Process for beneficiating sulfide ores
AssigneeHazen Research, Inc.
InventorsJames K. Kindig, Ronald L. Turner
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AssigneeHazen Research, Inc.
InventorsJames K. Kindig, Ronald L. Turner
Estimating the term…
In a process for beneficiating one or more mineral values of sulfide ores by treating the sulfide ore with a metal containing compound under conditions such as to selectively enhance the magnetic susceptibility of the mineral values to the exclusion of the gangue in order to permit a separation between the values and gangue, the improvement comprising pretreating the sulfide ore by heating it to a temperature of at least about 80.degree. C. for at least about 0.1 hours.
In a process for the beneficiation of a sulfide ore from gangue, excluding coal, wherein the ore is treated with a metal containing compound under conditions which cause the metal containing compound to react substantially at the surface of the metal sulfide particles to the substantial exclusion of the gangue particles so as to alter the surface characteristics of the metal sulfide values thereby causing a selective enhancement of the magnetic susceptibility of one or more metal sulfide values of the ore to the exclusion of the gangue in order to permit a physical separation between the metal sulfide values and the gangue, the improvement comprising:
In a process for the beneficiation of a metal sulfide ore from gangue, excluding coal, wherein the ore is treated with from about 0.1 to about 100 kilograms of metal containing compound per metric ton of ore at a temperature within a range of 125.degree. C. less than the general decomposition temperature of the metal containing compound in a specific system for the ore being treated for a period of time of from about 0.05 to about 4 hours to cause the metal containing compound to react substantially at the surface of the metal sulfide particles to the substantial exclusion of the gangue particles so as to alter the surface characteristics of the metal sulfide values thereby causing a selective enhancement of the magnetic susceptibility of one or more metal sulfide values contained in the ore to the exclusion of the gangue in order to permit a physical separation, the improvement comprising:
In a process for the beneficiation of a metal sulfide ore from gangue, excluding coal, wherein the metal sulfide ore is selected from a group consisting of galena, molybdenite, sphalerite, bornite, cinnabar, arsenopyrite, smaltite, chalcopyrite, orpiment, realgar, pentlandite, stibnite, and tetrahedrite and wherein the ore is treated with from about 2 to about 20 kilograms of an iron containing compound per metric ton of ore at a temperature within a range of 125.degree. C. less than the general decomposition temperature of the iron containing compound in a specific system for the ore being treated to cause the iron containing compound to react substantially at the surface of the metal sulfide particles to the substantial exclusion of the gangue particles so as to alter the surface characteristics of the metal sulfide values thereby causing a selective enhancement of the magnetic susceptibility of one or more metal sulfide values contained in the ore to the exclusion of the gangue in order to permit their magnetic separation, the improvement for the ore in a specific system comprising:
In a process for the beneficiation of a sulfide ore from gangue, excluding coal, wherein the ore is treated with an iron carbonyl compound under conditions which cause the iron carbonyl compound to react substantially at the surface of the metal sulfide particles to the substantial exclusion of the gangue particles so as to alter the surface characteristics of the metal sulfide values thereby causing a selective enhancement of the magnetic susceptibility of one or more metal sulfide values of the ore to the exclusion of the gangue in order to permit a separation between the metal sulfide values and the gangue, the improvement comprising:
Dependencies are inferred from the claim text.
This invention relates to a means for treating sulfide ores to separate the mineral value(s) from gangue material by selectively enhancing the magnetic susceptibility of the mineral value(s) so that they may be separated from the gangue.
As is well-known, mining operations in the past for recovering various metals, e.g., lead, copper, have utilized high grade ore deposits where possible. Many of these deposits have been exhausted and mining of lower grade ores is increasing. The processing of these leaner ores consumes large amounts of time, labor, reagents, power and water with conventional processing.
In addition to the increased expense associated with the extraction of these metals from low grade ores, proposed processes for separation of certain of the sulfide ores are technically very difficult and involve elaborate and expensive equipment. In many cases the expense incurred by such separation would be greater than the commercial value of the metal, such that the mineral recovery, while theoretically possible, is economically unfeasible.
Samples of different minerals were ground to a minus 65 mesh and mixed with minus 65 mesh silica sand to produce 3 percent synthetic ores with the exception of molybdenite which was a 5 percent ore. A sample of each ore was pretreated with steam by rapidly heating a reactor containing the sample to 200.degree. C. under a nitrogen purge; thereafter the sample was treated for 15 minutes with 200 kilograms of steam per metric ton of sample. The reactor was then cooled under a nitrogen purge. Following this pretreatment, each sample was treated with 8 kilograms of iron pentacarbonyl per metric ton of sample for 30 minutes at the temperature indicated in Table 1. For comparative purposes, a sample of each of these ores was only pretreated with the steam in the manner indicated above. All of the samples were then subjected to a wet magnetic separation process, and the analyses of the products thus obtained are presented below in Table 1.
TABLE 1 __________________________________________________________________________ Temp. of Fe(CO).sub.5 Treatment Weight Grade Metal Mineral Pretreatment (.degree.C.) Product (%) (%) Metal Distr. __________________________________________________________________________ Galena Steam 135 Magnetic 3.9 52.7 Pb 86.6 Nonmagnetic 96.1 0.33 Pb 13.4 Calculated Feed 100.0 2.37 Pb 100.0 Galena Steam blank -- Magnetic 0.48 17.2 Pb 3.3 Nonmagnetic 99.52 2.42 Pb 96.7 Calculated Feed 100.0 2.49 Pb 100.0 Molybdenite Steam 135 Magnetic 36.4 0.45 Mo 89.0 Nonmagnetic 63.6 0.032 Mo 11.0 Calculated Feed 100.0 0.18 Mo 100.0 Molybdenite Steam blank -- Magnetic 0.48 2.73 Mo 7.8 Nonmagnetic 99.52 0.156 Mo 92.2 Calculated Feed 100.0 0.168 Mo 100.0 Stibnite Steam 85 Magnetic 1.2 24.1 Sb 44.4 Nonmagnetic 98.8 0.367 Sb 55.6 Calculated Feed 100.0 0.652 Sb 100.0 Stibnite Steam Blank -- Magnetic 0.64 4.50 Sb 3.3 Nonmagnetic 99.36 0.847 Sb 96.7 Calculated Feed 100.0 0.87 Sb 100.0 Smaltite Steam 115 Magnetic 0.72 4.96 Co 11.6 Nonmagnetic 99.28 0.275 Co 88.4 Calculated Feed 100.0 0.309 Co 100.0 Smaltite Steam blank -- Magnetic 0.84 2.40 Co 6.6 Nonmagnetic 99.16 0.29 Co 93.4 Calculated Feed 100.0 0.31 Co 100.0 Chalcopyrite Steam 140 Magnetic 4.4 17.1 Cu 81.4 Nonmagnetic 95.6 0.18 Cu 18.6 Calculated Feed 100.0 0.924 Cu 100.0 Chalcopyrite Steam blank -- Magnetic 2.3 26.3 Cu 69.6 Nonmagnetic 97.7 0.271 Cu 30.4 Calculated Feed 100.0 0.87 Cu 100.0 Orpiment Steam 110 Magnetic 12.6 9.06 As 85.8 Nonmagnetic 87.4 [0.22]* As 14.2 Calculated Feed 100.0 1.33 As 100.0 Orpiment Steam blank -- Magnetic 0.61 10.8 As 5.0 Nonmagnetic 99.39 1.27 As 95.0 Calculated Feed 100.0 1.33 As 100.0 Cinnabar Steam 190 Magnetic 3.0 23.9 Hg 54.8 Nonmagnetic 97.0 0.61 Hg 45.2 Calculated Feed 100.0 1.31 Hg 100.0 Cinnabar Steam blank -- Magnetic 0.72 14.9 Hg 7.0 Nonmagnetic 99.28 1.43 Hg 93.0 Calculated Feed 100.0 1.53 Hg 100.0 Bornite Steam 140 Magnetic 15.1 8.95 Cu 89.9 Nonmagnetic 84.9 0.178 Cu 10.1 Calculated Feed 100.0 1.50 Cu 100.0 Bornite Steam blank -- Magnetic 2.4 49.5 Cu 80.0 Nonmagnetic 97.6 0.304 Cu 20.0 Calculated Feed 100.0 1.49 Cu 100.0 Realgar Steam 95 Magnetic 33.3 3.88 As 89.0 Nonmagnetic 67.7 0.24 As 11.0 Calculated Feed 100.0 1.45 As 100.0 Realgar Steam blank -- Magnetic 0.53 2.25 As 0.8 Nonmagnetic 99.47 1.56 As 99.2 Calculated Feed 100.0 1.56 As 100.0 Pentlandite Steam 105 Magnetic 2.6 7.65 Ni 91.1 Nonmagnetic 97.4 0.02 Ni 8.9 Calculated Feed 100.0 0.22 Ni 100.0 Pentlandite Steam blank -- Magnetic 3.0 7.93 Ni 49.5 Nonmagnetic 97.0 0.25 Ni 50.5 Calculated Feed 100.0 0.48 Ni 100.0 Tetrahedrite Steam 117 Magnetic 2.5 4.65 Cu 70.5 Nonmagnetic 97.5 0.05 Cu 29.5 Calculated Feed 100.0 0.165 Cu 100.0 Tetrahedrite Steam blank -- Magnetic 2.9 5.18 Cu 83.8 Nonmagnetic 97.1 0.03 Cu 16.2 Calculated Feed 100.0 0.179 Cu 100.0 __________________________________________________________________________ *Values in brackets are calculated from other analyses.
Samples of different synthetic ores were prepared as indicated in Example 1. A sample of each of the ores was pretreated with heat and nitrogen by rapidly heating a reactor containing the sample to 400.degree. C. during a nitrogen purge which flowed at a rate of one reactor volume of gas being introduced into the system every 4.3 minutes and maintaining these conditions for 15 minutes. Then the reactor was cooled under the same type of nitrogen purge. Following this pretreatment each sample was treated with 8 kilograms of iron pentacarbonyl per metric ton of sample for 30 minutes at the temperature indicated for the particular ore in Table 1. For comparative purposes, a sample of each of the ores was merely subjected to the heat and nitrogen pretreatment in the manner indicated above. All of the samples were then subjected to a magnetic separation process. The results are presented in Table 2
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By liquid-liquid extraction using organic compounds: ethers or epoxides
Pretreatment specially adapted for magnetic separation: by chemical treatment imparting magnetic properties to the material to be separated, e.g.…
Preliminary treatment of ores or scrap
Preliminary treatment of ores or scrap: roasting processes
Term ended 10 Oct 1998 (estimated)
USPTO file history isn’t available for this patent, so only indexed dates are shown.