Simultaneous use of water soluble polymers with ozone in cooling water systems

Abstract: Certain water soluble polymers in the presence of ozone are acceptable for scale control, corrosion control, microbiological control and the like because the effectiveness of these polymers is not substantially negated by ozone. The preferred polymers are homopolymers and copolymers containing at least 50 mole percent of acrylic acid or methacrylic acid or mixtures thereof. Certain other monomers may be used with the acrylic acid and methacrylic acid monomers, and still function as scale inhibitors and corrosion inhibitors in the presence of ozone in industrial waters. The industrial waters are particularly recirculating cooling waters.

Description: The use of ozone in cooling waters, particularly recirculating cooling waters has been recently touted as a way of controlling microbiological growth in these recirculating waters, and is also now being touted as a sole treatment including possible inhibition of corrosion and for scale inhibition. Normally, certain additives are added to cooling waters, particularly those cooling waters that have characteristics that might lead to hardness precipitates such as calcium and/or magnesium carbonate precipitates, to prevent these precipitates from accumulating and depositing on heat transfer surfaces, fouling these surfaces and contributing to lost energy efficiency in the process. Because ozone is such a strong oxidizing agent, there are many references to its reacting with organic materials, including these agents purposefully added as scale inhibitors, to degrade these organics. The presumption is that such degradation would eliminate any scale inhibiting characteristics that might be present when scale inhibitor chemicals are being used. Examples of prior art include a teaching by Ikemizu, et. al., Chemical Engineer Commun., 34(1-6), 77-85, 1985, wherein water soluble polymers are stated to be degraded by ozone and that the degradation rate is defined by change in the weight average molecular weight per unit time. Ikemizu teaches that the rate of degradation for poly(oxyethylenes) was proportional to 1.5 to 2.0 powers of the molecular weight and was 20 to 60 times higher than the rate of degradation of poly(acrylamides). He taught that the degradation rate of poly(sodium acrylate) was proportional to the 2.0 power of the molecular weight. Hanasaki, in Kankyo Gijutsu, 13(11), 817-20, (1984), taught that poly(acrylamide) was ozonized to remove it from waste waters. His observations indicated that chain severing occurred in a random fashion and that ozonation produced a carbonyl(aldehyde), carboxylate functionalities and ketone groups. Although he states that the amide groups in poly(acrylamide) were not themselves attacked by ozone, these teachings and others, such as Imamura, et. al., in the Journal of Applied Polymer Science, 25(6), 997-1005, (1980), taught destruction of polymers and UV light acceleration of ozonation of water soluble polymers, particularly polyethylene glycol, polyacrylamide, and poly(vinyl alcohol). In general, chain cleavage of polymers was observed in the presence of ozone, and this was accelerated in the presence of UV irradiation. Various products were observed in the ozonation reaction including formaldehyde and the presence in oligomers of ketones, carboxylic acids, terminal aldehydes, and the like. (See for example Suzuki, et. al., Journal Applied Polymer Science, 24(4), 999-1006, (1979). Numerous authors have determined that ozonation causes polymer degradation in aqueous solutions containing various water soluble polymers. It would have appeared then from these various treatments appearing in the prior art that water soluble polymers traditionally used to maintain calcium and other hardness components in solution in recirculating cooling waters would suffer in the presence of ozone. Ozone would be expected to degrade these polymers to the point where their usefulness would no longer exist for the purpose of maintaining calcium carbonate in solution or suspension and preventing scale formation on heat transfer surfaces in contact with the waters containing hardness. It is, therefore an object of this invention to select certain polymeric organic water soluble polymers, which are found to retain and maintain their ability to keep hardness precipitates in solution or in suspension in recirculating waters even in the presence of ozone, and to provide a method of treating recirculating cooling waters (especially those containing certain degrees of calcium/magnesium hardness, certain "M" alkalinities and operating in certain pH ranges) with both ozone and organic vinylic polymers having the capability in the presence of ozone to retain and maintain their calcium carbonate saturation ratio indicating that they are still useful for scale inhibition in these industrial cooling waters. The method of determination of which polymers are suitable involves exposing polymers having initial molecular weights ranging from about 1,500 to 40,000 and initial calcium carbonate saturation ratios ("CCSR") of at least 80, preferably at least 90, and most peferably at least 100, to 0.01 ppm to 2.5 ppm ozone for at least 30 minutes at a temperature within the range 8° to 60°C, measuring the CCSR after exposure, and selecting as suitable those polymers which retain at least 70 percent, and preferably at least 80 percent, of the initial calcium carbonate saturation ratios. This maintenance of their ability to maintain calcium carbonate at saturation levels or above is in Spite of the fact that these polymers are, in fact, undergoing molecular weight degradation apparently via ozonation reactions. Particularly preferred are those polymers that contain at least 50 mole percent (meth)acrylic acid or water soluble salts thereof, which have initial calcium carbonate saturation ratios of at least 90, and which after said exposure for 90 minutes, have the at least 70 percent of the initial CCSR measured for the polymer. The preferred organic water soluble vinylic polymers are those polymers that contain at least 50 mole percent (meth)acrylic acid, preferably at least 60 mole percent (meth)acrylic acid, and most preferably, from 70 to 100 mole percent (meth)acrylic acid, or as water soluble salts thereof. These preferred polymers also have an initial or original calcium carbonate saturation ratio of at least 90, preferably at least 100, and most preferably at least 110. The molecular weights are a weight average molecular weight as determined by aqueous gel permeation chromotography using a polystyrene sulfonate set of standard polymers. All of the molecular weights reported in this specification were determined by gel permeation chromatography (GPC) using the same polystyrene sulfonate standard sets. By the term (meth)acrylic acid or its salts, we mean to include exclusively acrylic acid monomer, exclusively methacrylic acid monomer, or any admixture of acrylic acid and methacrylic acid monomers, whether present as the free acid or partially neutralized salt or completely neutralized salt of these free acids. To form the salts, any common base alkali metal or alkaline earth metal ammonia, low molecular amine, or low molecular quaternary salt hydroxides, may be used. For the most part, the (meth)acrylic acid polymers are formed by polymerizing the monomers, acrylic acid methacrylic acid, or mixtures thereof, or salts thereof, and the. polymers may be either partially or completely neutralized, as in the sodium, potassium, ammonium or mixtures thereof salt forms. Other salt forms, either completely or partially neutralized, however, are incorporated and included within the concepts of this invention. Preferably, these organic water soluble vinylic polymers contain at least 60 mole percent (meth)acrylic acid, and can also contain at least one of the following comonomers chosen from the group consisting of (meth)acrylamide, maleic anhydride, N-methylsulfonic acid-(meth)acrylamide, (hereafter AMS), N-ethylsulfonic acid-(meth)acrylamide, (hereafter AES), vinyl sulfonic acid, itaconic acid, C 1 - C 3 esters of acrylic acid especially the isopropyl ester, hydroxypropyl acrylate, N-t-butyl acrylamide, vinyl acetate, vinyl ethers, acrylamidomethylpropane sulfonic acid (AMPS), and other similar vinylic monomers, which are successfully polymerised with acrylic acid, methacrylic acid, or mixtures thereof. In general, the term (meth) followed by a monomer identity is meant to include that monomer, the methylated monomer, and mixtures thereof, as earlier explained for (meth)acrylic acid. By the term "salts", when referring to our polymers, we mean any completely or partially neutralized salt form of the polymer which is water soluble, primarily amd preferably the sodium, potassium salts, or mixtures thereof. In general, the preferred sulfonated monomers useful in forming a copolymer are illustrated by the formula: where: R is H, CH 3 , or mixtures thereof; R' is a linear or branched alkylene group containing from 1 - 4 carbon atoms; and M is H, alkali metal, alkaline earth metal, protonated amine, ammonium, or quaternary ammonium, or mixtures thereof. Our invention also involves a method of treating recirculating cooling waters comprising adding thereto in effective amounts to inhibit microbiological growth and inorganic scale formation on heat transfer surfaces in contact with said cooling waters, of both ozone and organic water soluble vinylic polymers, which polymers have been determined is suitable by to performance of the above method as a preliminary step. In the practice of this method, the ozone is maintained at a concentration of at least 0.01 parts per million residual ozone in the recirculating waters, and the ozone is added at a sufficient rate to maintain this residual concentration of ozone. Also, the polymer, which may have an initial weight average molecular weight of from 1500-35,000, is added at a concentration and rate that would be sufficient to maintain at least 2ppm active polymer in the cooling waters treated. An initial active polymer concentration ranging from at least two and preferably, from 5 to 100 parts per million polymer, based on cooling water treated is normally achievable. As the waters to be treated are ozonated, it is most preferable to maintain these cooling waters at an ozone residual concentration of at least 0.05 ppm, based on the treated cooling waters, and to add polymers at rates sufficient to obtain an initial active polymer concentration of at least two parts per million, and preferably from 5 to 100 parts per million, and most preferably from 5 to 50 parts per million of the active polymer being added to the cooling waters. Mixtures of polymers may also be used when advantageous, and when mixtures are used, the total polymer weight concentration should be as above. The Cooling Waters The waters for the cooling systems being treated with both ozone and polymers can have characteristics such as the following: Parameters Range pH 6.5 - 9.7 Ca Hardness 20 - 2000ppm (as CaCO 3 ) Mg Hardness 10 - 1000ppm (as CaCO 3 ) Total Hardness 30 - 3000ppm (as CaCO 3 ) SiO 2 0.10 - 125ppm (as SiO 2 ) "M" alkalinity 20 - 2500ppm (as CaCO 3 ) Temperature 10°C. - 60°C. Although the initial concentrations of each element listed above in waters being treated are those within the lower limits of the ranges above, these limitations can increase when the waters are concentrated in a cooling water application, often from a factor ranging from about 2 up to as high 60 or above, and can lead to waters in the recirculation systems and blowdown system having concentration limits considerably higher than the upper limits listed above. Normally the recirculating cooling waters are treated with ozone from any useful ozone generator, and there are many available in the art, and the ozone is added to the recirculating waters at a concentration sufficient to maintain in the recirculating cooling waters, a residual ozone level of at least 0.01 parts per million based on the treated cooling waters, and preferably at least 0.05 parts per million ozone, or above. The polymers of primary interest in this invention are those polymers, which can withstand ozonation at concentrations of ozone up to nearing ozone saturation, such that ozone levels can range from at least 0.01 ppm up to concentrations, e.g. of approximately 2.0 - 2.5 parts per million ozone in water. Even with these exposures to ozone, the selected polymers maintain at least 70%, preferably at least 80%, of their initial calcium carbonate saturation ratio. The molecular weight of these homopolymers and copolymers normally range initially from 1500 to 40,000 although, as before, this molecular weight is degraded in contact with ozone. Preferably, the polymers have an initial molecular weight of from 2,000-15,000. In spite of this molecular weight degradation, the preferred polymeric polymers retain ozonated or oligomeric components after ozone is reacted with these copolymers which ozonated components maintains at least 70 percent and preferably 80 percent of the initial calcium carbonate saturation ratio of the starting copolymer. The Calcium Carbonate Saturation Ratio (CCSR) The calcium carbonate saturation test is completed as follows. A test solution is prepared by adding the chloride or sulfate salts of calcium and magnesium,. the polymeric inhibitor, and a solution of sodium bicarbonate to deionized water. Initial concentrations of these salts should be adjusted to achieve 360 parts per million calcium, 200 parts per million magnesium, 500 parts per million bicarbonate (as calcium carbonate), and 15 parts per million of the polymeric inhibitor on an active solids polymer basis. This inhibited hardness/bicarbonate solution was then ozonated at ambient temperatures for a total ozonation time of 90 minutes. During the first 60 minutes of ozonation, an ozone level less than 1 part per million ozone residual was maintained. During the final 30 minutes of ozonation, the level of residual ozone was increased so as to maintain approximately 1.0 to 2.3 parts per million ozone. During the test times, alkalinity, pH, and ozone residuals were monitored at set time intervals. Water samples from these test containers were collected at 0, 30, 60 and 90 minutes of ozonation, and tested for calcium carbonate inhibition activity via the calcium carbonate saturation ratio test, or CCSR test. This CCSR test involves the following: The collected solutions are placed in a hot water bath at temperatures maintained at 67.5°C (140° F). The solution is stirred at all times and pH is continuously monitored. The sample is titrated with dilute sodium hydroxide (0.1 molar) at a constant rate of addition. As the dilute sodium hydroxide solution is added, the pH of the test solutions slowly increases, then decreases slightly, and then increases again. The maximum pH prior to the slight decrease is referred to as the "breakpoint pH". A mineral solubility computer program is then used to calculate the calcium carbonate supersaturation ratio defined below based on test conditions at the breakpoint pH. This supersaturation ratio is related to the calcium carbonate inhibition performance or the calcium carbonate saturation ratio. The test procedure was repeated for different inhibitor solutions. The method for calculating CCSR is outlined by Johnson, et. al., International Water Conference, October, 1980* , which reference is incorporated herein by reference. The test procedure is also taught in Fong, et al, US-A-4,919,821. Preferably, when completing multiple tests, all precipitated calcium carbonate should be removed from test apparatus containers prior to the next test. This inhibits nucleation, which would foul the test results. The theory behind the above test is dependent on the formation of scale above a particular critical pH. Consequently, sodium hydroxide is added to the test solution to increase the pH and to supersaturate the test water until the breakpoint.pH is reached. Nucleation and crystal growth occur at this point. The measured break point pH is then used in a computer program based on mineral solubility prediction models to calculate a value called the saturation ratio. The saturation ratio is simply an index for predicting the formation of calcium carbonate and the computer program saturation ratio compensates for temperature, high ionic strength, ion paring effects, and the like. Other important factors included in the mineral solubility analysis are water composition, operating conditions, temperatures, break point pH, cycles of concentration, and acid control. A calcium carbonate saturation ratio is theoretically equal to the product of the concentration of calcium times the concentration of carbonate ions divided by the solubility product constant for calcium carbonate The higher the CCSR, the better the polymer will be as a scale inhibitor. Polymer Maintenance of Calcium Carbonate Saturation Ratios The homopolymers and copolymers found most useful in our invention are those polymers that initially contain a calcium carbonate saturation ratio (CCSR) of at least 90 preferably at least 100, and most preferably at least 110. Initial calcium carbonate saturation ratios can be as high 120 - 140. Typical initial calcium carbonate saturation values range from about 110 to about 135, and in some cases slightly higher. The homopolymers of acrylic acid normally have initial calcium carbonate saturation ratios ranging between about 110 and 137.5. The copolymers normally have initial calcium carbonate saturation ratios of at least 90, preferably at least 100, and most preferably from about 110 to about 135. These polymers are added to representative test cooling waters and ozonated for at least 30 and preferably 90 minutes. During the initial 60 minutes, the ozone level is maintained at concentrations ranging from about 0.01 to about 0.8 parts per million and during the last 30 minutes, the ozone residual is raised by increasing the rate of addition of ozone to these waters so that the residual is from about 1.0 to about 2.3 parts per million. The ozonation tests are run at temperatures ranging from ambient, about 18° C, to 60° C for a period of up to about 90 minutes as described. The last 30 minutes of the test is at temperatures of about 40-60° C. After the ozonation reaction has taken place, the molecular weight degradation is observed in all cases. Sometimes, the degree of molecular weight degradation relates to the initial molecular weight of the polymer added. However, even though these molecular weight degradations can range anywhere from as little as about 25 percent to as much as 85 percent of the original molecular weight, the calcium carbonate saturation ratio for those polymers that are successfully used in our invention is maintained at about 70 percent of the initial value, preferably 80 percent of the initial value or higher. In some cases, ozonation actually increases the calcium carbonate saturation ratio. If a polymer does not maintain at least 70 percent of its initial calcium carbonate saturation ratio, and more preferably at least 80% of its initial CCSR value, the polymer is not believed to be useful in combination with ozone in treating cooling waters. To further describe our invention the following tables are presented. These tables list certain polymers in terms of their chemical nature, molecular weight, initial and ozonated calcium carbonate saturation ratios, and give such other data as would be of interest. All of these tests were run in beakers and/or containers, which provide test results equivalent to those results expected in actual field use in recirculating cooling waters. SUMMARY OF CALCIUM CARBONATE SATURATION RATIO SCREENING TEST DATA Activity After Ozonation CCSR Inhibitor (15 ppm) Before Ozonation After Ozonation Hach Test ppm Ozone Residual Polymer A 136.9 ± 6.6 124.8 ± 6.6 2.3 ppm + Polymer B (first batch) 133.9 ± 6.6 138.8 ± 6.6 0.8 - 1.0 ppm Polymer B (second batch) 119.9 ± 6.6 110.6 ± 6.6 1.2 - 2.3 ppm + Polymer C 131.9 ± 6.6 128.9 ± 6.6 1.2 -2.3 ppm + Polymer D 113.7 ± 6.6 128.9 ± 6.6 1.0 - 1.8 ppm Polymer E 28.6 ± 6.6 80.0 ± 6.6 2.3 ppm + Polymer F 97.1 ± 6.6 103.3 ± 6.6 2.3 ppm + Polymer G 97.1 ± 6.6 97.1 ± 6.6 1.3 - 2.3 ppm + Polymer H 107.5 ± 6.6 85.4 ± 6.6 1.4 ppm Polymer I 125.9 ± 6.6 97.1 ± 6.6 1.2 ppm Polymer J 85.4 ± 6.6 69.9 ± 6.6 1.8 - 2.3 ppm + Polymer L 107.5 ± 6.6 113.7 ± 6.6 2.3 ppm + Polymer M 131.9 ± 6.6 131.9 ± 6.6 2.3 ppm + Phosphonates (Comparative) PBTC 145.9 ± 6.6 sample precipitated HEDP 137.7 ± 6.6 sample precipitated Blank 3.0 ± 6.6 sample precipitated In Table 1, you can see the results of adding various polymers to cooling waters and then ozonating these mixtures for a period of 90 minutes, as described above. After this ozonation, the calcium carbonate saturation ratio is measured. The results in Table 1 show that those polymers which are preferred, are the polymers that retain at least 70 and more preferably at least 80 percent of their initial calcium carbonate saturation ratio. In some cases after ozonation the ozonated saturation ratio is higher than the initial calcium carbonate saturation ratio. Also in Table 1, you can see that several organic phosphonates were tested. These materials have traditionally been used in treating cooling waters for hardness control and under ozonation conditions fail miserably. Blanks were also run to give the observer reasonable basis and background for the test results. Summary of Average Molecular Weight and Molecular Number Results for Ozonated Polymers Inhibitor Before Ozonation After Ozonation Polymer K Mw: 39,700 Mw: 2,400 Mn: 18,600 Mn: 2,000 Polymer B Mw: 4,400 Mw: 2,600 Mn: 3,500 Mn: 2,100 Polymer A Mw: 5,000 Mw: 2,500 Mn: 3,000 Mn: 2,000 Table II, is a summary of the average molecular weight and molecular number results obtained for ozonated polymers. Certain polymers were tested before and after ozonation, and their molecular weights determined again by GPC chromatography. As can be seen, when molecular weight is relatively high, the degree of degradation observed after ozonation is also high, when a molecular weight starts relatively low the degree of degradation of molecular weight is less, but there seems to be a fairly consistent molecular weight measured for all polymers irrespective of the initial molecular weight of these polymers. However, this data is limited, and we cannot limit the invention in terms of the ozonated final molecular weight. POLYMER COMPOSITIONS Polymer A: Polyacrylic acid homopolymer neutralized with NaOH, Mw: 5,000 Polymer B: Isopropyl ester of acrylic acid (low ester content), Mw: 5,000 (two different batches were used) Polymer C: Water soluble acrylic acid polymer, Mw: 5,100 Polymer D: Water soluble acrylic acid polymer, Mw: 5,800 Polymer E: Water soluble acrylic acid polymer, Mw: 240,000 (Comparative) Polymer F: Methyl sulfonic acid acrylamide, 50-60% acrylic acid/ 14-20% aminomethanesulfonate /remainder acrylamide, Mw: 18,000-19,000 Polymer G: 70% acrylic acid / 30% acrylamide copolymer, Mw: 30,000 Polymer H: Hydrolyzed polymaleic anhydride, Mw: 1,000 (Comparative) Polymer I: Terpolymer of acrylic acid, methacrylic acid and itaconic acid, Mw: 1,000 (Comparative) Polymer J: Polymethacrylic acid, Mw: 25,000 - 30,000 Polymer K: Ethyl sulfonic acid acrylamide, ("AES") taurine derivative, Mw: 40,000 *Polymer L: 70-80 mole% acrylic acid/20-30 mole% hydroxypropylacrylate, Mw: 6,000-10,000 Polymer M: 65-75 mole% acrylic acid/25-35 mole% acrylamidomethylpropane sulfonic acid, Mw: 10,000-15,000 Table III describes polymers A through M in terms of their chemical structure and initial molecular weights. In Table III, the methylsulfonic acid, acrylamide polymers are those that contain from 50 to 60 mole percent acrylic acid, from 10 to 20 mole percent acrylamido, N-methyl sulfonates (AMS) and the remainder acrylamide. Polymer K also contains from 50 to 60 mole percent acrylic acid, from 10 to 30 percent N-ethylsulfonic acid acrylamide(AES); the remainder being acrylamide. The remainder of the Tables, up to Table XVIII, provides additional information specifically for each of the polymers listed. Again, these tests show the ability of the specified polymers to maintain their calcium carbonate saturation ratio, even after the contact with ozone for periods of time known to lead to polymer degradation in terms of weight average molecular weight. In spite of this polymer degradation, certain of these polymers still maintain their ability to inhibit calcium carbonate scale formation in the presence of ozone. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer A Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 136.9 ± 6.6 2.5% O3 output 30 minutes O 3 0.55 - 0.6 ppm 142.6 ± 6.6 60 minutes O 3 0.55 - 0.6 ppm 144.3 ± 6.6 25% O3 output 90 minutes O 3 2.3 ppm + 124.8 ± 6.6 Polymer A continued to behave as a calcium carbonate inhibitor after 60 minutes of ozonation. However, after 30 additional minutes of exposure to very high levels of ozone, there was a decrease in activity which is within experimental error. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer B (first batch) Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 133.9 ± 6.6 2.5% O3 output 30 minutes O 3 0.5 ppm 136.5 ± 6.6 60 minutes O 3 0.4 ppm 139.7 ± 6.6 15% O3 output 90 minutes O 3 0.8 - 0.9 ppm 138.8 ± 6.6 The saturation ratio values indicate that Polymer B is maintaning its calcium carbonate inhibition activity even at unrealistically high ozone levels. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer B (second batch) Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 119.9 ± 6.6 2.5% O3 output 30 minutes O 3 0.7 - 0.8 ppm 131.9 ± 6.6 60 minutes O 3 0.6 - 0.7 ppm 137.7 ± 6.6 15% O3 output 90 minutes O 3 1.2 ppm 110.6 ± 6.6 (113.7 recheck) These saturation ratio values indicate that Polymer B is increasing in activity for the first 60 minutes of low level ozonation, and then drops to approximately the same performance level as the initial unozonated sample. When comparing this run of the Polymer B sample to the results in table I, note that the unozonated sample has a lower saturation ratio value to begin with, and used a different batch sample. This sample also experienced ozone levels of 2.3 ppm and greater, at 75 minutes of ozonation, while the highest ozone reading recorded for table I was 1.0 ppm at 75 minutes of ozonation. The Mw is -2,100, after ozonation. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer C Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 131.9 ± 6.6 2.5% O3 output 30 minutes O 3 0.65 ppm 125.9 ± 6.6 60 minutes O 3 0.6 ppm 128.9 ± 6.6 15% O3 output 90 minutes O 3 1.2 ppm 128.9 ± 6.6 The saturation ratio values indicate that Polymer C is maintaining its calcium carbonate inhibition activity at high ozone levels. The Mw of this sample is -5,100 and overall, is a very good calcium carbonate inhibitor. Mw = Weight average molecular weight by GPC chromatography using polystyrene sulfonate standards. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer D Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 113.7 ± 6.6 2.5% O3 output 30 minutes O 3 0.65 ppm 125.9 ± 6.6 60 minutes O 3 0.65 ppm 134.8 ± 6.6 15% O3 output 90 minutes O 3 1.0 ppm 128.9 ± 6.6 The saturation ratio values indicate that Polymer D is actually improving in activity upon ozonation. The Mw of this polymer is initially -5,800. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer E Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 28.6 ± 6.6 2.5% O3 output 30 minutes O 3 0.4 - 0.5 ppm 52.6 ± 6.6 60 minutes O 3 0.3 ppm 65.2 ± 6.6 15% O3 output 90 minutes O 3 2.3 ppm+ 80.0 ± 6.6 The saturation ratio values indicate that Polymer E is maintaining its calcium carbonate inhibition activity at unrealistically high ozone levels. Note that it is also a poor CaCO 3 inhibitor to begin with (solution was slightly turbid prior to ozonation), and ozonation increases the sample's performance. This is most probably due to the high molecular weight of the initial polymer (Mw - 240,000). Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer F Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 97.1 ± 6.6 2.5% O3 output 30 minutes O 3 0.5 ppm 103.3 ± 6.6 60 minutes O 3 0.9 ppm 107.5 ± 6.6 25% O3 output 90 minutes O 3 2.3 ppm+ 103.3 ± 6.6 Though Polymer F is not a superior calcium carbonate inhibitor initially, it is still important since ozonation at extremely high levels does not decrease the sample's activity. Note that after a total of 90 minutes of ozonation, the saturation ratio is equivalent to the initial unozonated sample. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer G Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 97.1 ± 6.6 2.5% O3 output 30 minutes O 3 0.10 ppm 113.7 ± 6.6 60 minutes O 3 0.70 ppm 122.9 ± 6.6 15% O3 output 90 minutes O 3 -2.0-2.3 ppm+ 97.1 ± 6.6 Polymer G is a 70% acrylic acid / 30 % acrylamide polymer with a MW-30,000. The saturation ratio values from this experiment demonstrate that even after 90 minutes of ozonation (30 minutes at a high level), this polymer has the same level of performance as the initial sample. Overall however, this sample is not the best inhibitor of choice for a good calcium carbonate inhibitor. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer H Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 107.5 ± 6.6 2.5% O3 output 30 minutes O 3 0.3 ppm 122.9 ± 6.6 60 minutes O 3 0.45 ppm 107.5 ± 6.6 25% O3 output 90 minutes O 3 1.4 ppm 85.4 ± 6.6 This is an example of a polymer that maintained calcium carbonate inhibition activity for the initial 60 minutes of ozonation, but after an additional 30 minutes of high ozonation, lost activity. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer I Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 125.9 ± 6.6 2.5% O3 output 30 minutes O 3 0.4 - 0.5 ppm 116.8 ± 6.6 60 minutes O 3 0.4 - 0.5 ppm 116.8 ± 6.6 25% O3 output 90 minutes O 3 1.15 ppm 97.1 ± 6.6 Polymer I, a terpolymer of acrylic acid, methacrylic acid and itaconic acid, also lost calcium carbonate inhibition activity upon extended exposure to ozone. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer J Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 85.4 ± 6.6 2.5% O3 output 30 minutes O 3 0.8 ppm 80.0 ± 6.6 60 minutes O 3 0.5 ppm 85.4 ± 6.6 15% O3 output 90 minutes O 3 2.3+ ppm 69.9 ± 6.6 Polymer J is a polymethacrylic acid with a Mw -25,000 -30,000 and is not a very good calcium carbonate inhibitor. The saturation ratio values above, indicate that this sample maintains activity for the first 60 minutes of low level ozonation (<1.0 ppm), but when exposed to higher concentrations for an additional 30 minutes, it begins to lose acitivity. Although functional, this material would not be preferrred. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer L Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 107.5 ± 6.6 2.5% O3 output 30 minutes O 3 0.60 ppm 110.6 ± 6.6 60 minutes O 3 0.46 ppm 122.9 ± 6.6 15% O3 output 90 minutes O 3 1.23 ppm 113.7 ± 6.6 The saturation ratio values indicate that Polymer L, an acrylic acid / hydroxypropylacrylate copolymer does maintain calcium carbonate inhibition activity after ozonation. The activity of the sample before ozonation and after 90 minutes of low and high exposure to ozone are essentially equivalent. Benchtop Scale Inhibition Screening Test for Calcium Carbonate Inhibitor: Polymer M Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 131.9 ± 6.6 2.5% O3 output 30 minutes O 3 0.65 ppm 148.5 ± 6.6 60 minutes O 3 0.69 ppm 131.9 ± 6.6 15% O3 output 90 minutes O 3 1.39 ppm 131.9 ± 6.6 The saturation ratio values indicate that Polymer M a 70 M% acrylic acid / 30 M% AMPS copolymer, MW- 12,300, does maintain calcium carbonate inhibition activity after ozonation. The activity of the sample before ozonation and after 90 minutes of low and high exposure to ozone are essentially equivalent. In fact, the saturation ratios indicate that this sample is a very good calcium carbonate inhibitor. Ozonation of Phosphonates at 40 C (Comparative) Inhibitor % O3 Output O3 Level Comments Blank 12.5% -.25 ppm turbid after 15 min of O 3 PBTC 12.5% <0.1 ppm turbid after 30 min of O 3 HEDP 12.5% <0.1 ppm turbid after 15 min of O 3 Each of these phosphonates were ozonated in 360 ppm Ca, 200 ppm Mg, 500 ppm alkalinity (as CaCO 3 ) water at 40 C. As the comments above indicate, the test solution became turbid within 30 minutes of ozonation. This indicated that the critical breakpoint pH had passed and testing a cloudy solution for CaCO 3 inhibition would be meaningless. Additional tests by LC showed the destruction of the phosphonates. PBTC - 1,2,4-tri-carboxy-2-phosphono-butane HEDP - 1-hydroxyethylidine-1,1-diphosphonic acid Benchtop Scale Inhibition Screening Test for Calcium Carbonate (Comparative) Inhibitor: PBTC - 18-20° C (Ambient Temperature) Dosage:15 ppm inhibitor as actives Ozonation Time Ozone Level Saturation Ratio no ozone 0.0 ppm 143.2 ± 6.6 2.5% O3 output 30 minutes O 3 0.36 ppm 134.8 ± 6.6 60 minutes O 3 0.66 ppm 128.9 ± 6.6 15% O3 output 90 minutes O 3 0.98 ppm 80.0 ± 6.6 The saturation ratio values indicate that the phosphonate PBTC is not maintaining calcium carbonate inhibition activity after ozonation. The last sample collected after 90 minutes of ozonation was slightly turbid in the hot water bath (60 C), prior to the saturation ratio test. Note that before ozonation, PBTC is an excellent scale inhibitor, but then declines in activity with extended exposure to ozone. The selected polymers may also be used in inhibiting hardness scale formation on heat transfer surfaces in contact with ozonated cooling waters. Our methods include methods of treating ozonated cooling waters with polymers as described above where the polymer is added to the ozonated cooling waters to obtain an initial total polymer. concentration of at least 2ppm active polymer(s) and preferably, from about 5 to about 100 parts per million total active polymer based on treated waters and wherein the polymer is chosen from at least one polymer having the following characteristics:

Claims: A method of determining the suitability of a polymer for use together with ozone in the treatment of recirculating cooling waters wherein the ozone concentration in those waters is maintained at at least 0.01 ppm comprising exposing a soluble vinylic polymer to 0.1 ppm to 2.5 ppm ozone in water for at least 30 minutes at a temperature ranging from 18° to 60°C, the soluble vinylic polymer having an initial calcium carbonate saturation ratio ("CCSR") of at least 80 and containing at least 50 mol% (meth)acrylic acid or its salt and an initial weight average molecular weight ranging from 1500 to 40000, measuring the CCSR of the polymer after said exposure and determining as a result of that measurement that any said polymer retaining at least 70% of its original CCSR is suitable for the stated purpose. A method according to claim 1 wherein the polymer contains at least 60 percent (meth)acrylic acid. A method according to claim 1 or claim 2 wherein the organic water soluble vinylic polymer is a copolymer of (meth)acrylic acid, and its water soluble salts thereof, with at least one of the vinylic monomers chosen from the group consisting of (meth)acrylamide, maleic anhydride, N-methyl sulfonic acid-(meth)acrylamide, N-ethyl sulfonic acid-(meth)acrylamide, itaconic acid, C 1 - C 3 esters of acrylic acid, hydroxypropylacrylate, N-Type-butylacrylamide, acrylamido methyl propane sulfonic acid, and vinyl acetate. A method according to any one of the preceding claims wherein the copolymer is at least one polymer having the characteristics: A method according to claim 1 wherein the polymer is a homopolymer of acrylic acid having an initial molecular weight of from 2,000 - 10,000 and an initial calcium carbonate saturation ratio of at least 100. A method according to claim 1 wherein the ozone residual concentration is maintained at at least 0.05 ppm, and the polymer is a homopolymer of methacrylic acid having an initial molecular weight of from 2,000-25,000, and an initial calcium carbonate saturation ratio of at least 80. A method of treating recirculating cooling waters by use of both ozone and at least 2 ppm an organic water soluble vinylic polymer which includes the preliminary step of determining the suitability of the polymer for the treatment method by the determination method according to any one of claims 1 to 6.

Inventors: FULKS KENNETH E, KHAMBATTA BINAIFER S, YOUNG PAUL R, FULKS, KENNETH E., KHAMBATTA, BINAIFER S., YOUNG, PAUL R.
Applicants: NALCO CHEMICAL CO, NALCO CHEMICAL COMPANY
Application year: 1992
Main classification: C02F1
IPC codes: C02F5, C02F1, C02F9