Abstract:
The current technology relates to mining processes and compositions which inhibit the growth of complex scale. More specifically it relates to a process for preventing/inhibiting and/or controlling gypsum scale in aqueous mineral ore slurries, and for inhibiting scale in relatively high solids content environments in industrial mining operations.

Description:
[0001]    This application claims the benefit of U.S. provisional application No. 61/890,998, filed 15 Oct. 2013, the entire contents of which are hereby incorporated by reference. 
     
    
     BACKGROUND OF THE INVENTION 
       [0002]    The invention relates to compositions which inhibit the growth of complex scale, more specifically gypsum scale in aqueous mineral ore slurries, and methods for inhibiting scale in relatively high solids content environments in industrial mining operations. The compositions comprise an active selected from carboxylate polymers, polyamine acids, organic phosphonates and the like. 
         [0003]    The mineral industry is a large consumer of chemicals which are used during many stages of the processing of the mineral ore. For example, chemicals are added to inhibit the development of various types of scale which can develop in different stages of ore processing. Different conditions during different unit operations of ore processing systems require different chemicals to inhibit the scale. 
         [0004]    The processing of mineral ore is very complex with maintenance required to maintain throughput throughout the process, with maintenance downtime kept to a minimum, thus allowing for more ore to be processed at less cost Unit operations within an industrial mining process involving the formation and/or cooling of mineral ore slurries need constant monitoring, cleaning and maintenance of equipment Examples of such equipment include quench tanks and autoclaves, as well as ancillary lines and equipment. Quench tanks and autoclaves, as well as ancillary lines and equipment, are subject to scaling which if not prevented requires stopping the mining operation and physically removing the scale. 
         [0005]    The mining industry is constantly seeking new additive technologies that will increase the efficiency of ore processing during various stages, thus enhancing the overall ore recovery in mineral processing operations. Chemicals, and chemical combinations, have been shown to inhibit scale in aqueous solutions. However, the conditions of the ore change dramatically throughout the processing and the mineral ore in the cooling stages of a quench tank or autoclave operation can have 
         [0006]    However, the conditions of the ore change dramatically throughout the processing and the mineral ore in the cooling stages of a quench tank or autoclave operation can have high solids content, i.e. in the form of slurry and are not 100% aqueous. New chemicals must be found to enhance mineral ore processing when in the slurry phase. Further, due to increased environmental concerns over mining operations, chemical anti-sealant additives comprising natural materials that provide decreased environmental harm are desired. 
         [0007]    All parts and percentages set forth herein are on a weight-by weight basis unless otherwise indicated. 
       SUMMARY OF THE INVENTION 
       [0008]    The compositions useful as anti-sealant controls in mining operations in the aqueous slurry phase comprise an active component selected from the group consisting of carboxylate polymers, polyamine acids, organic phosphonates, and the like, and combinations thereof. The anti-sealant compositions are typically added to mineral slurry in the mining operation in an amount effective to inhibit the formation of scale in pipes and equipment used for ore recovery, for example with respect to a quench tank or autoclave the composition can be added to the slurry in the quench tank or autoclave, and/or in an ancillary line or piece of equipment. Thus, the invention encompasses a mineral ore slurry comprising an aqueous phase having a mineral ore and a anti-sealant composition comprising an active component selected from the group consisting of carboxylate polymers, polyamino acids, organic phosphonates, and the like, and combinations thereof in an amount effective to inhibit scale on the metal, polymer, plastic or ceramic surfaces of the quench tank or autoclave, and/or ancillary line or equipment. 
         [0009]    Generally, application of the anti-sealant increases the capacity and throughput of mineral ores in the mining process by inhibiting the build-up of complex scale, in particular gypsum scale, in the interior walls and devices of the equipment and piping. This will benefit operations by decreasing downtime and cost associated with it due to cleaning and maintenance and also helps create a more efficient system by moving more ore slurry through the cooling process in shorter time periods. In addition, the use of the anti-sealant also reduces health and safety risks associated with high frequency quench circuit mechanical de-scaling and increases quench tank circuit equipment life time. 
     
    
     
       DESCRIPTION OF THE DRAWINGS 
         [0010]      FIG. 1  shows a typical mineral ore quenching operation in an embodiment of the invention. 
           [0011]      FIG. 2  shows typical mineral ore quenching operation comprising preliminary quench devices in an embodiment of the invention. 
           [0012]      FIG. 3  shows a typical mineral ore autoclave operation in an embodiment of the invention. 
       
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       [0013]    The active component of the anti-sealant composition can be selected from carboxylate polymers having the formula 
         [0000]      R 1 —CH 2 —CH(CO 2 H)—R 2 -R 3  
 
         [0000]    wherein R 1  is selected from a functional group, R 2  is a polycarboxylate and R 3  is hydrogen or a functional group. In embodiments, the functional groups of R 1  and R 3  comprise sulfonate, sulfate, phosphinate, phosphonate, alcohol, 1,1-diphenyl hexyl, tert-butyl, mercaptoethanol, mercaptopropionic acid, mercaptoglycolic acid and R 2  comprises a polyacrylic acid. Typically, the carboxylate polymers will have a molecular weight between about 1,000 g/mol to about 20,000 g/mol, such as between about 2,000 g/mol to about 12,000 g/mol. In an embodiment, the carboxylate polymer comprises polyacrylic acid. 
         [0014]    In one aspect, the active component of the anti-sealant composition can be selected from polyamine acids having the formula 
         [0000]      poly(X) m poly(Y) n , 
         [0000]    wherein X and Y are independently selected from the group consisting of an amino acid, a salt of an amino acid and an amino acid derivative, and m can be from about 2 to about 60, n can be up to about 60, and the sum of m and n is at least about 5. For example, X and Y may be independently selected from the group consisting of aspartic acid, glutamic acid, lysine, aspartate, glutamate, a salt of lysine, an aspartate derivative, a glutamate derivative, and a lysine derivative; m can be from about 5 to about 12; n can up to about 12 and the sum of m and n can be from about 5 to about 12. In one aspect the polyamine acid can comprise polyaspartic acid. 
         [0015]    The active component of the anti-sealant composition can be selected from organic phosphonates. In particular, the organic phosphonate may be selected from the group consisting of hexamethylene diamine tetra(methylene phosphonic acid) (“HDTMPA”), diethylenetriamine penta(methylene phosphonic acid) (“DETPMPA”), bis(hexamethylene triamine penta(methylene phosphonic acid) (“BHMTPMPA”) and the like, and combinations thereof. The anti-sealant composition is useful to control complex scale, such as gypsum scale, in mining operations. Typically, the process comprises the steps of adding to the aqueous mineral ore slurry having an aqueous phase an effective scale inhibiting amount of a scale inhibiting composition comprising an active component selected from the group consisting of i) a carboxylate polymer having the formula 
         [0000]      R 1 —CH 2 —CH(CO 2 H)—R 2 -R 3  
 
         [0000]    wherein R 1  is selected from the group consisting of sulfonate, sulfate, phosphinate, phosphonate, alcohol, 1,1-diphenyl hexyl, tert-butyl, mercaptoethanol, mercaptopropionic acid, mercaptoglycolic acid, R 2  is i) a polycarboxylate, and R 3  is H or R 1 ; ii) a polyamine acid having the formula: poly(X)mpoly(Y)n, wherein X and Y are independently selected from the group consisting of an amino acid, a salt of an amino acid and an amino acid derivative, and m can be from about 2 to about 60, n can be up to about 60, and the sum of m and n is at least about 5; and iii) an organic phosphonate; wherein the pH of the slurry is below 9.0 and the complex scale comprises gypsum. 
         [0016]    In an embodiment of the invention, the pH can be from about 3.0 to about 9.0, typically greater than about 4.0 to about 9.0, can be from about 4.5 to about 9.0, and may be from about 5.0 to about 8.0. The process may be applied to mineral ore slurries with mineral ore having temperatures of up to about 550° C., can be up to about 450° C., can be up to about 400° C., may be from about 40° C. to about 550° C., or from about 40° C. to about 450° C. Persons of ordinary skill in these arts, after reading this disclosure, will appreciate that all ranges and values for the pH and temperature ranges are contemplated. With respect to the active component of the anti-sealant composition, any of the active compounds discussed in this Specification may be used in the process. 
         [0017]    The anti-sealant composition described herein may be used for controlling complex scale, typically gypsum scale, in mineral ore slurry forming and cooling operations; such as an ore quench operation or an autoclave operation, including any associated piping or ancillary equipment. In some aspects, such processes may comprise the steps of a) providing an ore quench tank having a vessel with an interior surface or an autoclave having an interior surface, at least one feed line having an interior surface and at least one discharge line having an interior surface; b) providing a mineral ore slurry comprising mineral ore and an aqueous phase; c) adding to the mineral ore slurry an effective amount of a scale inhibiting composition comprising an active component selected from the group consisting of i) a carboxylate polymer having the formula: 
         [0000]      R 1 —CH 2 —CH(CO 2 H)—R 2 -R 3 ,
 
         [0000]    wherein R 1  can be selected from the group consisting of a sulfonate, sulfate, phosphinate, phosphonate, an alcohol, 1,1-diphenylhexyl, tert-butyl, mercaptoethanol, mercaptopropionic acid, mercaptoglycolic acid, R 2  is i) a polycarboxylate, and R 3  is H or R 1 ; ii) a polyamine acid having the formula: 
         [0000]      poly(X) m Poly(Y) n , 
         [0000]    wherein X and Y are independently selected from an amino acid and m is about 2 to about 60, n is up to about 60, and sum of m and n is at least about 5; and iii) an organic phosphonate, and wherein the pH of the mineral ore slurry in the vessel is below 9.0, can be from about 3.0 to about 9.0, can be greater than about 4.0 to about 9.0, can be from about 4.5 to about 9.0, can be from about 5.0 to about 8.0, and may be from about 7.0 to about 8.5. 
         [0018]    In some aspects, the temperature of the mineral ore in the slurry, particularly in the quench tank, is up to about 550° C., can be up to about 450° C., can be up to about 400° C., from about 40° C. to about 550° C., or from about 40° C. to about 450° C. In some aspects the temperature ranges of the mineral ore in the slurry in an autoclave can be up to about 220° C., can be up to about 190° C., with a typical temperature gradient of from about 80° C. to about 220° C., like about 80° C. to about 190° C. Persons of ordinary skill in these arts, after reading this disclosure, will appreciate that all ranges and values for the pH and temperature ranges are contemplated. With respect to the active component of the anti-sealant composition useful in this process, any of the active compounds discussed in this Specification may be used in the process. 
         [0019]    Typically, the solids content of the mineral ore slurry, that is the amount of mineral ore (mineral ore content) in the slurry, is at least about 8%, at least about 10%, at least about 20%, at least about 30%. For example, the mineral ore slurry may have a solids content of about 8% to about 30%, including about 10% to about 20%, such as about 10% to about 15%. Persons of ordinary skill in these arts, after reading this disclosure, will appreciate that all ranges and values for the solids content are contemplated. 
         [0020]    The mineral ore slurry generally comprises a mineral ore having a component selected from the group consisting of a precious metal, a base metal and combinations thereof. The mineral ore slurry can comprise a mineral selected from the group consisting of gold, aluminum, silver, platinum, copper, nickel, zinc, lead, molybdenum, cobalt, and the like, and combinations thereof. The mineral ore slurry may farther comprise one or more of quartz, dolomite, calcite, gypsum, barite or muscovite, and the like, and combinations thereof. 
         [0021]    The mineral ore slurry can comprise from about 5 ppm to about 300 ppm of the active component in the scale inhibiting composition per the aqueous phase. In some embodiments, the amount of active may be from about 15 ppm to about 250 ppm, can be from about 20 ppm to about 100 ppm, and may be from about 25 ppm to about 50 ppm. Persons of ordinary skill in these arts, after reading this disclosure, will appreciate that all ranges and values for the amount of active component are contemplated. 
         [0022]    The complex scale, such as gypsum, may be present on the interior surface of at least one feed line, the interior surface of the vessel of the quench tank or autoclave, the interior surface of at the least one discharge line or combinations thereof, as well as on any internal mechanisms or devices. The scale inhibiting composition can be added to the mineral ore slurry in at least one feed line, in at least one discharge line, in the vessel of the quench tank or in the autoclave or combinations thereof. 
         [0023]    An ore quenching operation, particularly applied with recovery of minerals and precious metals in the case of gold ore, is illustrated in  FIG. 1 . In the quenching operation  1 , hot, dry calcine from an upstream unit operation, typically a roaster (not shown) is processed to a calcine cooler  2 . After cooling, the calcine is fed through a feed line and/or launder line  3  to the quench tank  4 . In the operation shown in  FIG. 1 , water is added to the calcine in the feed line and/or launder line  3  via cooling water feed pipe  13  prior to the quench tank  4  to form the mineral ore slurry that is cooled in the quench tank  4 . After cooling, the mineral ore slurry exits the quench tank  4  through a discharge line  5  to downstream unit operations. Optionally, a portion of the aqueous phase of the mineral ore slurry may be circulated by pipes  6  and  6 ′ from the quench tank to a scrubber  7  and back as part of the operation. Gaseous material can be vented from the scrubber through a vent pipe  8 . In an alternative method, not shown, water is added to the calcine to form the mineral ore slurry in the vessel of the quench tank  4  and not in the feed line and/or launder line  3 . 
         [0024]    Alternative quenching operations comprise at least one preliminary quench device comprising a preliminary quench device vessel having a preliminary quench device vessel interior wall and providing water and hot, dry calcine wherein the water is added to the calcine in the preliminary quench device vessel to form the mineral ore slurry and complex scale is on the preliminary quench device vessel interior wall. In a further embodiment, the water is added to the vessel of the quench tank to form the mineral ore slurry instead of the in the preliminary quench device. The mineral ore slurry is transported to the quench tank from the preliminary quench device by the feed line and/or launder line. In these embodiments the scale inhibiting composition is generally added to the mineral ore slurry in the preliminary quench device vessel, the feed line and/or launder line, or can be added directly to quench tank and piping section coming out of quench tank depending on severity of scale formation and location of severe zones of scale formation, or combinations thereof. 
         [0025]      FIG. 2  illustrates a mineral ore quenching operation  9  comprising two preliminary quench devices. In this operation  9 , hot, dry calcine is transported from an upstream unit operation to first preliminary quench device  10 . One skilled in the art will recognize that the first preliminary quench device will comprise a first preliminary quench device vessel having a first preliminary quench device vessel interior wall. Water is added to the hot, dry calcine in first preliminary quench device  10 , typically within preliminary quench device vessel, to form the mineral ore slurry. The mineral ore slurry is conveyed from the first preliminary quench device  10  to a second preliminary quench device  11  through a means  12  to convey mineral ore slurry from the first preliminary quench device  10  to the second preliminary quench device  11  which, as one skilled in the art will appreciate, has a conveyance means interior wall. Typically, the means  12  is a pipe. One skilled in the art will also recognize that the second preliminary quench device  11  comprises a second preliminary quench device vessel having a second preliminary quench device vessel interior wall. Some cooling of the mineral ore slurry occurs in second preliminary quench device  11 . After the second preliminary quench device  11  the mineral ore slurry undergoes similar processing as that shown in  FIG. 1 , however the mineral ore slurry is not formed in the feed line or launder line  3 . The mineral ore from the second preliminary quench device  11  is sent to the quench tank  4  through feed line or launder line  3 . After cooling, the mineral ore slurry exits the quench tank  4  through a discharge line  5  to downstream unit operations. Optionally, a portion of the water phase of the mineral ore slurry may be circulated by pipes  6  and  6 ′ from the quench tank to a scrubber  7  and back to quench tank  4  as part of the operation. Gaseous material can be vented from the scrubber through a vent pipe  8 . Cooling water may be added through pipe system  25  to one or more of the first preliminary quench device  10 , second preliminary quench device  11  and quench tank  4  and scrubber  7 . In this method, the scale inhibiting composition may be added to the mineral ore slurry in the first preliminary quench tank device  10 , the second preliminary quench device  11 , the means  10 , feed line or launder line  3  or quench tank  4 . Complex scale may form on the first preliminary quench device vessel interior wall, the second preliminary quench device vessel interior wall, conveyance means interior wall or combinations thereof, in addition to the mechanisms and internal components of the mineral ore quenching operation discussed above, including those discussed with the operation shown in  FIG. 1 . 
         [0026]    Although  FIG. 2  illustrates and operation comprising a first preliminary quench device  10  and a second preliminary quench device  11 , operations comprising one or more than two of such devices, such as 3, 4, 5, 6, 7, 8, 9, 10, 11, 12 or more preliminary quench devices, are within the scope of the invention. 
         [0027]    In some aspects, the temperatures of the for hot calcine ore entering the quench tank are very high, such as up to about 550° C. and can be up to about 450° C. Typically, within the vessel, of the quench tank the temperature gradient for calcine can range from about 40° C. to about 550° C., can be from about 40° C. to about 450° C., with higher temperatures towards the top of quench tank. However, due to very short period of time for calcine slurry residence in the quench tank vessel and low pressure, the slurry aqueous phase bulk temperature should be not be higher than about 100° C. 
         [0028]      FIG. 3  shows a typical autoclave process  14  used to for mineral ore slurries. Typically, these processes will be applied to oxidize mineral ore slurry comprising acid, such as sulfuric acid, using oxygen in a high pressure and temperature environment prior to leaching the mineral from the ore in aJ so called acid oxidation autoclave processes. Also, the circuits described herein may be used in alkaline oxidation autoclave processes. The anti-sealant compositions described herein can be used in both acid oxidation autoclave processes and alkaline oxidation autoclave processes. As shown in  FIG. 3 , mineral ore slurry is mixed with acid or base upstream of the autoclave and the mineral ore slurry enters one or more heating towers  15 , which as shown in  FIG. 3  may be in series, to preheat the slurry. The preheated slurry may then be sent through a heating tower discharge line  16  as shown in  FIG. 3  to a condenser  17  and then to a feed line  18  to the autoclave  19 . One skilled in the art will appreciate that the condenser  17  is optional and the mineral ore slurry can be sent through the feed line  18  to the autoclave  19  directly from a heating tower  15 . Oxygen and steam may be added to the autoclave  19  such as in an acid oxidation autoclave process to oxidize the mineral ore slurry to oxidize sulfide material in the slurry, at high temperatures and pressure. The mineral ore slurry exits the autoclave  19  through a discharge line  20  to one or more cooling towers  21 , which as shown in  FIG. 3  may be in series, in which the slurry is cooled, for example, passing through flash cooling towers and then sent to downstream operations. Optionally, water phase from the mineral ore slurry may be circulated through a cyclone  22  through pipes  23  and  23 ′. Also, in certain embodiments, the mineral ore slurry may be processed via a heat exchanger feed line  26  through one or more heat exchangers  24  to further reduce slurry temperature prior to downstream processing. Typically, after the autoclave operation and subsequent cooling the mineral ore slurry undergoes neutralization and/or leaching. One skilled in the art will appreciate that although three heating towers and cooling towers and one autoclave are depicted in  FIG. 3 , the invention encompasses processes independently having any number of heating towers, cooling towers or autoclaves. Each of the pieces of equipment in the autoclaving operation such as shown in  FIG. 3 , including the heating towers  15 , heating tower discharge line  161  condenser  17 , feed line  18 , autoclave  19 , cooling towers  21 , heat exchanger feed line  26  and heat exchanger  24 , as well as other equipment and lines, will have interior surfaces or interior walls and possibly other mechanisms such as stirrers and heat exchange devices. Scale, such as gypsum scale, may form on any of the interior surfaces or walls or the surfaces of any internal devices exposed to the mineral ore slurry and any other associated equipment, pipes and lines. 
         [0029]    The temperature of the mineral ore of the acidified mineral ore slurry in the pressurized autoclave is high, such as up to about 220° C., can be up to about 190° C. Typically, within the autoclave the temperature range for the mineral ore can be from about 80° C. to about 250° C. and may be from about 80° C. to about 190° C. The pressure in autoclave operation can vary from about 400 kPa to about 4,000 kPa. Similar temperatures, but typically in a lower range specified above, may be experienced in the other equipment and piping associated with the autoclaving operation, such as, for example, the heating towers  15 , condenser  17 , cooling towers  21 , a′″:ld heat exchanger  24  and the associated equipment, pipes and lines. In alkaline oxidation autoclave process and slurry cooling circuits the typical pH range for ore slurry, discharged from high pressure autoclave, is below 9.0, more specifically between about 7.0 and about 8.5. 
       Examples 
       [0030]    In the Examples, scale inhibition was analyzed using a Model KS 4000 ic IKA shaker bath with a set of 16 10 oz jars. The details of equipment, reagents and protocol are described below. 
       Examples 1-15 
       [0031]    Mimic water, that is water having salt content typically found in mining operations, particularly gold mines, was made by combining de-ionized water with the following salts: CaCl 2 .2H 2 O, MgSO 4 .7H 2 O, Na 2 SO 4 , Al 2 (SO 4 ) 3 , FeSO 4 .7H 2 O, CuSO 4 .7H 2 O. The composition of the mimic water after gypsum formation is set forth in Table 1. 
         [0000]    
       
         
               
             
               
               
               
               
               
               
               
               
             
           
               
                 TABLE 1 
               
             
             
               
                   
               
               
                 Mimic water composition 
               
             
          
           
               
                   
                   
                 Mag- 
                 Chlor- 
                   
                   
                   
                   
               
               
                 Wt % 
                 Calcium, 
                 nesium, 
                 ides, 
                 Sulfates, 
                 Al 3 , 
                 Cu 2+ , 
                 Fe2+, 
               
               
                 Gypsum 
                 ppm 
                 ppm 
                 ppm 
                 ppm 
                 ppm 
                 ppm 
                 ppm 
               
               
                   
               
               
                 0.75 
                 5690 
                 3806 
                 4034 
                 10926 
                 1.0 
                 3.8 
                 1.0 
               
               
                   
               
               
                 Where: Ca and Mg amounts are expressed as CaC03 and MgC03 respectively. Gypsum wt % corresponds to total amount of gypsum formed in situ in mimic water. 
               
             
          
         
       
     
         [0032]    The mimic water was composed of proper salts to set gypsum scale in situ formation, with a small amount of polyvalent ions added. Gypsum scale super saturation ratio was kept constant for all examples. 
         [0033]    For each Example 1-15, mimic water set forth in Table 1 was added to jars with the type and amount of scale inhibiting composition set forth in Table 2. Two jars with only mimic water and no scale inhibiting composition (controls) were also made up for comparison. The jars were placed in the IKA shaker bath with revolutions per minute (“rpm”) kept constant at 130 rpm and a temperature of 60° C. with pH at 5.5 to 6.0. The tests typically lasted 16 to 18 hours to ensure sufficient time to reach the state of equilibrium for scale formation. The percent inhibition by mass was calculated using a proprietary mass balance method applied to Ashland&#39;s scale deposition test. The water, after filtering out of suspended scale/slurry, was submitted to ICP analysis and threshold inhibition was measured using ICP analysis by the amount of soluble Ca-ion and calculated by: 
         [0000]    
       
         
           
             
               
                 
                   
                     
                       
                         Conc 
                         . 
                         
                             
                         
                          
                         of 
                       
                        
                       
                           
                       
                        
                       Cain 
                        
                       
                           
                       
                        
                       treated 
                        
                       
                           
                       
                        
                       Jars 
                        
                       
                           
                       
                        
                       
                         ( 
                         ppm 
                         ) 
                       
                     
                     - 
                   
                 
               
               
                 
                   
                     
                       Conc 
                       . 
                       
                           
                       
                        
                       of 
                     
                      
                     
                         
                     
                      
                     Cain 
                      
                     
                         
                     
                      
                     Blank 
                      
                     
                         
                     
                      
                     
                       ( 
                       ppm 
                       ) 
                     
                   
                 
               
             
             
               
                 
                   
                     
                       Total 
                        
                       
                           
                       
                        
                       amount 
                        
                       
                           
                       
                        
                       of 
                        
                       
                           
                       
                        
                       Caused 
                        
                       
                           
                       
                        
                       
                         ( 
                         
                           control 
                            
                           
                               
                           
                            
                           run 
                            
                           
                               
                           
                            
                           every 
                            
                           
                               
                           
                            
                           test 
                         
                         ) 
                       
                        
                       
                         ( 
                         ppm 
                         ) 
                       
                     
                     - 
                   
                 
               
               
                 
                   
                     
                       Conc 
                       . 
                       
                           
                       
                        
                       of 
                     
                      
                     
                         
                     
                      
                     Cain 
                      
                     
                         
                     
                      
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                      
                     
                         
                     
                      
                     
                       ( 
                       ppm 
                       ) 
                     
                   
                 
               
             
           
         
       
     
         [0034]    The results of percent (%) inhibition by ICP and percent (%) inhibition by mass of scale deposited are set forth in Table 2. All tests have been repeated 2 to 4 times on average to achieve good reproducibility. 
         [0000]    
       
         
               
             
               
               
               
               
               
             
               
               
               
               
               
             
           
               
                 TABLE 2 
               
             
             
               
                   
               
               
                 Deposition and threshold inhibition data for scale inhibiting products in mimic 
               
               
                 water 
               
             
          
           
               
                 Example# 
                 Product 
                 Product 
                 % Inhibition ICP 
                 % Deposition Inhibition by Mass 
               
               
                   
               
             
          
           
               
                 Comparative 1 
                 50 ppm in water 
                 Polystabil AN (Batch 
                 72.37 
                 95.58 
               
               
                 Comparative 2 
                 25 ppm in water 
                 Polystabil AN (Batch 
                 0.00 
                 0.00 
               
               
                 Comparative 3 
                 50 ppm in water 
                 Baypure 
                 71.37 
                 96.15 
               
               
                 Comparative 4 
                 25 ppm in water 
                 Baypure 
                 0.00 
                 17.52 
               
               
                 Comparative 5 
                 50 ppm in water 
                 Mayoquest 1635 
                 72.33 
                 97.48 
               
               
                 Comparative 6 
                 25 ppm in water 
                 Mayoquest 1635 
                 0.00 
                 −3.94 
               
               
                 Comparative 7 
                 50 ppm in water 
                 Polystabil AN (Batch 
                 54.78 
                 74.12 
               
               
                 Comparative 8 
                 25 ppm in water 
                 Polystabil AN (Batch 
                 0.00 
                 −2.48 
               
               
                 Comparative 9 
                 50 ppm in water 
                 Dequest 2066 
                 5.70 
                 −3.54 
               
               
                 Comparative 10 
                 25 ppm in water 
                 Dequest 2066 
                 0.00 
                 41.46 
               
               
                 Comparative 11 
                 50 ppm in water 
                 Drew 11-664 
                 2.23 
                 −11.59 
               
               
                 Comparative 12 
                 50 ppm in water 
                 Cublen 45 
                 2.55 
                 −18.01 
               
               
                 Comparative 13 
                 50 ppm in water 
                 Degapas 1105N 
                 11.69 
                 34.78 
               
               
                 Comparative 14 
                 50 ppm in water 
                 Polystabi I ANA 
                 35.39 
                 76.24 
               
               
                 Comparative 15 
                 50 ppm in water 
                 Polystabil VZK 
                 52.70 
                 80.66 
               
               
                 Comparative 16 
                 50 ppm in water 
                 Polystabil AN 
                 25.06 
                 49.25 
               
               
                   
               
             
          
         
       
     
         [0035]    In Table 2, product amount is expressed in ppm (parts per million or mg/L) of active ingredient per mimic water phase. Soluble Ca ion was measured by ICP. Total scale deposited, mass percent, was measured by a proprietary method. 
         [0036]    The results summarized in Table 2 show a broad range of scale inhibition efficacy by both deposition and threshold mechanisms. Threshold inhibition varies from 0% to 100%. Polyacrylate, polyaspartate and organic phosphonate, HDTMPA, acid salts showed the best efficacy. 
       Examples 17-27 
       [0037]    In Examples 17-27, dried mine slurry relevant to a quench tank circuit and having the compositions set forth in Tables 3 and 4 was re-dispersed at a given weight percent dose levels in water to obtain aqueous slurries. 
         [0000]    
       
         
               
             
               
               
               
             
               
               
               
             
           
               
                 TABLE 3 
               
             
             
               
                   
               
               
                 Slurry composition, Case 1 
               
             
          
           
               
                   
                 Slurry Components (Dry) 
                 Wt % 
               
               
                   
                   
               
             
          
           
               
                   
                 Quartz 
                 67% 
               
               
                   
                 Dolomite 
                 9% 
               
               
                   
                 Calcite 
                 6% 
               
               
                   
                 Gypsum 
                 5% 
               
               
                   
                 Barite 
                 2% 
               
               
                   
                 Muscovite 
                 11% 
               
               
                   
                   
               
             
          
         
       
     
         [0000]    
       
         
               
             
               
               
               
             
               
               
               
             
           
               
                 TABLE 4 
               
             
             
               
                   
               
               
                 Slurry composition, Case 2 
               
             
          
           
               
                   
                 Slurry Components (Dry) 
                 Wt % 
               
               
                   
                   
               
             
          
           
               
                   
                 Quartz 
                 61% 
               
               
                   
                 Dolomite 
                 18% 
               
               
                   
                 Calcite 
                 3% 
               
               
                   
                 CaS0 4 •H 2 0 
                 8% 
               
               
                   
                 Barite 
                 8% 
               
               
                   
                 Muscovite 
                 −1% 
               
               
                   
                   
               
             
          
         
       
     
         [0038]    In Examples 17-27, gold ore was added to the slurry described in Table 3 (Case 1) to obtain slurries having a gold ore (solids) content of 10% by weight. The slurries containing gold ore were placed in the jars as described above and the type and amount of scale inhibiting composition was added. The jars were then placed in the IKA shaker bath and processed as described above for Examples 1-16. Two control jars were also processed. After processing scale inhibition was measured using ICP analysis as described above and the results are set forth in Table 5. 
         [0000]    
       
         
               
             
               
               
               
               
             
               
               
               
               
             
           
               
                 TABLE 5 
               
             
             
               
                   
               
               
                 Threshold inhibition data for scale inhibiting products in mimic water with 
               
               
                 10 wt % gold ore slurry, Case 1. 
               
             
          
           
               
                 Example# 
                 Product Amount* 
                 Product Type 
                 % Inhibition ICP 
               
               
                   
               
             
          
           
               
                 17 
                 25 ppm in water 
                 Polystabil AN (Batch 
                 75 
               
               
                 18 
                 25 ppm in water 
                 Baypure 
                 53 
               
               
                 19 
                 25 ppm in water 
                 Mayoquest 1635 
                 36 
               
               
                 20 
                 25 ppm in water 
                 Polystabil AN (Batch 
                 33 
               
               
                 21 
                 25 ppm in water 
                 Dequest 2066 
                 19 
               
               
                 22 
                 25 ppm in water 
                 Drew 11-664 
                 16 
               
               
                 23 
                 25 ppm in water 
                 Cublen 45 
                 14 
               
               
                 24 
                 25 ppm in water 
                 Degapas 1105N 
                 11 
               
               
                 25 
                 25 ppm in water 
                 Polystabil ANA 
                 7 
               
               
                 26 
                 25 ppm in water 
                 Polystabil VZK 
                 6 
               
               
                 27 
                 25 ppm in water 
                 Polystabil AN 
                 3 
               
               
                   
               
               
                 *In Table 5, product amount is expressed in ppm (parts per million or mg/L) of active ingredient per aqueous phase in mimic water, containing 10 wt % gold ore slurry. Soluble Ca ion was measured by ICP. 
               
             
          
         
       
     
         [0039]    Polyacrylate, polyaspartate and organic phosphonate, HDTMPA, acid salts showed good efficacy, while tested at half a dose level compared to mimic water conditions (Examples 1-16). The presence of suspended slurry unexpectedly enhanced inhibition. 
       Examples 28-44 
       [0040]    In Examples 28-44, gold ore was added to the aqueous mimic water with the ore composition described in Table 4 (Case 2) to obtain slurries having gold ore (solids) content of 10% by weight and 15% by weight. The slurries containing gold ore were placed in jars described above and the type and amount of scale inhibiting composition was added. The jars were then placed in the IKA shaker bath and processed as described above for Examples 1-16. Two control jars were also processed. After processing, scale inhibition was measured using ICP analysis as described above and the results are set forth in Table 6. 
         [0000]    
       
         
               
             
               
               
               
               
             
               
               
               
               
             
           
               
                 TABLE 6 
               
             
             
               
                   
               
               
                 Threshold inhibition data for scale inhibiting products in mimic water with 
               
               
                 10 wt % and 15 wt % (high solids) gold ore slurry, Case 2 
               
             
          
           
               
                 Example# 
                 Product Amount* 
                 Product Type 
                 % Inhibition ICP 
               
               
                   
               
             
          
           
               
                 28 
                 50 ppm in water 
                 Polystabil AN (Batch 16763) 
                 49 
               
               
                 29 
                 50 ppm in water (high solids) 
                 Polystabil AN (Batch 16763) 
                 45 
               
               
                 30 
                 50 ppm in water 
                 Baypure 
                 55 
               
               
                 31 
                 50 ppm in water (high solids) 
                 Baypure 
                 37 
               
               
                 32 
                 50 ppm in water 
                 Mayoquest 1635 
                 62 
               
               
                 33 
                 50 ppm in water (high solids) 
                 Mayoquest 1635 
                 16 
               
               
                 34 
                 50 ppm in water 
                 Polystabil AN (Batch 16764) 
                 45 
               
               
                 35 
                 S0 ppm in water 
                 Dequest 2066 
                 27 
               
               
                 36 
                 50 ppm in water 
                 Drew 11-664 
                 8 
               
               
                 37 
                 50 ppm in water 
                 Cublen 45 
                 21 
               
               
                 38 
                 50 ppm in water (high solids) 
                 Cublen 45 
                 3 
               
               
                 39 
                 50 ppm in water 
                 Degapas 1105N 
                 47 
               
               
                 40 
                 50 ppm in water 
                 Polystabil ANA 
                 4 
               
               
                 41 
                 50 ppm in water 
                 Polystabil VZK 
                 58 
               
               
                 42 
                 50 ppm in water (high solids) 
                 Polystabil VZK 
                 35 
               
               
                 43 
                 50 ppm in water 
                 Polystabil AN 
                 45 
               
               
                 44 
                 50 ppm in water (high solids) 
                 Polystabil AN 
                 27 
               
               
                   
               
               
                 *Where product amount is expressed 1n ppm (parts per million or mg/L) of active ingredient per aqueous phase in mimic water, containing either 1Owt % or 15 wt % gold ore slurry. Soluble Ca ion was measured by ICP. Note that (high solids) are slurries having 15% by weight gold ore (solids) content, others without any notation as to solids have 10% by weight gold ore (solids) content. 
               
             
          
         
       
     
         [0041]    Polyacrylate, organic phosphonate and polyaspartate show good inhibition performance. Organic phosphonate and polyaspartate performance decreases with the increase in the solids content, while polyacrylate product retains essentially the same inhibition performance as in the prior examples (17-27). This indicates that slurry type, composition and amount have an impact on scale inhibition.