%
Fe2O3%
Feldspar %
1.30
91.87
65.63
15.92
0.118
76.42
2.60
75.46
68.79
17.83
0.120
85.58
5.20
64.89
65.30
18.65
0.119
89.52
3.3. Pilot Plant Operations and Materials Metallurgical Balance Calculations
Complete chemical analyses of the pilot plant feldspar concentrates of both samples is shown in Table 8 and the metallurgical balance of the whole operations is depicted in Table 9. Concentrates having 78.62% and 87.02% feldspar minerals were obtained with Road Ashaab feldspar samples, 1 and 2 respectively at an overall recovery of 80.74% and 92.8%. Both products satisfy the international specifications for ceramics industries. They are rich in potash, moderate in alumina and have a minimum content of iron oxide and free silica impurities.
4. Conclusions
The amenability of two feldspar samples to a differential flotation process including both anionic and cationic
Complete chemical analysis of final feldspar samples concentrates
Sample Constituents, %
Sample No.1
Sample No. II
Total SiO2
65.30
67.86
Al2O3
18.65
16.84
Fe2O3
0.119
0.127
CaO
2.00
1.50
MgO
0.25
0.20
Na2O
2.30
2.20
K2O
10.97
10.92
L.O.I.
0.23
0.30
Complete chemical analysis of pilot plant final feldspar samples concentrates
Sample Constituents, %
Sample No. 1
Sample No. II
Total SiO2
67.95
66.41
Al2O3
16.38
18.13
Fe2O3
0.13
0.15
CaO
1.57
2.03
MgO
0.20
0.26
Na2O
2.09
2.30
K2O
10.91
10.71
L.O.I.
0.29
0.30
Feldspar Mineral
78.62
87.02
Metallurgical balance of pilot plant beneficiation operations of feldspar samples
Pilot Plant Product
Sample I
Sample II
Flow Rate, Kg/h
Wt%
Fe2O3%
Flow Rate, Kg/h
Wt%
Fe2O3%
Feed
200.00
100.00
0.225
200.00
100.00
0.53
Spiral Classifier O.F
23.00
11.50
11.00
10.50
Hydro-classifier O.F.
8.00
4.50
5.00
2.50
Tailings (Anionic & cationic Flotation Process)
51.00
25.50
23.00
Final Concentrate
118.00
59.00
0.130
128.00
64.00
0.143
circuits was investigated on laboratory and pilot plant scales. The ores are pegmatites belonging to the alkali feldspar granite type, mostly microcline and orthoclase coarse-grained rocks. Quartz, as the main gangue mineral, occurs in either free grains or as veins intercalating the feldspar crystals or intermingled with them. Iron, as the other impurity, is found in different forms as free magnetite embedded in the feldspar crystals as microcrystalline crystals or as magnetite filling cracks in the feldspar.
The secondary crushed ores were wet ground to −0.25 mm in a ball mill in closed circuit with the screen, then deslimed to reject the slimes less than 0.03 mm before subjected to flotation. This was carried out through a reverse anionic circuit followed by a direct cationic one. A locally produced dodecyl benzene sulphonic acid was employed as an iron oxide collector at pH 3 in the former process. A small dose of rice bran oil (0.75 kg/t) in kerosene that was added to the collector as a foam conditioner resulted in a remarkable decrease in its consumption from 7.0 kg/t to 1.5 kg/t. Cationic flotation of feldspar from this pre-concentrate was then carried out using a locally produced amine at pH 2.5 - 3.0 in presence of HF as a free silica depressant and a feldspar activator. Final feldspar concentrates assaying 80.8% to 89.5% feldspar mineral, 0.119% - 0.127% Fe2O3 and 16.84% - 18.65% Al2O3 that satisfy the requirements of the International Ceramic Society.
A metallurgical balance of the whole operations and complete chemical analyses of products were shown.
Cite this paper
Tawfik RefaatBoulos,Suzan SamiIbrahim,AhmedYehia, (2015) Differential Flotation of Some Egyptian Feldspars for Separation of Both Silica and Iron Oxides Contaminants. Journal of Minerals and Materials Characterization and Engineering,03,435-443. doi: 10.4236/jmmce.2015.36046
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