POLYMERIC ADDITIVES FOR WATER

Abstract: An admixture suitable for use in inhibiting scale and corro­ sion in aqueous system comprises a water-soluble polymer, preferably having a weight average molecular weight of less than 25,000, as determined by low angle laser light scattering, and comprising an unsaturated carboxylic acid and an unsaturated sulfonic acid, or their salts, the weight ratio of carboxylic to sulfonic acid being in the range 1:20 to 20:1, and at least one water soluble polycarboxylate, phosphonate, phosphate, polyphosphate, metal salt or sulfonates. Also in accordance with the invention, the formation of insoluble alluvial, metal oxide and metal hydroxide deposits in an aqueous system is inhibited by adding to the system at least 0.1 mg/l of a water-soluble polymer, preferably having a weight average molecular weight of less than 25,000, as determined by low angle laser light scattering, comprising an unsaturated carb­ oxylic acid and an unsaturated sulfonic acid, or their salts, the weight ratio of carboxylic to sulfonic acid being in the range 1:20 to 20:1, and a phosphonate.

Description: POLYMERIC ADDITIVES FOR WATER This invention relates to polymeric additives for water. Most industrial waters contain alkaline-earth metal cations, such as those of calcium, barium and magnesium, and several anions such as bicarbonate, carbonate, sulfate, oxalate, phosphate, silicate and fluoride. When combinations of these anions and cations are present in concentrations that exceed the solubility of their reaction products, precipitates form until these concentrations are no longer exceeded. For example, when the concentrations of calcium ion and carbonate ion exceed the solubility of calcium carbonate, a solid phase of calcium carbonate will form. Such concentrations are exceeded for various reasons, such as partial evaporation of the aqueous phase, changes in pH, pressure and/or temperature, and the introduction of additional ions that form insoluble compounds with the ions already present in the solution. As these reaction products are precipitated on the surfaces of the watercarrying system, they form scale or deposits, accumulation of which prevents effective heat transfer, interferes with fluid flow, facilitates corrosive processes, and harbors bacteria. Scale is an expensive problem in many industrial water systems and causes delays and shutdowns for cleaning and removal. Scale-forming compounds can be prevented from precipitating by inactivating their cations with chelating or sequestering agents, so that the solubility of their reaction products is not exceeded. Generally, this requires as much chelating or sequestering agent as cation, since chelation is a stoichiometric reaction, and these amounts are not always desirable or economical. Almost fifty years ago, it was discovered that certain inorganic polyphosphates would prevent such precipitation when added in amounts far less than the concentrations needed for sequestering or chelating. By "polyphosphates" is meant phosphates having a molar ratio of metal oxide to P205 in the range 1:1 to 2:1. When a precipitation inhibitor is present in a potentially scaleforming system at a markedly lower concentration than that required for sequestering (stoichiometric) the scale-forming cation, it is said to be present in "threshold" amounts. See for example, Hatch and Rice, "Industrial Engineering Chemistry", Vol. 31, pages 51 to 53 (3an. 1939); Reitemeier and Buehrer, 1,3ournal of Physical Chemistry", Vol. 44, No. 5, pages 535 to 536 (May 1940); and U.S. Patents Nos. US-A-2,358,222 and US A-2,539,305. Generally, sequestering takes place when the weight of the threshold active compound is greater than that of the scale-forming cation components. Threshold inhibition generally takes place at a weight ratio of threshold active compound to scale-forming cation components of less than 0.5:1.0. Certain water-soluble polymers, including groups derived from acrylamide and acrylic acid,have been used to condition wate?containing scale-forming compounds, for example, see U.S. Patents US-A-2,783,200; 3,514,476; 2,980,610; 3,285,886; 3,463,730 and 3,518,204. U.S. Patent US-A-3,928,196 discloses the use of a copolymer of 2acrylamido-2-methylpropylsulfonic acid and acrylic acid in inhibiting scale. The present invention is based on the discovery that an admixture of a water-soluble polymer comprising a carboxylic acid and a sulfonic acid, or their salts, including the copolymer of U S. Patent 3,928,196, in combination with a water-soluble polycarboxylate, phosphonate, phosphate, polyphosphate, metal salt and/or sulfonate, has a greater effect than would be expected from the sum of their separate effects, i.e. is synergistic. The present invention provides an admixture comprising: (a) a water-soluble polymer, preferably having a weight average molecular weight of less than 25,000, as determined by low-angle laser light scattering and comprising at least one unsaturated monocarboxylic acid and at least one unsaturated sulfonic acid or salt of such an acid, the sulfonic acid(s) being 2-acrylamido-2 methylpropyl sulfonic acid, 2-methacrylamido-2-methylpropyl sulfonic acid, styrene sulfonic acid, vinyl sulfonic acid, sulfoalkyl acrylate, sulfoalkyl methacrylate, allyl sulfonic acid, methallyl sulfonic acid, 3-methacrylamido-2-hydroxy-propyl sulfonic acid, and/or sulfonic acid acrylate, and the weight ratio of carboxylic to sulfonic acid being in the range 1:20 to 20: :1, and (b) at least one water-soluble polycarboxylate, phosphonate, organic phosphate, organic polyphosphate, metal salt and/or sulfonate. Also in accordance with the present invention, a method of inhibiting the corrosion of metal in an aqueous system comprises adding to the system at least 0.1 mg/l of such an admixture. Also in accordance with the invention, a method of inhibiting the precipitation of scale-forming salts in an aqueous system comprises adding to the system at least 0.1 mgll of such an admixture in which the unsaturated monocarboxylic acid is one or more of acrylic acid, methacrylic acid, c*-halo acrylic acid, maleic acid or anhydride, itaconic acid or anhydride, vinyl acetic acid, ally1 acetic acid, fumaric acid and/or & carboxyethyl acrylate, and/or a salt of any such acid. The invention also provides a method of inhibiting the formation of insoluble alluvial, metal oxide and metal hydroxide deposits in an aqueous system, comprising adding to the system at least 0.1 mg/l of a water-soluble polymer having a weight average molecular weight of less than 25,0Q0, as determined by low-angle laser light scattering, comprising at least one unsaturated carboxylic acid or salt and at least one unsaturated sulfonic acid or salt in a weight ratio of 1:20 to 20:1, together with a phosphonate. The phrase 11inhibiting the precipitation" includes threshold inhibition, dispersion, solubilization, and particle size reduction. The phrase "scale-forming salts includes any of the scale-forming salts, including, but not limited to, calcium carbonate, calcium sulfate, calcium phosphate, calcium phosphonate (including calcium hydroxyethylidene diphosphonic acid), calcium oxalate, calcium fluoride, barium sulfate and magnesium salts. The phrase "aqueous system" includes any system containing water; including, but not limited to, water in cooling systems, boilers, desalination plants, gas scrubbers, blast furnaces, sewage sludge thermal conditioning equipment, reverse osmosis apparatus, sugar evaporators, paper processing, and mining circuits. The carboxylic acid/sulfonic acid polymer was also found to be effective in inhibiting insoluble alluvial deposition, metal oxide and metal hydroxide deposition, especially in combination with a phosphonate. Alluvial deposits include silts; clays; and particulate material extracted from the air, such as dust. Deposits of any metal oxide or metal hydroxide, e.g. iron oxide, chromous oxide, or zinc hydroxide, may be inhibited. Any unsaturated carboxylic acid or its salt may be used to prepare the polymer (a). Examples are given above. The preferred carboxylic acids are acrylic acid and methacrylic acid. Any unsaturated sulfonic acid or its salt may be used in producing the polymer (a). Examples are given above. The preferred sulfonic acid is 2acrylamido-2-methylpropylsulfonic acid. Polymer (a) may be prepared from more than two monomers. Monomers other than carboxylic and sulfonic acids or their salts may be present in the polymer. Mixtures of the polymers may be used. The weight ratio of carboxylic acid to sulfonic acid is 1:20 to 20:1, preferably 1:10 to 10:1, and particularly 4:1 to 1:4. Any water-soluble polycarboxylate may be used as component (b). Examples include polymers derived from homo- andtor copolymers (including terpolymers, tetra-, etc.) of acrylic acid, methacrylic acid, vinyl acetic acid, allyl acetic acid, fumaric acid, phosphinocarboxylic acid, maleic acid or anhydride, itaconic acid, a-halo acrylic acid and ss-carboxyethyl acrylate. Any water-soluble phosphonate may be used as component (b). Examples include 2-phosphono-l , 2, 4-tricarboxybutane, amino tri (methylene phosphonic acid), hydroxyethylidene diphosphonic acid, phosphonosuccinic acid, benzene phosphonic acid, 2-aminoethyl phosphonic acid, polyamino phosphonates and the like. Additional phosphonates are identified in U.S. Patent 3,837,803, which is hereby incorporated by reference. The preferred phosphonates are 2-phosphono-l , 2, 4-tricarboxybutane, amino tri(methylene phosphonic acid) and hydroxyetbylidene diphosphonic acid. Any water-soluble phosphate may be used as component (b). Examples include orthophosphate; condensed phosphates, such as sodium hexametaphosphate; phosphate esters; organophosphate esters, such as the lower alkyl mono-, di- and trialkyl phosphates. The alkyl group is selected from C1 to C4 and may be branched or unbranched. The alkyl group may be substituted with hydroxy, amino, halide, sulfate or sulfonate, alone or in combination; and molecularly dehydrated phosphates. Any water-soluble metal salt may be used as component (b). Examples include water-soluble salts of zinc, molybdenum, chromate and sodium silicate and mixtures thereof. The combination of zinc and chromate were found especially effective. The polymer stabilizes the zinc ion and prevents its precipitation at high pH. Any water-soluble sulfonate-containing polymer may be used as component (b). Examples include homo- and/or copolymers of 2-acrylamido-2-methylpropylsul fonic acid, 2-methacrylamido-2-methylpropylsùlfonic acid, styrene sulfonic acid, vinyl sulfonic acid, sulfo alkyl acrylate or methacrylate, allyl or methallyl sulfonic acid, sulfonic acid acrylate, 3-methacrylamido-2-hydroxy propyl sulfonic acid, their salts and mixtures thereof. It is possible that the carboxylic acid, from which the polycarboxylate used as component (b) is prepared, is the same carboxylic acid used to prepare the polymer of component (a). However, the carboxylic acid used to prepare component (b) is not polymerized with the same sulfonic acid as (a). The same is true with regards to the sulfonate. The weight ratio of component (a) to component (b) is preferably 1:50 to 50:1, more preferably 1:10 to 10:1. It is preferred that component (a) be a copolymer. The carboxylic acid/sulfonic acid polymer was found, in addition, to enhance the effectiveness of the water-soluble polycarboxylates, phosphonates, polyphosphates, phosphates, metal salts and sul fonates. Calcium phosphate scale is a particular problem at a pH of 7 to 9. The admixtures of the instant invention were surprisingly found to be effective at a pH 7 to 9 and at temperatures ranging from 0 to 80 C. The admixtures of the instant invention are, of course, effective over a broad pH range (e.g. less than 7 and to some extent, greater than 9). The admixture is used at a minimum dosage of 0.1 mg/l in inhibiting scale and corrosion, preferably in a dosage of 1 to 100 mg/l, most preferably 1 to 15 mg/l. It is preferred that component (a) have a weight average molecular weight of less than 25,000, preferably less than 15,000, most preferably less than 10,000, as determined by low angle laser light scattering. The admixture was found to be synergistic in that the admixture inhibited scale and corrosion to a greater extent than expected. Examples The following abbreviations and product names are used in the Examples and are defined as indicated: AA/AMPS = copolymer of acrylic acid and 2-acrylamido-2-methylpropyl sulfonic acid having a weight average molecular weight of about 8200, as determined by low angle laser light scattering. CL361S = an aqueous solution of alkyl phenoxy poly(ethyleneoxy) ethanols and propylene oxide terminated ethylene oxide adduct, available from Calgon Corporation. PMA = polymaleic acid, MWT = 1300, as determined by light scattering, 70 percent active. HEDP = hydroxyethylidene diphosphonic acid. PBS-AM = 2-phosphono-l ,2,4-tricarboxybutane, manufactured by Mobay Chemical Corporation. Natrol 42 = a solution of a 60/40 copolymer of acrylic acid and 2-hydroxypropyl acrylate, manufactured by National Starch Corporation. Belclene 500 = phosphinocarboxylic acid, manufactured by Ciba Geigy. Versa TL-3 = copolymer of maleic anhydride and sulfonated styrene, manufactured by National Starch Corporation. Versa TL-70 = sulfonated polystyrene, manufactured by National Starch Corporation. PAA = polyacrylic acid, MWT 47Q0, as determined by light scattering. PolyAMPS = polyacrylamido methyl propyl sulfonic acid. AMP = amino tri(methylene phosphonic acid). Zn ++ = zinc ion added as zinc dissolved in hydrochloric acid. The concentration reported is solely zinc ion. CrO4-2 = chromate ion added as potassium dichromate. The concentration reported is solely chromate ion. P-35 = copolymer of 40 percent acrylamide and 60 percent acrylate, MWT 7500, manufactured by American Cyanamid. PolyDMDAAC = polydimethyldiallyl ammonium chloride, MWT 130,000, as determined by light scattering. MoO4-2 = molybdate ion added as sodium molybdate. The concentration reported is solely molybdate ion. PO4 = phosphate ion added as potassium dihydrogen phosphate. The concentration reported is solely phosphate ion. AA/AS = copolymer of acrylic acid and allyl sulfonic acid. Examples 1 through 65: Synergism between copolymers of carboxylic acids and sulfonic acids and other building blocks were screened for threshold inhibition of calcium carbonate, calcium sulfate and calcium phosphate. Stagnant flask tests were used with solutions stored for 24 hours at constant temperature. The standard test conditions used were as follows: Calcium Calcium Calcium Carbonate Sulfate Phosphate Calcium, mg/l 200 2000 200 Bicarbonate, mg/l 600 Sulfate, mg/l --- 4800 Phosphate, mg/l --- ---- 4 pH 8.0-8.2 7.0 8.5 Temperature, C 65 65 60 Four flasks were used for each test; one for a control (no inhibitor), one with the copolymer alone, one with the other inhibitor alone, and the last with both inhibitors. For all inhibitors, a level of inhibitor was picked which by itself would give 0 to 50 percent inhibition as determined by the following equation: 5T - 5c Percent Inhibition = ¯¯¯¯¯¯¯ x 100 where: Si - 5c SI = level of test species initially; Sc - level of test species at end of control test; and 5T = level of test species at end of inhibitor test. Calcium was used as the test species in the calcium carbonate and calcium sulfate tests, and phosphate was the test species in the calcium phosphate test. Synergism was determined by comparing the percent inhibition obtained using both inhibitors, each at the same level as used alone, with the sum of the inhibition obtained using the inhibitors alone. The results are summarized in Tables I, II and III. Examples 66 through 85: Synergism data on the inhibition of iron oxide deposition by a combination of the copolymer and other building blocks was determined by zeta potential measurements. The test solution consisted of 500 mg/i iron oxide (foe203) and O.O1M sodium nitrate (for ionic strength) at pH 7.1 to 7.2. Caustic was used to adjust the pH. The test solutions were treated with 1.0 mg/l of the copolymer and the various building blocks, alone or with a combination of 0.5 mg/l of the copolymer of and 0.5 mg/l of the other building block. The pH of the test solution was readjusted to 7.1 to 7.2, if necessary. The change in zeta potential of the control (without inhibitor) with the inhibited solutions was determined. Synergism was noted when that change was greater in the solutions treated by the combination of building blocks than with the building blocks alone. The results are summarized in Table IV. Examples 86 through 104: The synergistic effects of the AA/AMPS copolymer and other building blocks for corrosion inhibition were determined in eight liter test cells using synthetic four-cycle Pittsburgh water at pH 7.5. The tests were run for 7 days at a constant temperature of 50 C. Two steel test coupons (1 inch x 2 inches) were suspended on glass rods in each test cell. The test solution was constantly agitated by a submersible pump and air was constantly bubbled through the solution to keep it saturated. The various test solutions were treated with the AA/AMPS copolymer and the other building blocks, alone or with a combination of the copolymer and another building block. Synergism was determined by comparing the corrosion rates obtained on the test coupons from the cells containing the individual inhibitors with those from the cell containing the combination of inhibitors. The results are summarized in Table V. Example 105: The effect of the AA/AMPS copolymer in inhibiting the precipitation of calcium HEDP (hydroxyethylidene diphosphonic acid, a common scale inhibitor) precipitation was tested using synthetic four-cycle Pittsburgh water at pH 8.5. The tests were run for the number of days indicated at a constant temperature of 50 C. Thirty mg/l of HEDP was added. Fifty-three percent of the HEDP remained in solution in the absence of the copolymer. The turbidity was also measured and found to be 9 NTU. Ninety percent remained in solution when 15 mg/l, active, of a 60/40 AA/AMPS copolymer was added and the turbidity was 1.5 NTU. The effect of the 60/40 AA/AMPS copolymer in preventing calcium HEDP precipitation in industrial water was tested at pH 8.5 at a constant temperature of 50 C. The results are summarized in Table VI. Example 106: Forty grams of zinc ion were added to 8 liters of Pittsburgh tap water which had been concentrated 4 times. Ten experiments were run, five without additive and five with 10 mg/l of 60/40 AA/AMPS. The temperature of the test solutions was maintained at 50 C. The pH of the five solutins without additive was 7.0, 7.5, 8.0, 8.5 and 9.0, respectively. The pH of the five additive-containing solutions was likewise 7.0, 7.5, 8.0, 8.5 and 9.0, respectively. Samples were taken after one and three days from each of the solutions. The samples were filtered and the zinc ion concentration determined by atomic adsorption spectrometry. The results are summarized in Table VII. Both solutions at pH 9 contained 0.25 mg/l AMP to prevent any CaCO3 precipitation and interference at the high pH with the zinc data. Example 107: 3.1 grams of CrO3 in 500 ml of distilled water was reduced to Cr+3 with 25 ml of NaHSO3. The pH was adjusted to 11 and the solution was stirred for 45 minutes. 20 ml of the mixture was added to 180 ml of Pittsburgh tap water which had been concentrated 4 times. The solution was split in two samples. 15 mg/l of active of 60/40 AA/AMPS was added to one of the samples. The two samples were shaken. In the sample without the additive, the precipitate settled after 5 minutes, while the sample containing the additive retained a blue turbidity and precipitate took much longer to settle. The effect was quantified using a Brinkmann colorimeter at 450 nm. The sample with no additive had a 69.1 percent change in transmittance after 7 minutes, while the sample with additive had only a 3.7 percent change in transmittance. Example 108: The change in percent transmittance of iron oxide-containing BOF water and various dispersants was determined using the fiber optics probe from a Brinkmann PC/l000 colorimeter. The percent dispersant effectiveness was calculated from the following: A % transmittance with dispersant 100 1 A * transmittance without dispersant The iron oxide-containing BOF water was an industrial steel water sample characterized as follows: : Total Dissolved Ion (mg/l) (mg/l) C03 24 HCO3 > 968 C1- 110 SiO2 1.5 SOz 200 Orthophosphate 40.05 Polyphospha te < 0.1 Organic Phosphate < 0.1 Fluoride 32 Iron 855 < 0.05 Calcium 560 19 Magnesium 152 34 Suspended Solids 3500 3.5E The percent dispersion effectiveness of various concentrations of additive to disperse iron oxide in BOF scrubber water at a pH of 8.8 is summarized in Table VIII. Example 109 (Polyphosphate Stabilization): The ability of 60/40 AA/AMPS to stabilize polyphosphate (hexametaphosphate) was determined by measuring the reversion of polyphosphate to orthophosphate. 250 mg/l HCO3 was added to 8 liters of water characterized as follows: Ion mg/l Ca++ 400 Mg++ 48 SOW 788 Cl 708 HCO-3 250 which had been concentrated 4 times. The pH was 8.5 and the temperature was 50 C. After 7 days, using 10 mg/l hexametaphosphate (9.0 mg/l PO4), there was 0.433 mug/1 total PO4 still in solution. After 7 days, using 10 mg/l hexametaphosphate and 10 mg/l 60/40 AA/AMPS, there was 8.95 mg/l total P04 still in solution. TABLE I CaCO3 Inhibition 200 mg/l Ca++, 600 mg/l HCO3, pH 8.0-8.2, 60 C, 24 Hours Concen- Concen tration Percent tration Percent Percent Percent Actual Component (mg/l Inhibi- Component (mg/l inhibi- Expected Actual Expected Example A active) tion B active) tion A + B A + B (Percent) Ortho 1 60/40 AA/AMPS 0.5 34 Phosphate 2.0 34 68 55 +27 Ortho 2 20/80 AA/AMPS 0.5 5 Phosphate 2.0 28 33 60 +27 3 60/40 AA/AMPS 0.5 34 CL-361S 10.0 0 34 46 +12 4 60/40 AA/AMPS 0.5 34 MA 0.1 12 46 52 +6 5 60/40 AA/AMPS 0.5 34 @ElP 0.05 23 57 60 +3 Ortho 6 80/20 AA/AMPS 0.5 70 Phosphate 2.0 28 98 98 0 7 60/40 AA/AMPS 0.5 34 PR8-AM 0.2 20 54 52 -2 8 60/40 AA/AMPS 0.5 34 Matrol 42 0.5 34 68 66 -2 9 60/40 AA/AMPS 0.5 34 Lalclene 500 0.25 39 73 68 -5 10 60/40 AA/AMPS 0.5 34 Verme IL-70 5.0 16 50 42 -8 11 60/40 AA/AMPS 0.5 34 Poly AMPS 10.0 3 38 25 -13 12 60/40 AA/AMPS 0.5 34 MA 0.5 52 82 65 -17 Sodium Hexa 13 60/40 AA/AMPS 0.5 34 meta Phosphate 0.2 37 71 52 -19 14 60/40 AA/AMPS 0.5 34 Verme IL-3 10.0 37 71 50 -21 15 60/40 AA/AMPS 0.5 34 AMP 0.1 30 64 42 -22 16 60/40 AA/AMPS 0.5 34 P35 LO 68 102 69 -33 17 60/40 AA/AMPS 0.5 34 Poly IMDAAC 15.0 28 62 14 -48 Ortho 18 70/30 AA/AS 1.0 62 Phosphate 2.0 28 90 77 -13 TABLE II CaSO4 Inhibition 2000 mg/l Ca++, 4800 mg/l SO4ê, pH 7.0 65 C, 24 Hours Concen- Concentration Percent tration Percent Percent Percent Actual Component (mg/l Inhibi- Component (mg/l inhibi- Expected Actual Expected Example A active) tion B active) tion A + B A + B (Percent) 19 60/40 AA/AMPS 1.0 16.7 AMP 1.0 5.3 22.0 45.6 +23.6 20 60/40 AA/AMPS 1.0 16.7 RHA 1.0 47.4 64.1 85.1 +21.0 21 60/40 AA/AMPS 1.0 16.7 PMS-AM 1.0 5.3 22.0 36.8 +24.8 22 60/40 AA/AMPS 1.0 16.7 Balcleme 500 1.0 8.8 25.5 38.6 +23.1 23 60/40 AA/AMPS 1.0 16.7 DIA 0.5 10.5 27.2 36.0 +6.8 24 60/40 AA/AMPS 1.0 16.7 HEDP 1.0 4.4 21.1 26.3 +5.2 25 20/80 AA/AMPS 1.5 7.0 AMP 1.0 2.0 9.0 13.0 +4.0 26 60/40 AA/AMPS 1.0 11.0 F-35 2.0 16.0 27.0 31.0 +4.0 27 60/40 AA/AMPS 1.0 16.7 Metrol 42 0.5 8.8 2S.5 28.9 +3.4 28 20/80 AA/AMPS 1.5 7.0 FMA 1.0 18.0 25.0 27.0 +2.0 29 80/20 AA/AMPS 1.5 25.0 AMP 1.0 2.0 27.0 28.0 +1.0 <RTI ID=21.3> Ortho 30 60/40 AA/AMPS 1.0 16.7 Phosphate 1.0 4.4 21.1 21.1 0 Sodium Hexa 31 60/40 AA/AMPS 1.0 16.7 meta Phosphate 1.0 3.5 20.2 20.2 0 32 60/40 Aa/MS 1.0 16.7 CL-361 1.0 3.5 20.2 19.3 -0.9 33 60/40 AA/AMPS 1.0 16.7 Verme IL-70 1.0 7.0 23.7 21.1 -2.6 34 60/40 AWMs 1.0 16.7 Verme IL-3 1.0 5.3 22.0 19.3 2.7 35 60/40 AA/AMPS 1.0 11.0 Poly AMPS 4.0 5.0 16.0 13.0 -3.0 36 60/40 AA/AMPS 1.5 25.0 EMI 1.0 18.0 43.0 36.0 -7.0 37 60/40 AA/AMPS 1.0 16.7 Poly INDAAC 1.0 5.3 22.0 8.8 -13.2 38 Verne IL-3 50.0 28 AMP 2.0 42 70 31 -39 39 70/30 AA/AE 2.0 14 AMP 2.0 42 56 100 t44 40 70/30 AA/AS 2.0 14 PMA 1.0 18 32 46 +14 @@@ the CuSO3 inhibition curve is very steep, experimental variance in quite large. TABLE III Ca/SO4 Inhibition 200 mg/l Ca++, 4 mg/l NH4 , pH 8.5, 60 C, 24 Hours Concen- Concen tration Percent tration Percent Percent Percent Actual Component (mg/l Inhibi- Component (mg/l inhibi- Expected Actual Expected Example A active) tion B active) tion A + B A + B (Percent) 41 60/40 AA/AMPS 1.5 20 Verme IL-3 4.0 20 40 97 +57 42 60/40 AA/AMPS 1.5 20 Verme IL-70 10.0 36 56 100 +44 43 60/40 AA/AMPS L5 23 BA 1.5 30 53 95 442 44 60/40 AA/AMPS 1.5 16 F-85 5.0 31 47 81 +34 45 80/20 AA/AMPS 1.5 6 PMA 1.5 13 19 45 +25 46 80/20 AA/AMPS 1.5 6 Verme IL-8 4.0 57 63 86 +23 47 60/40 AA/AMPS 1.5 23 MA 1.5 30 53 75 +22 48 60/40 AA/AMPS 1.5 23 Natrol 42 3.0 54 77 95 +18 49 60/40 AA/AMPS 1.5 23 Balcleme 500 5.0 44 67 76 +9 50 20/80 AA/AMPS 1.5 18 Verme IL-3 4.0 57 75 77 +2 51 60/40 AA/AMPS 1.5 14 Poly INDAAC 1.5 5 19 19 0 52 20/80 AA/AMPS L5 18 EMA L5 13 31 31 0 53 60/40 AA/AMPS 1.5 20 Poly AMPS 10.0 34 54 50 -4 54 60/40 AA/AMPS 1.5 26 CL-361 10.0 5 31 22 -9 Dioctyl Sulfin 55 60/40 AA/AMPS 1.5 26 Succinate 10.0 5 31 13 -18 56 60/40 AA/AMPS 1.5 23 AMP 1.5 26 51 27 -24 57 60/40 AA/AMPS 1.5 14 PRG-AM 1.5 29 43 18 -25 Sodium Hexa 58 60/40 AA/AMPS 1.5 23 meta Phosphate 1.5 20 43 15 -28 59 60/40 AA/AMPS 1.5 23 HEDP 1.5 30 53 19 -24 60 Verme IL-3 5.0 19 Verme IL-70 10 39 58 63 +5 61 70/30 AA/AS 5.0 20 Verme IL-70 10 39 59 20 -39 62 Verme IL-3 5.0 19 PAA 1.5 20 39 19 -20 63 70/30 AA/AS 5.0 20 PAA 1.5 20 40 30 -10 64 Verme IL-3 5.0 19 P-35 5.0 24 43 86 +43 65 70/30 AA/AS 5.0 20 P-35 5.0 24 44 72 +28 "The AA/AMPS CaPO4 inhibition was tested each time a comparison test was conducted. The testing was conducted over a several-week period. Since the CaPO4 inhibition curve is very steep, experimental variance is quite large. TABLE IV Fe2O3 500mg/l Fe2O3, .01M MnNO3, pH 7.10-7.16 A+B # Teta # Zeta #Zeta Component Potential Component Potential Potential Exemple A (mv)ê B (mv) (mv) Synergisme 66 60/40 AA/AMPS 30 PRG-AM 31 37 x 67 60/40 AA/AMPS 30 MHDF 32 34 x 68 60/40 AA/AMPS 50 AMPS 48 49 69 60/40 AA/AMPS 50 F-35 49 50 70 60/40 A/AMPS 50 Metrol 42 54 47 71 60/40 AA/AMPS 50 Balclene 500 49 47 72 60/40 AA/AMPS 30 BAA 24 28 Dioctyl Sulfio 73 60/40 AA/AMPS 50 Succinate 5 45 74 60/40 AA/AMPS 30 BA 30 26 75 60/40 AA/AMPS 50 CL-361S 1 44 76 60/40 AA/AMPS 30 (50) Verme IL-70 28 (40) Sodium Hexa 77 60/40 AA/AMPS 50 meta Phosphate 41 40 78 60/40 AA/AMPS 50 FO34 30 42 79 60/40 AA/AMPS 50 Verme IL-3 49 39 80 60/40 AA/AMPS 30 AMP 26 23 81 60/40 AA/AMPS 50 INDAAC 26 30 82 Verme IL-8 23 FB8-AM 26 35 x 83 70/30 AA/AS 22 FB8-AM 26 51 x 84 Verme IL-3 23 HEDP 26 60 x 85 70/30 AA/AS 22 HEDP 26 24 *The AA/AMPS # zeta potential for Fe2O3 shifted during the experimenta tion. The zeta potential for AA/AMPS was measured for each exemple. Aging of iron oxide is believed to be the somme of the zeta potential drift. TABLE V Steel Corrosion Exhibition 4 Cycle Pittsburgh Water, 50 C, pH 7.5, 7 Days Concen- Corro- Concen- Corro tration sion tration sion Corrosion Rate Component (mg/l Rate Component (mg/l Rate (spy) Example A active) spy B active) spy A + B Synergisme 86 Blank Blank 74.0 87 60/40 AA/AMPS 20 49.0 Zn++ 10 23.9 31.5 88 60/40 AA/AMPS 75 20.1 Zn++ 10 23.9 12.9 x 89 60/40 AA/AMPS 10 35.6 AMP 10 12.9 24.4 x 90 60/40 AA/AMPS 75 20.1 AMP 10 12.9 5.0 x 91 60/40 AA/AMPS 10 55.6 HEDP 10 25.9 23.9 x 92 60/40 AA/AMPS 75 20.1 HEDP 10 25.9 6.0 x Sodium Hexa 93 60/40 AA/AMPS 10 35.6 meta Phosphate 10 19.4 22.6 Sodium Hexa 94 60/40 AA/AMPS 75 20.1 meta Phosphate 10 19.4 5.8 x 95 60/40 AA/AMPS 75 20.1 KF34 10 3.6 2.7 x 96 60/40 AA/AMPS 75 20.1 CnO4-ê 25 0.5 2.0 97 60/40 AA/AMPS 75 20.1 FNG-AM 10 41.5 6.9 x 98 60/40 AA/AMPS 75 20.1 MnO24 25 62.4 8.4 x 30 mg/l B 99 60/40 AA/AMPS 100 8.7 Metrol 42 100 8.0 15.4 100 60/40 AA/AMPS 100 8.7 PMA 100 28.9 27.2 101 60/40 AA/AMPS 100 8.7 PMA 100 10.1 7.1 x 35/10/55 AA/ 102 60/40 AA/AMPS 100 8.7 INDAAC/AM 100 67.0 38.5 103 60/40 AA/AMPS 100 8.7 Balclame 500 100 27.6 28.2 104 60/40 AA/AMPS 100 8.7 PolyINDAAC 100 43.5 49.0 TABLE VI Calcium Phosphate Inhibition - Industrial WaterÚ Initial Final Condition NIU PO- 4 Level PO- 4 Level Comments No Additive 10 11 5 After 7 Days 3 mg/1 EHDP/ 10 mg/l IRC-233 30 34 4 After 7 Days (3 FO4, 1 HEDP) 30 MG/l HEDP/ 50 mg/l IRC-233 1.5 41 40 After 5 Days (17.5 FO4, 22HEDP) Turbidity remained constant for at least three weeks Ú 310 mg/l calcium ion, 76 mg/l magnesium ion, 960 mg/l chlorides, 4800 mg/l sulfate ion, 30 mg/l nitrate ion, 60 mg/l silice, 11 mg/l orthophosphate. TABLE VII Initial Zinc Concentration 5 mg/l in 4 Cycle Pittsburgh Water1; 50 C Zinc Concentration (mg/l) Zinc Concentration (mg/l) with Without Additive 10 gm/l 60/60 AA/AMPSCopolymer ------------------------- ----------------------------- pH Day 1 Day 3 Day 1 Day 3 ----- ----- ----- ------ ----- 7.0 4.1 4.5 4.5 4.8 7.5 3.8 4.4 4.8 5.42 8.0 0.90 0.65 4.6 4.7 8.5 0.30 0.25 4.5 4.9 9.0 0.25 0.30 4.6 4.6 188 mg/l Ca++, 24 mg/l Mg++, 328 mg/l SO@4, 70 mg/l Cl-, 40 mg/l HOO3-1. @Values alightly elevated above 5 mg/l dur to a concentrating effect due to solution evaporation. TABLE VII Active Percent Concentration Disperment Additiveness (mg/l) Effectiveness 60/40 AA/AMPS 4 80 60/40 AA/AMPS 8 90 60/40 AA/AMPS 12 100 60/40 AA/AMPS and HEDP 1 74 60/40 AA/AMPS and HEDP 2 96 60/40 AA/AMPS and HEDP 3 100

Claims: CLAIMS 1. An admixture comprising (a) a water-soluble polymer comprising at least one unsaturated monocarboxylic acid and at least one unsaturated sulfonic acid or salt of such an acid, the sulfonic -acid(s) being 2-acrylamido-2 methylpropyl sulfonic acid, 2-methacrylamido-2-methylpropyl sulfonic acid, styrene sulfonic acid, vinyl sulfonic acid, sulfoalkyl acrylate, sulfoalkyl methacrylate, allyl sulfonic acid, methallyl sulfonic acid, 3-methacrylamido-2-hydroxy-propyl sulfonic acid, and/or sulfonic acid acrylate, and the weight ratio of carboxylic to sulfonic acid being in the range 1:20 to 20:1, and (b) at least one water-soluble polycarboxylate, phosphonate, organic phosphate, organic polyphosphate, metal salt and/or sulfonate. 2. An admixture as claimed in Claim - 1, in which polymer (a) has a weight average molecular weight of less than 25,000, as determined by low angle laser light scattering, and the unsaturated mono-carboxylic acid is one or more of acrylic acid, methacrylic acid, halo acrylic acid, vinyl acetic acid, allyl acetic acid, Scarboxyethyl acrylate, and their salts. 3. An admixture as claimed in Claim 1 or 2, in which component (b) is one or more of polyacrylic acid, hydroxyethylidene diphosphonic acid, amino tri(methylene phosphonic acid), polymaleic acid or anhydride, zinc chloride, sodium polystyrene sulfonate, a copolymer of maleic anhdride and sulfonated styrene, or a copolymer of acrylamide and acrylate. 4. A method of inhibiting the precipitation of scale-forming salts in an aqueous system, comprising adding to the system at least 0.1 mg/l of an admixture as claimed in Claim 1, in which the unsaturated carboxylic acid is one or more of acrylic acid, methacrylic acid, a-halo acrylic acid, maleic acid or anhydride, itaconic acid or anhydride, vinyl acetic acid, allyl acetic acid, fumaric acid, Scarboxyethyl acrylate, and their salts. 5. A method as claimed in Claim 4, in which polymer (a) has a weight average molecular weight of less than 25,000, as determined by low-angle laser light scattering. 6. A method as claimed in Claim 4 or 5, in which component (b) is one or more of polyacrylic acid, hydroxyethylidene diphosphonic acid, phosphinocarboxylic acid, amino tri(methylene phosphonic acid), polymaleic anhydride, zinc chloride, sodium orthophosphate, sodium polystyrene sulfonate, a copolymer or maleic anhydride and sulfonated styrene, a copolymer of acrylamide and acrylate, and mixtures thereof. 7. A method of inhibiting the corrosion of the metal in an aqueous system, comprising adding to the system at least 0.1 mg/l of an admixture as claimed in Claim 1. 8. A method as claimed in Claim 7, in which polymer (a) has a weight average molecular weight of less than 25,000, as determined by low angle laser light scattering, the carboxylic acid is acrylic acid and/or methacrylic acid and the sulfonic acid is one or more of 2-acrylamido-2-methylpropyl sulfonic acid, alkyl sulfonic acids and their salts. 9. A method of inhibiting the formation of insoluble alluvial metal oxide and metal hyroxide deposits in an aqueous system, comprising adding to the system at least 0.1 mg/l of a water-soluble polymer comprising an unsaturated carboxylic acid and an unsaturated sulfonic acid, or their salts, weight ratio of carboxylic to sulfonic acid being in the range 1:20 to 20:1, and at least one phosphonate. 10. A method as claimed in Claim 9, in which the polymer (a) has a weight average molecular weight of less than 25,000, as determined by lowangle laser light scattering, the metal oxide or hydroxide is zinc oxide and/or chromous oxide or zinc hydroxide, and the phosphonate is one or more of hydroxyethylidene diphosphonic acid, amino tri(methylene phosphonic acid), a carboxyl phosphonate, and mixtures thereof.

Inventors: BOFFARDI, BENNETT P., PERSINSKI, LEONARD J., WALKER, JERRY L.
Applicants: CALGON CORPORATION
Application year: 1984
Main classification: C02F5
IPC codes: C23F11, C02F5, F02B75