Patent Application
20140190895
1. Field of the Invention
The present invention relates to the inhibition of scale formation in desalination plant feed brine, and particularly to calcium sulfate scale-inhibiting compositions that provide polyelectrolyte antiscalant compositions for inhibiting calcium sulfate scales and a method of using the same.
2. Description of the Related Art
Due to the needs for potable water in the developing world, there has been great interest in the development of antiscalants for controlling scaling in various industrial water treatment systems, such as desalination plants, cooling towers, boilers, oil wells, etc. Precipitation and scale deposition is a particular problem in reverse osmosis (RO) desalination plants and other water treatment installations. In the RO process, the dissolved salts in the feed water are concentrated as a reject brine stream due to the high salt rejection properties of membranes. If supersaturation occurs in the reject brine, and their solubility limits are exceeded, precipitation or scaling will occur.
Conventional scale inhibitors are generally referred to as “threshold agents”. Although generally effective, such conventional threshold agents are typically formed from organophosphates, polyacrylic acid, polymaleic acid, and hydrolyzed water-soluble copolymers of maleic anhydride. Newer antiscalants include polycarboxylates, phosphonates, phosphates, sulfonates and polyamides, along with the use of polyaspartic acids and their mixtures with surfactants and emulsifiers for inhibiting or delaying precipitation of scale forming compounds in membrane processes. These materials, however, are hazardous to humans and are very damaging to the environment. It would be desirable to be able to inhibit scale formation in the production of potable drinking water without the risk of harmful contamination, either to humans or the environment.
Thus, calcium sulfate scale-inhibiting compositions solving the aforementioned problems are desired.
The calcium sulfate scale-inhibiting compositions inhibit calcium sulfate scale formation in desalination plant feed brine, such as that typically used with reverse osmosis desalination plants. In order to inhibit the formation of calcium sulfate scales, the polyelectrolyte antiscalant compositions are mixed into the desalination plant feed brine at a concentration between about 1 ppm and about 50 ppm. The compositions are polyelectrolyte antiscalant compositions that may be either poly[disodium 3-(diallylamino)propanephosphonate]-alt-(sulfur dioxide), poly[sodium 5-(diallylcarboxymethylammonio)pentanoate]-alt-(sulfur dioxide), or poly[sodium 5-(diallylcarboxymethylammonio)pentanoate].
These and other features of the present invention will become readily apparent upon further review of the following specification and drawings.
Similar reference characters denote corresponding features consistently throughout the attached drawings.
Subsequently, 5.5 grams, or 14.6 mmol, of the CPE poly[diallyl-3-(diethylphosphonato)propylammonium chloride]-alt-(sulfur dioxide) was hydrolyzed in a solution of 6 M HCl at 90° C. for 48 hours. The homogeneous mixture was dialyzed against deionized water for 24 hours to produce the polyzwitterionic acid (PZA) poly[3-(diallylammonio)propanephosphonic acid]-alt-(sulfur dioxide) (at a 97% yield), which, upon treatment with two equivalents of NaOH (H2O), was converted into the dianionic polyelectrolyte (DAPE) poly[disodium 3-(diallylamino)propanephosphonate]-alt-(sulfur dioxide)]. Both the PZA and the resultant DAPE were characterized by elemental analysis, 1H, 13C, and 31P NMR and IR spectroscopy. It should be noted that the DAPE has only one phosphonate group, thus minimizing its relative weight % in the scale inhibitor composition.
Experimentally, the poly[disodium 3-(diallylamino)propanephosphonate]-alt-(sulfur dioxide) was evaluated as a calcium sulfate scale inhibitor by addition to and mixing with the feed water of a brackish water reverse osmosis (RO) desalination plant, the polyelectrolyte being added in small quantities between 1 ppm and 50 ppm. Two alternative related substances were also evaluated in the same experiment: poly[sodium 5-(diallylcarboxymethylammonio)pentanoate]-alt-(sulfur dioxide) and poly[sodium 5-(diallylcarboxymethylammonio)pentanoate], the structures of which are shown in
Table 1 below shows the composition of the brackish feed water and reject brine (corresponding to 70% recovery) used in the experimental evaluation.
The three antiscalant compositions poly[disodium 3-(diallylamino)propanephosphonate]-alt-(sulfur dioxide), poly[sodium 5-(diallylcarboxymethylammonio)pentanoate]-alt-(sulfur dioxide), and poly[sodium 5-(diallylcarboxymethylammonio)pentanoate] were evaluated using synthetically prepared supersaturated 3 CB brine. The concentration measurement “CB” is defined such that a 1 CB concentration corresponds to a reject brine concentration at recovery ratio of 70%, as tabulated in Table 1 for brackish water. A CaCl2 solution was prepared at six times the Ca2+ concentration in 1 CB solution (corresponding to 70% recovery in Table 1) and a Na2SO4 solution was prepared at six times the SO42− ion concentration in 1 CB solution.
About 60 ml of the 6 CB calcium chloride solution was taken in a two-neck round bottom flask and antiscalant was added at a dose level of 10 ppm. The solution was heated to 50° C. by placing the round bottom flask on a heating mantle equipped with a magnetic stirrer. About 60 ml of 6 CB concentration sodium sulfate solution was prepared in a small glass bottle fitted with a Teflon cap, and heated to a temperature of 50° C. When both solutions reached 50° C., they were mixed together via stirring at 200 rpm. The concentration of the final solution after mixing was 3 CB (a mixture of about 2600 mg/l as Ca2+ and 6300 as SO42−).
Conductivity measurements were made at an interval of every 10 seconds to quantify the effectiveness of the antiscalants. A drop in conductivity indicates the precipitation of CaSO4. Induction time was measured when precipitation started. The experiments were continued until equilibrium was reached. Visual inspection was carefully performed to see any turbidity arising from precipitation. The test conditions for evaluation of the three antiscalant additives are shown in Table 2 below.
A blank, or control, experiment was first performed without any additive in the solutions. The results of this blank experiment serve as a basis to compare the performance of the present antiscalant additives.
About 60 ml of the 6 CB calcium chloride solution was next taken in a two-neck round bottom flask and the antiscalant poly[disodium 3-(diallylamino)propanephosphonate]-alt-(sulfur dioxide), prepared as described above, was added at a dose level of 10 ppm. The solution was heated to 50° C. About 60 ml of 6 CB sodium sulfate solution was then prepared in a small glass bottle fitted with a Teflon cap and heated to 50° C. When both the solutions reached 50° C., they were mixed together via stirring at 200 rpm. The concentration of the final solution after mixing was 3 CB. Conductivity measurements were made at an interval of every 10 seconds to quantify the effectiveness of the antiscalant poly[disodium (diallylamino)propanephosphonate]-alt-(sulfur dioxide). A drop in conductivity indicates the precipitation of CaSO4. Induction time was measured when precipitation started, and the experiments were continued until equilibrium was reached. It was found that conductivity remained constant for more than 1800 minutes. The conductivity dropped from 17.35 mS/cm to 15.11 mS/cm, as shown in
Next, about 60 ml of the 6 CB calcium chloride solution was taken in a two-neck round bottom flask and the antiscalant poly[sodium 5-(diallylcarboxymethylammonio)pentanoate]-alt-(sulfur dioxide), prepared as described in M. M. Ali, H. P. Perzanowski, and S. A. Ali, “Polymerization of functionalized diallyl quaternary salt to poly(ampholyte-electrolyte)”, Polymer, 41, 5591-5600 (2000), was added at a dose level of 10 ppm. The experiment to evaluate the additive poly[sodium 5-(diallylcarboxymethylammonio)pentanoate]-alt-(sulfur dioxide) was carried out as in the previous experiment for the first antiscalant composition. The induction time was found to be 90 minutes. Equilibrium concentration was reached after 470 minutes and the conductivity dropped from 17.16 mS/cm to 14.5 mS/cm. The precipitation behavior of 3 CB supersaturated solution with respect to CaSO4 when poly[sodium 5-(diallylcarboxymethylammonio)pentanoate]-alt-(sulfur dioxide) was added is illustrated in
About 60 ml of the 6 CB calcium chloride solution was again taken in a two-neck round bottom flask and the third antiscalant poly[sodium 5-(diallylcarboxymethylammonio)pentanoate], prepared as described in M. M. Ali, H. P. Perzanowski, and S. A. Ali, “Polymerization of functionalized diallyl quaternary salt to poly(ampholyte-electrolyte)”, Polymer, 41, 5591-5600 (2000), was added at a dose level of 10 ppm. The experiment to evaluate the additive poly[sodium 5-(diallylcarboxymethylammonio)pentanoate] was carried out as in the previous two experimental evaluations. The induction time was found to be about 500 minutes. Equilibrium concentration was reached after 1400 minutes and the conductivity dropped from 17.30 mS/cm to 14.97 mS/cm. The precipitation behavior of 3 CB supersaturated solution with respect to CaSO4 when poly[sodium 5-(diallylcarboxymethylammonio)pentanoate] was added is illustrated in
The antiscalant poly[disodium 3-(diallylamino)propanephosphonate]-alt-(sulfur dioxide) composition was found to be comparable to conventional antiscalants. As a final control experiment, a conventional antiscalant was studied, and the conventional antiscalant, under similar experimental conditions, was found to produce an induction time of 1,880 minutes. The conductivity was measured at equilibrium. The conductivity dropped from 17.48 mS/cm to 14.92 mS/cm.
It is to be understood that the present invention is not limited to the embodiments described above, but encompasses any and all embodiments within the scope of the following claims.
