>*x X .. « *. ▼Jh 0* ,-»,£. *c 3*« %> <$> »J > aV **^ • ^•> x^x y,^-> ,/\-^.\, >*.*&•> **.•&&,: r v * **0« *•"••* .*o ^°^ . ^0* * ^.*^te\ /&% ^••^Bfe-X ^° v #<&:•/*+ SsJite.%. y.:^:..^ .^ A%\ y,:i a»9 fe - X/^tot-X y$fe-\ **••&•% c sjg^*\ / - - *"». .V ^- ' * A •X^ ,* .-. Sr&J x'tt's V^ , > 1 ' V*^V \-! °o BUREAU OF MINES INFORMATION CIRCULAR/1989 Study of Zeta Potential for Material Particles in Chemical Additive Solutions By Pamela J. Watson and Patrick A. Tuzinski UNITED STATES DEPARTMENT OF THE INTERIOR Mission: As the Nation's principal conservation agency, the Department of the Interior has respon- sibility for most of our nationally-owned public lands and natural and cultural resources. This includes fostering wise use of our land and water resources, protecting our fish and wildlife, pre- serving the environmental and cultural values of our national parks and historical places, and pro- viding for the enjoyment of life through outdoor recreation. The Department assesses our energy and mineral resources and works to assure that their development is in the best interests of all our people. The Department also promotes the goals of the Take Pride in America campaign by encouraging stewardship and citizen responsibil- ity for the public lands and promoting citizen par- ticipation in their care. The Department also has a major responsibility for American Indian reser- vation communities and for people who live in Island Territories under U.S. Administration. Information Circular 9229 Study of Zeta Potential for Material Particles in Chemical Additive Solutions By Pamela J. Watson and Patrick A. Tuzinski UNITED STATES DEPARTMENT OF THE INTERIOR Manuel Lujan, Jr., Secretary BUREAU OF MINES T S Ary, Director Results and discussion 7 Effect of water quality on PZC concentration 9 Effect of material composition on PZC concentration 9 Effect of inorganic salt cation valence on PZC concentration 9 Effect of anionic and nonionic additives on zeta potential 10 Effect of anionic plus nonionic combinations on zeta potential 10 Effect of excess cationic additive on zeta potential 10 Conclusions 11 References 11 Appendix 12 ILLUSTRATIONS 1. Stern layer schematic 3 2. Example of graphical analysis 5 3. Example of anionic additive results 6 4. Example of nonionic additive results 6 5. Example of A1C1 3 high concentration test 10 TABLES 1. Average zeta potential values for Sioux Quartzite with A1C1 3 in DDrW test series 4 2. PZC concentrations as determined from graphical analysis for Sioux Quartzite with A1C1 3 in DDIW .... 5 3. Values used in graph of Sioux Quartzite tests using anionic and nonionic additives 5 4. Materials tested 7 5. Additives tested 8 6. Baseline waters 8 A-l. Summary of zeta potential tests performed, by material type 12 A-2. Summary of zeta potential tests performed, by additive 15 A-3. Chemical analyses of waters used 17 A-4. Oxide content of raw materials 18 A-5. Chemical analyses of coal, diamond, and cobalt powder 19 A-6. Summary of PZC zeta potential results for cationic and anionic additives, by material type 19 A-7. Summary of PZC zeta potential results for cationic and anionic additives, by additive 22 A-8. PZC zeta potential results for A1C1 3 when using pH modification 24 A-9. Zeta potential test results for nonionic and anionic additives with Sioux Quartzite, and anionic additives with Mahogany granite 25 A-10. Zeta potential test results for nonionic PEO 27 A-ll. Summary of zeta potential test results using combinations of anionic additives with nonionic PEO 32 A- 12. Average zeta potential values for Sioux Quartzite with A1C1 3 in DDIW at higher than normal concentrations 34 UNIT OF MEASURE ABBREVIATIONS USED IN THIS REPORT °C degree Celsius mol/L mole per liter g gram ppm part per million /iS/cm microsiemens per centimeter pet percent mL milliliter V/cm volt per centimeter mV millivolt STUDY OF ZETA POTENTIAL FOR MATERIAL PARTICLES IN CHEMICAL ADDITIVE SOLUTIONS 1 * By Pamela J. Watson and Patrick A. Tuzinski' ABSTRACT A novel technique has been employed by the U.S. Bureau of Mines to determine the zeta potential of particles for a far-reaching series of material types in a wide variety of baseline waters, both alone and with many different chemical additives. The materials tested ranged from naturally occurring Sioux Quartzite and Tennessee marble to commercially produced magnesium oxide bricks. The waters tested ranged from ultrapure distilled, deionized water to municipal tap water and mine-site water. The chemical solutions tested included inorganic additives, such as aluminum chloride (AlCl 3 ) and sodium chloride (NaCl); organic additives, such as dodecyltrimethyl ammonium bromide (DTAB); and nonionic polymers, such as polyethylene oxide (PEO). The results of precise zeta potential determinations have application in a large number of laboratory studies as well as in various mining and processing operations. fining engineer. 2 Research geochemist. Twin Cities Research Center, U.S. Bureau of Mines, Minneapolis, MN. INTRODUCTION There are many areas of research and manufacturing that make use of either zero zeta potential or some other zeta potential value to control desired product properties. A knowledge of a system's unique zeta potential charac- teristics is therefore required to successfully perform many research or manufacturing tasks. Manufacturing and pro- duction applications for zeta potential range from pro- cessing techniques for such diverse items as paints and detergents (i) 3 to selective mineral flotation by cation or anion control (2-3). Optimum flocculation of turbidity- producing particles by zeta potential control is a critical aspect of municipal water treatment and purification sys- tems (4). Some research areas related to zeta potential include studies of hardness and dislocation mobilities of rocks and other materials (5), understanding the nature of rock weathering (6), characterizing differences between minerals of similar chemical composition (6), studies of rock penetration by diamond indenters (7), and the use of chemical additives in drilling fluids (8-9). With respect to chemical additives in drilling fluids, the Bureau found that optimized drilling performance could be obtained under zero zeta potential conditions (10). This zeta potential controlled drilling requires precise knowl- edge about the point of zero charge (PZC) concentration for a given fluid additive in relation to the rock being drilled. Because of the critical nature of this process, it was necessary to develop a way to accurately predict the PZC concentration for a given material-additive system. These results have also demonstrated that testing the zeta potential of ground particles does indeed represent the whole material zeta potential (10). At the PZC concen- tration demonstrated by the material particle tests, the performance of the drilling tests was maximized, as postulated by many researchers (5-10). The Stern model of the electrical double layer of ions can be employed to explain the electrical equilibrium state set up around a solid in a liquid phase. In that model, the solid has a rigidly fixed electrical charge and the innermost layer of ions, called the Stern layer, is a practically immo- bile layer of oppositely charged ions in the liquid phase that are absorbed on the solid. Farther away from the solid, next to the Stern layer, is the mobile diffuse layer of ions, which is composed of mobile positively and nega- tively charged ions in the liquid phase. This layer may have a net charge of the same or opposite sign from that of the Stern layer. The electrical potential difference that develops between the solid and the bulk solution (across the Stern and diffuse layers) is called the Nernst potential. This potential is the balance between the electrostatic attraction of the solution counter ions to the solid surface and their tendency to diffuse away from the surface. The potential drop that occurs across the diffuse layer is called the zeta potential and it is that potential that is readily varied through changes in bulk solution concentrations (see figure 1). As the zeta potential drops to zero, the diffuse layer thickness approaches zero and the Nernst potential drop occurs totally within the Stern layer. Under these con- ditions, a PZC or zero surface charge (ZSC) exists on the solid surface. The zeta potential of materials in water of nearly neutral pH can be negative (usually the case) or positive (chrysotile and magnesium oxide). By adding cations or anions to the water, the magnitude of the charge on the material surface can be reduced until the zeta potential reaches zero. Continued addition of cations or anions will result in a zeta potential of increasing magnitude and opposite sign. The procedure developed by the Bureau and described herein is a unique and novel approach for zeta potential determinations. Most of the older methods used for deter- mining the zeta potential of any given material particle in a given solution rely on single tests of a unique fluid com- position. If the PZC concentration is to be known, several separate and discrete tests must be performed and the PZC concentration determined by interpolation, or worse by extrapolation. If there are any contaminants or foreign particles present during any single test, repeatable results may not be obtained in subsequent tests if the same con- taminant is not present or if other contaminants or foreign particles are present. In the technique described in this report, the zeta potentials can be determined for a com- plete range of additive concentrations with the same con- taminant levels being present at all the additive con- centrations. By adding small known increments of additive to the closed system, the PZC concentration can be pre- cisely determined in a simple calculation and subsequent graphing procedure. EXPERIMENTAL LABORATORY PROCEDURE ZETA POTENTIAL TEST EQUIPMENT The procedure for determining the zeta potential was the same regardless of the chemical additive or the water 3 Italic numbers in parentheses refer to items in the list of references preceding the appendix at the end of this report. (distilled, deionized [DDIW]; tap; or mine) used for a baseline fluid. The same commercially available elec- trophoretic mobility-type apparatus was used for all the tests. The electrophoretic apparatus operates on the basis that the surface charge of a material particle is proportional to the speed of the particle in a fluid in an electric field. The zeta potential for each fluid concentration increment was + + - + + - + - + + + - + T~T~~ ::r ^\ + + + - + ^s- + + + + - + - \ + + - y- + + + - -+ \r + - + +/- + + + - + - A + Bulk of solution Electrial potential surrounding the particle Shear plane Figure 1. -Stern layer schematic. determined by following the movement of an individual material particle across a monitor screen in an electric field of 10 V/cm, matching the speed of a grid line on the screen to the particle speed, and noting the zeta potential as displayed on the digital readout. When using calcium chloride (CaCl 2 ), magnesium sulfate (MgS0 4 ), or sodium chloride (NaCl), the required high ionic strength led to electrolysis at 10 V/cm, therefore, 5 V/cm was used, with no loss of accuracy. Zeta potential values are temperature sensitive, which the zeta reader instrument accounts for in calculating the resulting, displayed zeta potential. All of the tests were conducted at room temperature, and the zeta reader was consistently between 25° and 40° C. The temperature values were noted for each test to assure that the test was conducted within that temperature range. A plastic beaker was used as the fluid-material particle reservoir for all of the tests in order to prevent erroneous values resulting from possible adherence of ions to a glass beaker. The baseline fluid-particle mixture was kept in suspension with a magnetic stirrer. However, when a magnetic (or suspected magnetic material) was tested, a stirring propeller ("milkshake" stirrer) was employed to prevent biasing the zeta potential results to nonmagnetic particles resulting from removal of magnetic particles by attraction to the magnetic stir bar. In fact, a few materials that were not originally thought to be magnetic proved to be; and those tests were repeated using the milkshake stirrer. ZETA POTENTIAL TEST PROCEDURE In preparation for each test, the zeta reader was cleaned by flushing ultrapure distilled, deionized water (DDIW) through the system until no particles were ob- served on the monitor screen and the specific conductance read <10 yLzS/cm. After thoroughly cleaning the plastic beaker, 1,000 mL of fresh baseline water was put in it and the appropriate stirring system employed. The apparatus intake and outflow tubes were placed in the water and the stirrer was started. Next, approximately 0.2 g of minus 100-mesh crushed material particles was added to the baseline water. In the few cases (most notably Wausau quartzite) when the particles were very difficult to detect on the screen because of low optical density (semitrans- parent), 0.5 g of particles was added to make the tracking of particle movement easier. Thirty zeta potential determinations were made for material particles in the baseline water system. After this test was completed, a precise amount (0.01 to 1.0 mL) of the test additive was added to the system from a concen- trated stock solution, and again 30 zeta potential readings were made. Incremental additions of concentrated stock solution and zeta potential determinations (30) were con- tinued until the zeta potential value was positive for several concentrations or until a relatively high concentration of additive was added without attaining a positive zeta poten- tial reading, i.e., the zeta potential remained at or very near to zero or the zeta potential remained constant. For magnesium oxide (MgO) brick, the zeta potential of particles in DDIW is positive below a pH of 12.4. For those tests, the procedure was identical to that described, except that the MgO zeta potential in DDIW was initially positive and changed to negative with incremental addi- tions of an anionic additive. In tap water, however, the normally positive charge of MgO was more than neutral- ized by adsorbed anions from the tap water; the resulting initial zeta potential being negative as with most materials. Three separate tests were performed for each cationic additive. Because there was no PZC concentration to be determined, only one test was performed for the anionic and nonionic additives to indicate performance trends. ZERO SURFACE CHARGE CONCENTRATION DETERMINATION PZC concentrations were determined using the fol- lowing procedure. The 30 zeta potential determinations made in the baseline water and each additive concentration were respectively averaged. These average zeta potential values were then plotted as a function of additive con- centration. Table 1 lists the average zeta potential values for the series of tests for Sioux Quartzite with aluminum chloride (A1C1 3 ) in DDIW. These values (in millivolts) were plotted versus A1C1 3 concentration (in moles per liter). The best curve was drawn through the points of each test using a curve-fitting program, and the con- centration where the curve crossed the zero zeta potential line was taken as the PZC concentration. Figure 2 illus- trates these curves for the Sioux Quartzite-AlCl 3 -DDrW system. Table 1. -Average zeta potential values for Sioux Quartzite with AICI 3 in DDIW test series, millivolts Additive cone, 10' 7 mol/L Test 1 Test 2 Test 3 DDIW -26.00 -25.50 -25.40 1 -24.40 -20.60 -18.00 3 -14.70 -12.50 -11.60 6 -5.90 -3.90 -2.30 10 11.00 10.30 18.50 30 28.30 28.50 31.90 60 35.70 35.70 45.40 90 41.10 43.50 47.80 DDIW Distilled, deionized water. For cationic additives, PZC concentration values were determined for each of the three replicate tests and then averaged to get a single PZC concentration for each material-additive system. Table 2 lists the average zeta potential values and the average PZC concentration for the Sioux Quartzite-AlCl 3 -DDIW system. This procedure was followed for all of the cationic additive tests. 1 2 3 -26.0 -25.5 -25.4 7.4 7.2 6.5 Av -25.6 7.0 Table 2.-P2C concentrations as determined from graphical analysis for Sioux Quartzite with AICI 3 in DDIW Test Zeta potential of PZC cone, particles in DDI W, mV ^Q 7 mol/L -26.0 -25.5 -25.4 -25.6 DDIW Distilled, deionized water. PZC Point of zero charge. For anionic and nonionic additive tests, the graphing procedure was similar. The average zeta potential values for the single test were plotted versus additive concen- tration. Figure 3 is a representative graph for the results of Sioux Quartzite in the anionic surfactant, Nalco 8830, while figure 4 illustrates the results for Sioux Quartzite using the nonionic polymer, polyethylene oxide (PEO), with the values used in plotting the curves in these two figures listed in table 3. Table 3.-Values used in graph of Sioux Quartzite tests using anionic and nonionic additives Additive cone, ppm Zeta potential, mV Anionic, Nalco 8830: DDIW -29.14 1 -34.04 5 -42.98 10 -57.21 100 -59.51 190 -75.37 Nonionic, PEO: Tap water -33.01 1 -11.25 3 -1.18 7.48 .00 12.4 .00 122 .00 DDIW Distilled, deionized water. > E LU r- o 0- LU N 60 40- 20- -20 -40 1 III KEY l i l i I I l I I I I I I □ Test 1 A Test 2 o Test 3 Vy^^S^ I I I I I I I I I I I I I I I 1 I 10 ADDITIVE CONCENTRATION, 10" 7 mol/L Figure 2.-Example of graphical analysis. 100 -30 -40- > E -J -50 - < H Z LU h- o Q- -60 < I- u N -70h -80 1 1 1 1 1 1 1 1 | 1 1 1 1 1 1 1 1 1 1 1 1 1 Mil - ^V^D D '*— «*» - " "*~~*^^ D ~" 1 i i I I I III I i I I I 1 i I 1 i I i I i I I I 10 100 ADDITIVE CONCENTRATION, ppm Figure 3.-Example of anionic additive results. 1,000 10 100 ADDITIVE CONCENTRATION, ppm Figure 4. -Example of nonionic additive results. 1,000 RESULTS AND DISCUSSION The wide variety of materials, the diverse series of chemical additives, and the baseline waters used in these tests are listed in tables 4, 5, and 6, respectively. Test results and additional information is contained in the ap- pendix. Table A-l compiles the zeta potential tests per- formed for each additive categorized by material type, while table A-2 lists the same data for each material tested, categorized by chemical additive. Table A-3 is a compilation of the chemical analyses for the waters tested; table A-4 lists the oxide content of the materials tested; and table A-5 describes the special materials of coal, dia- mond, and cobalt. These tables are presented to explain the differences between the subsequent zeta potential results for the materials. The zeta potential and PZC values for cationic and anionic additives are listed by mat- erial type in table A-6 and by additive in table A-7. Table A-8 lists the pH modified zeta potential tests, table A-9 lists the cationic nonionic, and anionic results for Sioux Quartzite and the anionic results for Mahogany granite, table A- 10 lists nonionic PEO results, table A-ll lists the results when using combinations of anionic additives with PEO, and table A- 12 lists the results when using an excess of additive. In comparing the results of these tests, several impor- tant and interesting correlations can be made from several critical factors in the zeta potential and PZC concentration determinations. These factors are water quality, material composition, inorganic additive cation valence, organic additive carbon-chain length, the effect of anionic and nonionic additives, the effect of anionic plus nonionic additive combinations, and the effect of excess cations on the zeta potential. These results given in the tables are discussed in the following sections. Table 4.-Materials tested Material Source Australian muscovite Barre Granite Biotite Charcoal granite Coal Cobalt Cobalt powder Diamond Dresser basalt Feldspar series (albite, andesine, anorthite, bytownite, microcline, and oligoclase). INCO section 275: Quartzite Pegmatite INCO 2800 level quartzite INCO 3400 level nickel-sulfide ore LCA pegmatite: Samples A and B Magnesium oxide brick °. Mahogany granite: Grindings Saw cuttings Minnesota taconite (whole, magnetic, and nonmagnetic fractions: Samples A, B, and C. Minntac taconite: Samples A and B Rockville Granite Salida granite Sioux Quartzite South Dakota feldspar Sudbury granite Tennessee marble Tungsten carbide: Powder and powder with 6 pet Co granules. Wausau quartzite Westerly Granite Purchased mineral sample. Barre, VT. Purchased mineral sample. St. Cloud, MN (known as St. Cloud Gray Granodiorite). Jim Walters Resources Coal Mine, Alabama. Purchased mineral sample. Hard Materials Research Inc., Mississauga, Ontario, Canada. Purchased mineral sample. Dresser Mine, Dresser, Wl. Purchased mineral sample. Thompson Mine, Thompson, Manitoba, Canada. Do. Do. Do. Lithium Corporation of America (LCA) mine, Bessemer City, NO Sample from previous MgO research project. Dakota Granite Quarry, Milbank, SD. Do. Erie Mining Co., Hoyt Lakes, MN. Minntac Mine, Eveleth, MN. St. Cloud, MN. Denver, CO. Jasper Stone Quarry, Jasper, MN. Purchased mineral sample. Sudbury, Ontario, Canada. Holston Limestone formation, east Tennessee. Hard Materials Research Inc., Mississauga, Ontario, Canada. Wisconsin. Bradford, Rl. Table 5.-Additives tested Additive Cone range Cationic: Aluminum chloride mol/L Aluminum nitrate mol/L Calcium chloride mol/L Magnesium sulfate mol/L Potassium aluminum sulfate mol/L Potassium chloride mol/L Sodium chloride mol/L Titanium iodide mol/L Zirconium chloride mol/L Zirconium nitrate mol/L DTAB mol/L HTAB mol/L TTAB mol/L Armac series (Akzo Chemie America) mol/L Nalco series (Nalco Corp.) mol/L Percol series (Allied Colloids, Inc.) mol/L Polyacrylamide (American Cyanamid) ppm Nonionic, ppm: Tergitol NPX (Union Carbide) Surfynol 465 (Air Products and Chemicals, Inc.) PEO (Union Carbide) HEC (Union Carbide) Revert (UOP Johnson, Inc.) Anionic, ppm: Biocut 2 Polymer Solulube (Texaco) Vibrastop ZEP Lubeeze (ZEP Manufacturing Co.) Dromus B 2 DTAB Dodecyltrimethyl ammonium bromide. HTAB Hexadecyltrimethyl ammonium bromide. HEC Hydroxyethyl cellulose. PEO Polyethylene oxide. TTAB Tetradecyltrimethyl ammonium bromide. 'Nalco 8830 was anionic. 2 Supplied by Longyear Canada. 1 X 10-1 1 X 10" 7 -1 1 X 10" 3 X 10"- X10" X10" -1 1 X 10'f-1 X 10 -1 -1 -1 -1 -1 1 X 10" 1 X 10" 1 X 10" : 1 X10" X X X 1 X 10" 7 -1 X 1 X10" 1 X10" 1 X 10" 1 X 10^-1 1 X 10' 7 -1 1 X 10" 7 -1 0.01- 0.1- 0.1- xi E UJ i- O CL < H LU N 100 80 60 40 20 -20 1 1 1 1 I 1 i ' I i i i i i i i i I I I II!!! II \_ I i i i i i i_e KEY I - D Test 1 A Test 2 - - O Test 3 % / - - - V A ' a - 7 I i i I i I I i I I I I i i i m I i i I l I I M 1 I 1 1 l l 1 1 I 10 100 1,000 ADDITIVE CONCENTRATION, 10* mol/L 10.000 Figure 5.-Example of AICI 3 high concentration test. 11 CONCLUSIONS This novel technique for the determination of the zeta potentials and the resulting PZC and/or ZSC concen- trations for materials in baseline water and additive so- lutions under many varied conditions should prove to be useful in other operations as well as in drilling, cutting, and grinding. Any needed zeta potential and/or PZC concen- tration values for a given system should be obtainable with the use of this closed-system technique and should prove to be very accurate, reliable, and repeatable. Any electro- phoretic mobility-type zeta potential equipment can be adapted to this technique. The zeta potential and PZC concentration values in this report, and the noted varia- tions in the values because of changes in additive and/or baseline waters, should further the understanding of how to control zeta potentials in many processes. Several conclusions can be drawn from the zeta poten- tial results by comparing the diversity of effect on the zeta potential caused by water quality, material type, cationic additives, anionic additives, and/or nonionic additives. The critical effect of each of these parameters must be con- sidered when determining zeta potentials and predicting PZC concentrations for any chemical additive-material system. Generalizations and close approximations can be made regarding the response of any particular material and/or additive in a zeta potential experiment. However, when precise or accurate zeta potentials and/or PZC concentrations are required, special care must be exercised. The use of the closed-system and graphing technique should yield those precise values required by the experimenter. REFERENCES 1. Akers, R J. Zeta Potential and the Use of the Electrophoretic Mass Transport Analyzer. Am. Lab. (Fairfield, CT), v. 4, June 1972, pp. 41-53. 2. Gaudin, A. M., and D. W. Fuerstenau. Quartz Flotation With Anionic Collectors. Min. Eng. (Littleton, CO), v. 202, Jan. 1955, pp. 66-72. 3. . Quartz Flotation With Cationic Collectors. Min. Eng. (Littleton, CO), v. 202, Oct. 1955, pp. 958-962. 4. Luce, R. W., and G. A. Porks. Point of Zero Charge of Weathered Forsterite. Chem. Geol., v. 12, 1973, pp. 147-153. 5. Macmillan, N. H., R. D. Huntington, and A. R. C. Westwood. Relationship Between Zeta Potential and Dislocation Mobility. Martin Marietta Corp. (Baltimore, MD), MML Tech. Rep. 73-1 lc, July 1973, 26 pp. 6. Martinez, E., and G. L. Zucker. Asbestos Ore Body Minerals Studied by Zeta Potential Measurements. J. Phys. Chem., v. 64, July 1960, pp. 924-926. 7. Engelmann, W. H., O. Terichow, and A. A. Selim. Zeta Potential and Pendulum Sclerometer Studies of Granite in a Solution Environment. BuMines RI 7048, 1967, 16 pp. 8. Engelmann, W. H. Chemical Fragmentation. Sec. in SME Mining Engineering Handbook, ed. by A. B. Cummins and I. A. Given. Soc. Min. Eng. AIME (Littleton, CO), 1973, pp. 11-112-11-123. 9. Watson, P. J., and W. H. Engelmann. Chemically Enhanced Drilling. An Annotated Tabulation of Published Results. BuMines IC 9039, 1985, 53 pp. 10. Engelmann, W. H., P. J. Watson, P. A. Tuzinski, and J. E. Pahlman. Zeta Potential Control for Simultaneous Enhancement of Penetration Rates and Bit Life in Rock Drilling. BuMines RI 9103, 1987, 18 pp. 12 APPENDIX Table A-1 .-Summary of zeta potential tests performed, by material type Material Additive Australian muscovite Barre Granite Biotite Charcoal granite . . . Coal (Jim Walters Resources) Cobalt Cobalt powder Diamond Dresser basalt Feldspar series: Albite Andesine Anorthite Bytownite Microcline Oligoclase INCO section 275: Quartzite Pegmatite INCO 2800 level quartzite INCO 3400 level nickel-sulfide ore LCA pegmatite Samples A and B Sample A Magnesium oxide brick Mahogany granite: Grindings Saw cuttings Aluminum chloride. Aluminum nitrate. Potassium chloride. HTAB. PEO in Roanoke, VA, tap water. Aluminum chloride. Do. Aluminum chloride in tap water. Calcium chloride. Magnesium sulfate. Sodium chloride. Zirconium chloride. PEO in tap water. Do. Aluminum chloride. PEO in tap water. Aluminum chloride. Do. Aluminum chloride in Dresser, Wl, city water. Aluminum chloride in mine water. Aluminum chloride, pH modified. Aluminum chloride. Do. Do. Do. Do. Do. PEO in INCO tap water. PEO in tap water. Do. Do. Do. Aluminum chloride. Aluminum chloride in mine water. Aluminum nitrate. Aluminum nitrate in mine water. Aluminum chloride in mine water. Aluminum nitrate in mine water. PEO in mine water. Nalco 8830. PEO. PEO in tap water. PEO in Dakota Granite quarry water. Do. Anionic polymer in tap water. ZEP Lubeeze in tap water. ZEP Lubeeze in quarry water. ZEP Lubeeze plus PEO in quarry water. Minnesota taconite: Whole, magnetic, and nonmagnetic fractions: Samples A, B, and C Samples A and B Whole fractions: Samples A and B Aluminum chloride. Aluminum chloride in November mine water. Aluminum chloride in May mine water. Aluminum chloride, pH modified. Nalco 7132 in mine water. Percol 402 in mine water. PEO. PEO in tap water. PEO in mine water. See explanatory notes at end of table. 13 Table A-1 .-Summary of zeta potential tests performed, by material type-Continued Material Additive 1 Minntac taconite: Sample A Sample B Rockville Granite Salida granite . Sioux Quartzite South Dakota feldspar Sudbury granite . . Tennessee marble Aluminum chloride. PEO in mine water. Aluminum chloride. PEO in mine water. Aluminum chloride. Aluminum chloride in tap water. Calcium chloride. Magnesium sulfate. Sodium chloride. Zirconium chloride. DTAB. HTAB. TTAB. PEO in tap water. Aluminum chloride in Denver, CO, tap water, pH modified. PEO in Denver, CO, tap water. Aluminum chloride. Aluminum chloride in tap water. Aluminum chloride in tap water, pH modified. Aluminum chloride at high concentrations. Aluminum nitrate. Calcium chloride. Magnesium sulfate. Potassium aluminum sulfate. Sodium chloride. Titanium iodide. Zirconium chloride. Zirconium nitrate. DTAB. HTAB. HTAB in tap water. TTAB. Armac series. Nalco series. Percol series. Tergitol NPX. Surfynol 465 in tap water. Biocut in tap water. HEC in tap water. Revert in tap water. Soluble in tap water. Vibrastop in tap water. Polyacrylamide in tap water. PEO. PEO in tap water. PEO in Farmington, MN, tap water. Aluminum chloride. Calcium chloride. Magnesium sulfate. DTAB. HTAB. TTAB. PEO in tap water. PEO plus Dromus B in tap water. Aluminum chloride. Aluminum chloride in tap water. Calcium chloride. Magnesium sulfate. Sodium chloride. Titanium iodide. Zirconium chloride. Zirconium nitrate. DTAB. HTAB. TTAB. PEO in Farmington, MN, tap water. See explanatory notes at end of table. 14 Table A-1 .-Summary of zeta potential tests performed, by material type-Continued Material Additive 1 Tungsten carbide: Powder Powder with 6 pet Co granules Wausau quartzite Westerly Granite PEO in tap water. Do. Aluminum chloride. Calcium chloride. Magnesium sulfate. Sodium chloride. Zirconium chloride. Zirconium nitrate. DTAB. HTAB. TTAB. Aluminum chloride. Aluminum chloride in tap water. Calcium chloride. Magnesium sulfate. Sodium chloride. Zirconium chloride. PEO in tap water. DDIW Deionized, distilled water. DTAB Dodecyltrimethyl ammonium bromide. HTAB Hexadecyltrimethyl ammonium bromide. HEC Hydroxyethyl cellulose. PEO Polyethylene oxide. TTAB Tetradecyltrimethyl ammonium bromide. 1 A1! tests conducted in DDIW unless otherwise stated. Tap water used was from Minneapolis, MN, unless otherwise stated. 15 Table A-2.-Summary of zeta potential tests performed, by additive Additive Material Aluminum chloride Alumnium chloride in tap water Aluminum chloride, pH modified Aluminum chloride in LCA mine water Aluminum chloride in Erie mine water Aluminum chloride in Dresser, Wl, tap water Aluminum chloride in Denver, CO, tap water, pH modified Aluminum chloride in Erie mine water, pH modified Aluminum chloride in Dresser, Wl, city water Aluminum nitrate Aluminum nitrate in LCA mine water Calcium chloride Magnesium sulfate Potassium aluminum sulfate Potassium chloride Sodium chloride Titanium iodide . . Zirconium chloride Zirconium nitrate Australian muscovite. Biotite. Charcoal granite. Cobalt powder. Diamond. Dresser basalt. Feldspar series. LCA pegmatite. Minnesota taconite. Minntac samples A and B. Rockville Granite. Sioux Quartzite. South Dakota feldspar. Tennessee marble. Wausau quartzite. Westerly Granite. Charcoal granite. Rockville Granite. Sioux Quartzite. Tennessee marble. Westerly Granite. Dresser basalt. Sioux Quartzite. LCA pegmatite. Minnesota taconite. Dresser basalt. Salida granite. Minnesota taconite. Dresser basalt. Australian muscovite. LCA pegmatite. Sioux Quartzite. LCA pegmatite. Charcoal granite. Rockville Granite. Sioux Quartzite. South Dakota feldspar. Tennessee marble. Wausau quartzite. Westerly Granite. Charcoal granite. Rockville Granite. Sioux Quartzite. South Dakota feldspar. Tennessee marble. Wausau quartzite. Westerly Granite. Sioux Quartzite. Australian muscovite. Charcoal granite. Rockville Granite. Sioux Quartzite. Tennessee marble. Wausau quartzite. Westerly Granite. Sioux Quartzite. Tennessee marble. Charcoal granite. Rockville Granite. Sioux Quartzite. Tennessee marble. Wausau quartzite. Westerly Granite. Sioux Quartzite. Tennessee marble. Wausau quartzite. See explanatory notes at end of table. 16 Table A-2.-Summary of zeta potential tests performed, by additive-Continued Additive Material DTAB HTAB HTAB in tap water TTAB Armac series Nalco series Nalco 7132 in Erie mine water Percol series Percol 402 in Erie mine water . Polyacrylamide in tap water . . Anionic polymer in tap water . Biocut in tap water Tergitol NPX Solulube in tap water Surfynol 465 in tap water Vibrastop in tap water ZEP Lubeeze in tap water ZEP Lubeeze in quarry water HEC in tap water Revert in tap water PEO PEO in tap water PEO in Roanoke, VA, tap water PEO in Denver, CO, tap water PEO in Farmington, MN, tap water PEO in INCO tap water PEO in LCA mine water PEO in Erie mine water PEO in Minntac mine water PEO in quarry water PEO plus Dromus B in tap water PEO plus ZEP Lube eze in quarry water DDIW Deionized, distilled water. DTAB Dodecyltrimethyl ammonium bromide. HEC Hydroxyethyl cellulose. HTAB Hexadecyltrimethyl ammonium bromide. PEO Polyethylene oxide. TTAB Tetradecyltrimethyl ammonium bromide. 'All tests conducted in DDIW unless otherwise stated. Tap water used was from Rockville Granite. Sioux Quartzite. South Dakota feldspar. Tennessee marble. Wausau quartzite. Australian muscovite. Rockville Granite. Sioux Quartzite. South Dakota feldspar. Tennessee marble. Wausau quartzite. Sioux Quartzite. Rockville Granite. Sioux Quartzite. South Dakota feldspar. Tennessee marble. Wausau quartzite. Sioux Quartzite. Do. Minnesota taconite sample B. Sioux Quartzite. Minnesota taconite sample B. Sioux Quartzite. Mahogany granite. Sioux Quartzite. Do. Do. Do. Do. Mahogany granite. Do. Sioux Quartzite. Do. Magnesium oxide brick. Minnesota taconite sample B. Sioux Quartzite. Charcoal granite. Coal (Jim Walters Resources). Cobalt powder. INCO section 275 quartzite. INCO section 275 pegmatite. INCO 2800 level quartzite. INCO 3400 level nickel-sulfide ore. Magnesium oxide brick. Minnesota taconite sample B. Rockville Granite. Sioux Quartzite. Sudbury granite. Tungsten carbide powder. Tungsten carbide powder with 6 pet Co granules. Westerly Granite. Barre Granite. Salida granite. Sioux Quartzite. Tennessee marble. INCO section 275 quartzite. LCA pegmatite sample A. Minnesota taconite sample B. Minntac sample A. Minntac sample B. Mahogany granite. Sudbury granite. Mahogany granite. Minneapolis, MN, unless otherwise stated. Table A-3. -Chemical analyses of waters used 17 Al, PPm Ca, Mg, PPm Mn, PPm Na, Pp™ K, ppm s r- 3 O TI TI Dep au o ES fiingl O o artm f Mil treet on, S3 > °0 r~ O- ? fl> 3 I =: 03 S nt of es N.W. .C. m c (A m I ■4ft z m jo- ._ ^ CO u tO § CO 2. o o o -• > z m O O TJ TJ O DO 3 m O -< m 3D 125 90 > V » «. * »- ^ 5*1$* \<* • ^ A^ »J< 6? ^is .^^ A -*S ^» A^^. o% §?• C*< % f / V^v %-^v V^V %' ^o< -ot^ .<£°** • %**':tit&.\f r ** v \ r** ♦*~** <°^ °* ^^t% ^.^fe-% X.^i.% V 6«»? HECKMAN BINDERY INC. ^ FEB 90 N. MANCHESTER, «^^ INDIANA 46962 .i» ..^. o » e *<$i^ 4°" \