Polyampholytes and their use

Abstract: Polyampholytes and their salts are used as scale and corrosion inhibitors, in drilling fluids and as a water oil ratio modifier in enhanced oil recovery. Novel polyampholyte polymers of intrinsic viscosity 0.05 to 4.5 in 1 0 M Na Cl are prepared from 20 to 90 weight % of a monomer of formula: in which each R, which may be the same as or different from the other, is hydrogen, phenyl, C₁₋₃ alkyl or -COOX R¹ is a straight or branched chain of from 0 to 12 carbon atoms, and X is hydrogen or an alkali or alkaline-earth metal; 1.5 to 85 weight % of a monomer of formula: where each R⁶, which may be the same as or different from the other, is hydrogen, phenyl or C₁₋₃ alkyl, preferably hydrogen, methyl, or ethyl, and each R², which may be the same as or different from the other, is hydrogen or C₁₋₃ alkyl; and 0.5 to 40 weight weight % of a cationic-containing monomer containing quaternary ammonium, phosphonium or sulfonium ion.

Description: POLYAMPHOLYTES AND THEIR USES Polyampholytes are polymers containing both a cationic and an anionic mer unit, nonionic mer units optionally being present. Polyampholytes have found particular use as retention aids in the paper industry (see for example, U.S. Patents US-A-3,639,208 and US-A-4,171,417). There has also been some use of polyampholytes in the oil-drilling industry (see for example, published British Patent Application CB-A-2,044,32 I and U.S. Patent US-A-4,330,450). Scale deposits are incrustation coatings which may be formed from a wide variety of simple and complex inorganic salts that accumulate on the metallic surfaces of a water-carrying system through a number of different causes. Various industrial and commercial water-carrying systems are subject to scale-formation problems. Scale is of particular concern in heatexchange systems using water, for example, boiler systems and once-through and open recirculating water-cooling systems. Corrosion of metal in aqueous systems is usually caused by the presence of dissolved oxygen in the water. Currently available corrosion inhibitors include phosphorus-containing inorganic and organic compounds, zinc, chromates, polyacrylates, polyacrylamides, and polycarboxylates, such as polymaleic anhydride, and their adducts. Drilling fluids are used in the drilling of earth formations to tap subterranean deposits such as gas or oil. The drilling fluid serves to cool and lubricate the drill bits, -to carry the cuttings to the surface as the drilling fluid is circulated in and out of the well, to support at least part of the weight of the drill pipe and drill bit, to provide a hydrostatic pressure head to prevent caving of the walls of the well bore, to deposit on the surface of the well bore a filter cake which acts as a thin semi-impervious layer to prevent undue passage of fluids, and to perform other functions as are well known in the drilling art. It is important that the drilling fluid should exhibit a relatively low rate of filtration or fluid loss, and in addition that it should have desirable rheological properties such as viscosity and gel strength. it is also important that the drilling fluid system should be kept as simple and inexpensive as possible in order to avoid undue expense in the drilling of the well. Oil-producing formations are generally porous layers having varying degrees of permeability to the flow of fluids such as oil, water and gas. Consequently, the rate of oil production is largely determined by the rate of flow through these permeable formations which, in turn, is dependent upon the porosity or permeability of the sand or stone present. In drilling through such a porous layer, it is desirable to use a drilling fluid having characteristics that prevent excessive amounts of liquids or solids from penetrating through the porous formation. The ability of the drilling fluid to prevent excessive penetration of formation fluid is called filtration control. Acrylic and methacrylic derivatives, such as those that are copolymerized with hydrocarbon substituted styrenes, such as alpha methylstyrene, para-methylstyrene, and 2,4-dimethylstyrene have been utilized in drilling fluids, (see for example, U.S. Patents US-A-2,718,497 and US-A-2,650,905). Acrylic acid derivatives, such as copolymers of acrylamide and sodium acrylate derivatives, have been frequently used commercially as flocculants for drilling fluids, as is disclosed in U.S. Patents US-A-3,558,545 and US-A-3,472,325. Similarly, a copolymer derived from acrylic acid and acrylamide is disclosed in U.S. Patent US-A-3,323,603 as a flocculant for aqueous drilling fluids. Published British Patent Application GB-A-2,044,321 discloses a copolymer additive prepared from (1) a meth(acrylamido alkyl sulfonic acid) or alkali metal salt thereof and (2) a (meth)acrylamide or N-alkyl (meth)acrylamide. The copolymer may be crosslinked with a quaternary ammonium salt. In producing oil from both natural and artificial water driven oil reservoirs, the wells ultimately produce sufficiently large volumes of connate water to constitute a serious operating problem and eventually production of the water forces abandonment of the well. The cost of raising water to the Earth's surface and of separating it from the oil represents an economic loss and, in addition, in many instances, there is a problem in disposal of the waste water. Even more important, the total volume of fluid that can be produced daily is often limited by the well bore and artificial lift equipment so that water production unnecessarily reduces the oil production rate. In many instances, a portion of the reservoir is producing essentially all water, while the remainder is producing a substantial quantity of oil. If production from the watered-out portion of the reservoir is eliminated or reduced, the production, handling and disposal of large volumes of water is avoided. Certain polymers can reduce the water:oil production ratio so more oil is produced while handling less water This results in major savings in operating costs, the avoidance of unnecessary depletion of the water drive, and increased production from the remaining oil interval which results in greater ultimate recovery and greater current income. U.S. Patent US-A-4,330,450 is directed to amphoteric water-in-oil self-inverting polymer emulsions containing polymer having 1 to 35 parts by weight anionic monomer units in the polymer. The primary use disclosed is in paper making. Their use in secondary and tertiary oil recovery is suggested. However, polymers containing 1 to 35 parts by weight of anionic monomer units were found to be poor polymers to enhance oil recovery. The use of polyampholytes as scale and corrosion inhibitors appears unknown. The present invention provides a method of inhibiting corrosion and scale in an aqueous system comprising adding an effective amount of a polyampholyte or a salt thereof to the aqueous system. The polyampholyte is preferably a carboxylic functional polyampholyte. Also, in accordance with the invention there is provided an aqueous drilling fluid comprising an aqueous clay dispersion and a polyampholyte, preferably a carboxylic functional polyampholyte, or a salt thereof. Such an aqueous drilling fluid is, in accordance with the invention, used in a method for drilling a well in a subterranean formation comprising circulating into the well, during drilling, the said aqueous drilling fluid. The invention also provides a method of recovering oil andlor gas from a subterranean formation penetrated by a well bore and for reducing the concomitant production of reservoir water from it, comprising injecting into the formation through the well bore an aqueous treating solution or emulsion containing a polyampholyte, preferably a carboxylic or sulfonic functional polyampholyte, or a salt thereof. The invention also provides a carboxylic polyampholyte polymer, having an intrinsic viscosity of 0.05 to 4.5 in 1.0 M NaCI. While the method and compositions of the present invention have been found particularly useful in providing inhibition of calcium phosphate scales and silica polymerization, inhibition of magnesium hydroxide, calcium fluoride, calcium carbonate, calcium sulfate and other scales may also be obtained. The preferred anionic component is a carboxylic functional monomer. Any carboxylic functional monomer, or its salt, may be used. Examples include acrylic acid, crotonic acid, methacrylic acid, vinyl acetic acid, allylacetic acid, 4-methyl-4-pentenoic acid, and dicarboxylic acids such as maleic acid and itaconic acid. The preferred carboxylic functional monomers are acrylic acid and methacrylic acid. Mixtures of carboxylic functional monomers may be used in preparing the polyampholyte. Sulfonic functional polyampholytes are especially effective in enhanced oil recovery applications. Any cationic-containing monomer may be used. The preferred cationic-containing monomers are: EMI7.1 where R3is hydrogen, phenyl, or C1 3 alkyl, preferably hydrogen or methyl; R is a straight or branched chain of from 1 to 12 and preferably I to 3 carbon atoms; and X is an anion, preferably a halide or alkyl sulfate. Other examples of X include sulfate, sulfonate, phosphate, hydroxide, borate, cyanide, carbonate, thiocyanate, thiosulfate, isocyanate, sulfite, bisulfite, nitrate, nitrite, oxalate, silicate, sulfide, cyanate and acetate; other common inorganic and organic anions are also suitable. Specific examples of the particularly preferred cationic-containing monomers include diethyldiallyl ammonium chloride, dimethyldiallyl ammonium chloride, methacryloyloxy ethyl trimethyl ammonium methylsulfate and methacrylamido propyl trimethyl ammonium chloride. Mixtures of cationic-containing monomers may be used in preparing the polyampholyte. The polyampholyte may also be prepared by polymerizing a monomer containing a tertiary amine as the pendant group with subsequent quaternization of the nitrogen in the polymer to form the cationic mer units. Likewise, sulfur-containing and phosphorus-containing monomers may be exhaustively methylated to form cations. One or more non-ionic monomers may optionally be used. Examples include: acrylamide and its derivatives, such as methacrylamide and N,Ndimethyl acrylamide; acrylonitrile; vinyl acetate; vinyl pyridine; hydroxyalkyl acrylates; methacrylate and its derivatives; butadiene; styrene and its derivatives, including substituted styrenes; esters of olefinic carboxylic acids; alkylene oxides; divinyl ketones; vinyl ketones; divinyl ethers and alkyl vinyl ethers. The preferred non-ionic monomer is acrylamide. Mixtures of non-ionic monomers may be used in preparing the polyampholyte The particularly preferred carboxylic functional polyampholytes are polymers, preferably terpolymers prepared from: (i) at least one carboxylic functional monomer of the formula: EMI9.1 in which each R, which may be the same as or different from the other, is hydrogen, phenyl, C1 3 alkyl or -COOX, preferably hydrogen, methyl or ethyl, R1 is a straight or branched chain of from 0 to 12, preferably 0 to 3, carbon atoms, and X is hydrogen or an alkali or alkaline-earth metal, preferably hydrogen, sodium, potassium or caesium; (ii) optionally, at least one non-ionic monomer, preferably of the formula: : EMI9.2 where each R6, which may be the same as or different from the other, is hydrogen, phenyl or C1 3 alkyl, preferably hydrogen, methyl, or ethyl, and each R2, which may be the same as or different from the other, is hydrogen or c1 3 alkyl, and (iii) at least one cationic-containing monomer, preferably one containing a quaternary ammonium, phosphonium or sulfoniumion. Non-ionic monomer may be used, and subsequently hydrolysed to obtain the desired amount of anionic component. Likewise, a copolymer may be prepared from non-ionic monomer and cationic monomer with subsequent hydrolysis of the non-ionic monomer to form the anionic portion, e.g. acrylamide can be hydrolysed to form acrylic acid. The term "aqueous", as used herein, is intended to include water in any physical state and to include water in which is dissolved or dispersed any substance, for example, inorganic salts in brine or seawater. The polyampholyte polymers may be prepared by mixing the monomers preferably in the presence of a free radical initiator. Any free radical initiator may be used. Examples include peroxides, azo initiators and redox systems. The preferred catalysts are sodium persulfate or a mixture of ammonium persulfate and any azo type initiator, such as 2,2'-azobis-(2,4-dimethyl-4-methoxyvaleronitrile). The polymerization may also be initiated photochemically. The polyampholyte may be made by any of a variety of procedures, for example, in solution, suspension, bulk and emulsions. The temperature is not critical. The reaction will generally occur between 10 and 1000C., preferably 40 to 600C. It is generally impractical to run the reaction below room temperature because the reaction is too slow. Above a temperature of 600C., the molecular weight of the polymer tends to decrease. The reaction, depending on the temperature, generally takes from 1 to 12 hours. Measuring for residual monomer will verify when the reaction is complete. The pHof the reaction mixture is not critical. The pH is generally in the range of 4.5 to 9.0. The molecular weight of ampholytic polymers is difficult to accurately measure. The polymers are instead, usually identified by intrinsic viscosity. The intrinsic viscosity of the polyampholyte is not critical in the instant invention. It is preferred that the intrinsic viscosity be at least .05 dl/g. in 1.0 M sodium chloride (measured on a 75 Cannon Ubbelohde capillary viscometer). Scale and Corrosion The polymer may be produced from any ratio of the monomers. It is preferred for scale and corrosion inhibition that the polymer be prepared from 5 to 90%, most preferably 22.5 to 70%, by weight, carboxylic functional monomer; 0.5 to 85%, most preferably 2.5 to 25%, by weight, cationic monomer; and 0 to 85%, more preferably 1.5 to 85%, and most preferably 5 to 67.5%, by weight, non-ionic monomer. The treatment concentration of the polyampholyte employed in the present invention to inhibit corrosion and scale deposit and formation is generally at least 0.1 ppm, preferably 0.1 to 500 ppm by weight of the total solution of the water-carrying system being treated. Preferably, the concentration level range will be from about 1.0 to 200 ppm. The aqueous system may be any aqueous system, for example, a cooling water, boiler water, desalination or gas scrubber system. If the system isca desalination system, the polyampholyte should have an intrinsic viscosity below 2.8 dl/g in 1.0 M sodium chloride. Drilling Muds The clay dispersion may be any finely divided solid which is capable of being dispersed or suspended in an aqueous liquid vehicle. Ordinarily, such material will include hydratable clay or colloidal clay bodies such as Wyoming bentonite, commerical medium-yield drilling clays mined in various parts of the country such as in Texas, Tennessee and Louisiana, and those produced when clayey subsurface formations are drilled. Weighting materials added to increase specific gravity such as barites, iron oxide, and the like may also be included. The aqueous medium may be fresh water such as is obtained from wells or streams; it may be salt water from the sea or from wells; or, it may even include oil-in-water emulsions, i.e. water which has become contaminated in some way with small quantities of oil, or to which such oil has been added to gain some desired advantage. It is contemplated that the drilling muds of the invention may also contain other additives besides the polymers of the invention. Materials such as caustic, quebracho, lime and the like may be added to the drilling mud at the surface while other materials such as gypsum, shale and the like may be encountered in subsurface formations during drillig operations. When employed in accordance with the invention, the polymer may be added directly to the drilling mud as a dry powder, as a slurry suspended in a suitable liquid, or as a solution in water or some other suitable solvent, and they may be incorporated in it at any convenient point in the mud circulation system. It may be desirable to employ a mixing device such as a cone and jet mixer or the equivalent for incorporating the additive in the mud. Any carboxylic functional polyampholyte, or a salt of it may be used. The anionic mer unit contains the carboxyl group. It is preferred (although not required) that at least 10 mole percent or, in terms of weight percent, at least 5%, by weight, of the polyampholyte be made up of anionic mer units. It is preferred for drilling mud applications that the polymer be prepared from 5 to 90 percent, especially 32.5 to 85 percent, by weight, carboxylic functional monomer; 0.5 to 85 percent, especially 1.5 to 40 percent, by weight, cationic monomer; and 0 to 85 percent, especially 5 to 65 percent, by weight, non-ionic monomer. The quantity of the polymer to be used in drilling mud applications will vary with circumstances over a reasonably wide range and the amount used in a specfic suspension or dispersion will depend on these circumstancs and the characteristics of the drilling fluid treated. Ordinarily, satisfactory results with regard to water loss reduction will be obtained with quantities ranging from 1 to 4 pounds per 42-gallon barrel 928.5 to 114 kg/m3) of drilling mud. For optimum reduction in fiItration rate with certain drilling muds, however, quantities up to 6 pounds per 42-gallon barrel (171 kg/m3) may be required. On the other hand, in some cases where, for example, only small improvement in filtration rate is desired, as little as 0.125 pound of the additive per barrel.5 kg/m3) of will produce the desired effect. The exact amount to be added, as previously pointed out, depends upon the original character of the mud and on the properties desired. This can be determined, as is customary in the field, by simple tests at the time the addition is made. The carboxylic functional polyampholyte may be prepared by mixing the monomers, preferably in the presence of a free radical initiator. Any free radical initiator may be used. Examples include peroxides, azo initiators and redox systems. The polymerization may also be initiated photochemically. The preferred catalysts are sodium persulfate or a mixture of ammonium-persulfate and any azo type initiator, such as 2,2'-azobis-(2,4-dimethyl-4-methoxyvaleronitrile). Enhanced Oil Recovery The concentration of amphoteric polymer treating agent in the aqueous solution pumped down the well may vary over a wide range, from about 1 ppm to about 5 percent by weight. The optimum concentration will depend, to a large extent, upon the volume of reservoir water with which the treating solution will be diluted in the formation and the crude oil viscosity. It is preferred to adjust the concentration of treating agent, and the volume of the aqueous slug injected, so that the concentration of treating agent in the formation waters will be between about 0.01 percent and 0.5 percent by weight. It is further preferred that the volume of the aqueous slug injected be between about 0.02 percent and 5 percent of the oil volume in the oil recovery area around the given producing well being treated. It is preferred for enhanced oil recovery applications that the polymer be prepared from 40 to 90 percent, most preferably 47 to 70 percent, by weight, anionic-containing monomer; 0.5 to 60 percent, most preferably 1.5 to 33 percent, by weight, cationic-containing monomer; 0 to 59.5 percent, most preferably 20 to 48 percent, by weight, non-ionic monomer. It is preferred that the anionic-containing monomer be of the formula: EMI16.1 wherein R, which may be the same sr different, is hydrogen, a phenyl or an alkyl group of from 1 to 3 carbon atoms, R1 is a straight or branched chain of from 0 to 12 carbon atoms, X is -NHCH2C(CH3)2S03Y or OY, and Y is hydrogen or an alkali or alkaline earth metal. It is preferred that the polyampholyte for enhanced oil recovery be prepared from an anionic-containing monomer selected from the group consisting of acrylic acid, methacrylic acid, vinyl acetic acid, crotonic acid, allylacetic acid, 4-methyl-4-pentenoic acid and acrylamide methyl propane sulfonic acid; a cationic-containing monomer selected from the group consisting of dimethyldiallyl ammonium chloride, methacryloyloxy ethyl trimethyl ammonium methylsulfate and methacrylamido propyl trimethyl ammonium chloride, and optionally a non-ionic monomer selected from the group consisting of acrylamide and its derivatives, acrylonitrile, vinyl acetate, butadiene, vinyl pyridine, methacrylate and its derivatives, and styrene and its derivatives. The most preferred polymer for this use is prepared from acrylic acid, methacryloyloxy ethyl trimethyl ammonium methylsulfate and acrylamide. In contrast to the other uses disclosed herein, the higher the intrinsic viscosity of the polymers, the better they appear to work. Intrinsic viscosities of 10 to 20 are preferred. In carrying out the process of this invention, conventional injection procedures are employed, i.e., the well to be treated is suitably fitted with packers, if required, and the aqueous treating agent is forced down the well bore and out into the reservoir formation by means of conventional pumping equipment (if required) located at the well head. For a producing well, the injection can be completed in about 1/2 to 3 days, after which the well may be immediately placed back on production. The initial well effluent following the treatment is sharply reduced in water/oil ratio, and production may be continued for several weeks or months with improved oil recovery and reduced water production. Gradually, however, the water/oil ratio will begin to rise again, and when the ratio reaches an undesirably high level, the well may be again shut in and the treatment repeated to again improve production. For secondary and tertiary enhanced oil recovery, a polymer slug is followed by water, in a pattern of injection wells, until a satisfactory sweep of the producing formation has been obtained. The process of this invention may be used in waterflooding (injection well), tertiary recovery or a producing well, either an oil well or a gas well. The producing well may be operating under natural flow conditions, or it may be a producing well involved in a secondary recovery operation wherein a flooding medium, or gaseous driving medium is being injected into an adjacent well. It is contemplated that in such secondary recovery operations, treatment of the producing well will cause the selective diversion of reservoir waters to other wells, or to adjacent aquafer structures, thus reducing the water/oil ratio in the producing well effluent. Polyampholyte Polymer It is preferred, for composition claims purposes, that the polymer have an intrinsic viscosity of 0.5 to 4.5 in 1.0 M sodium chloride, as measured in a size 75 Cannon Ubbelohde viscometer, and be prepared from 20 to 90 percent, most particularly 32.5 to 85 percent, by weight, carboxylic functional monomer; 1.5 to 85 percent, particularly 5 to 65 percent, by weight, non-ionic monomer; and 0.5 to 40 percent, particularly 1.5 to 30 percent, by weight, cationic-containing monomer. Examples Preparation of the Polymers Polymers 1 to 58: The polymers of the examples were produced by mixing the cationic, anionic and optional non-ionic monomers indicated in Table I, using the amounts, solids concentration, initial temperatures and pH indicated. The monomer mix was purged with nitrogen for one hour. The solvent was deionized water. The initiator was added and the components allowed to react for about 3 hours. Polymers 31 to 37 of Table I were prepared by mixing the cationic, anionic and nonionic monomers in the ratios indicated in Table I. The solutions were then neutralized to a pH of 7.0 with 50% w/v aqueous sodium hydroxide. Chain transfer agent and catalyst were added in the amounts indicated in Table I. The solutions were placed under fluorescent lights for sixty minutes. The resulting gels were diluted to 600 mg/L active polymer. TABLE I ------- Monomer Weight Initiator Chein Percent Temperature Polymer Cationic/Anionlc/Non-Ionic Percent (Moles Initietor/Moles Monomer) Trensfer Agent Solids pH ( C.) [n]19 1 DHDAAC1/AA2/AM3 1.5/18.2/50.3 .003 SPS4/1.6x10-4 SMBS5 ----- 30 4.5 50 1.5 2 DMDAAC/AA/AM 2.5/32.5/65 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.3 3 DMDAAC/AA/AM 2.5/47.5/50 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.8 4 DMDAAC/AA/AM 2.5/5/20 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 2.2 5 DMDAAC/AA/AM 2.5/62.5/35 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.9 6 DMDAAC/AA/AM 5/85/10 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 0.82 7 DMDAAC/AA/AM 8/44/48 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 0.91 8 DMDAAC/AA/AM 8/50/42 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 0.93 9 DMDAAC/AA/AM 10/35/55 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.50 10 DMDAAC/AA/AM 10/40/50 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.60 11 DMDAAC/AA/AM 10/47/43 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 0.33 12 DMDAAC/AA/AM 10/55/35 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 2.2 13 DMDAAC/AA/AM 10/70/20 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 2.5 14 DMDAAC/AA/AM 12/44/44 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.54 15 DMDAAC/AA/AM 12/50/38 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.70 16 DMDAAC/AA/AM 17.5/32.5/50 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.0 17 DMDAAC/AA/AM 17.5/47.5/35 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 1.6 18 DMDAAC/AA/AM 17.5/62.5/20 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 3.3 19 DMDAAC/AA/AM 25/70/5 .003 SPS/1.6x10-4 SMBS ----- 30 4.5 50 4.3 20 DMDAAC/AA/DMAM6 20/70/10 .003 APS7/.0005ADM8 ----- 10 7.0 60 4.3 21 DMDAAC/AA/MA9 20/70/10 .003 APS/.0005 AMD ----- 10 7.0 60 4.3 22 DMDAAC/AA 30/70 .003 SPS/6.4x10-5 SMBS ----- 15 7.0 60 -- 23 DMDAAC/AA/Vinyl Acstate 20/70/10 .003 SPS/6.4x10-5 SMBS ----- 10 7.0 50 -- 24 DMDAAC/AA/Styrene10 10/70/20 .003 SPS/6.4x10-5 SMBS ----- 20 4.5 50 -- 25 DMDAAC/MAA11/AM 10/70/20 .003 APS/.0005 ADM ----- 10 7.0 60 4.3 26 MAPTAC12/AA/AM 20/70/10 .003 APS/.0005 ADM ----- 10 7.0 60 4.3 27 MAPTAC/AA/AM 40/40/20 .003 APS/.005 ADM ----- 10 7.0 50 2.25 28 METAMS13/AA/AM 10/70/10 .002 APS ----- 10 7.0 40 4.3 29 VTPPB14/AA/AM 10/70/20 .003 APS/.0005 ADM ----- 10 7.0 60 1.1 30 DMDAAC/DEDAAC/AA/AM 27.5/2.5/30/40 .05 TBP20 ----- 30 4.5 50 11.4 31 MAPTAC/AMPS15/AM 10/70/20 5.3x10-5 Rlboflavin 1 % IPA16 30 4.5 50 5.5 32 METAMS/AA/AM 5/47/48 5.3x10-5 Rlboflavin 1 % IPA 30 4.5 50 14.0 33 DMDAAC/AA/AM 8/60/32 1.06x10-5 Riboflavin/.053 SPS 1 % IPA 30 4.5 50 3.3 34 METAMS/AA/AM 8/60/32 7.35x10-4 Riboflavin 20 % TEA17 30 4.5 50 11.2 35 DMDAAC/AA/AM 8/60/32 1.06x10-5 Riboflavin 20 % TEA 30 4.5 50 3.1 36 METAMS/AA/AM 8/60/32 7.35x10-5 Riboflavin 2.1 % TEA 30 4.5 50 11.0 37 METAMS/AA/AM 8/60/32 4.2x10-5 Rlboflavin 1 % IPA 30 4.5 50 11.2 38 DMDAAC/AA/HPA18 10/67.5/22.5 .003 SPS/6.4x10-5 SMBS 10 % IPA 30 4.5 50 0.3 39 DMDAAC/AA/HPA 10/22.5/67.5 .003 SPS/6.4x10-5 SMBS 10 % IPA 30 4.5 50 0.3 40 DMDAAC/AA/HPA 10/67.5/22.5 .003 SPS/6.4x10-5 SMBS 10 % IPA 30 4.5 50 0.5 41 DMDAAC/AA/HPA 10/22.5/67.5 .003 SPS/6.4x10-5 SMBS 10 % IPA 30 4.5 50 0.3 42 MAPTAC/AA/AM 10/35/55 .003 SPS/6.4x10-5 SMBS 12.5 % IPA 30 4.5 50 0.5 Table 1 (Continued) : : Monomer meidrt Inftintor Chaln Percent Temperature Polymer Cationic/Anionic/Non-Ionic Percent (Moles Initistor/Moles Monomer) Trensfer Agent Solids pH ( C.) [n]19 -------- -------------------------- -------- ------------------------------- -------------- ------- ----- ------------ ------ 43 VIPPB/AA/AM 20/30/50 .003 SPS/6.4x10-4 SMBS 10 % IPA 30 4.5 50 0.4 44 METAHS/AA/AM 10/30/60 .003 SPS/6.4x10-4 SMBS 10 % IPA 30 4.5 50 0.14 45 DMDAAC/AMPS/AM 11/39/50 .003 SPS/6.4x10-4 SMBS 10 % IPA 30 4.5 50 0.57 46 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 1.5 % IPA 30 4.5 50 1.1 47 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 2.0 % IPA 30 4.5 50 0.9 48 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 2.5 % IPA 30 4.5 50 0.9 49 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 3.0 % IPA 30 4.5 50 0.9 50 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 3.5 % IPA 30 4.5 50 0.8 51 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 5.0 % IPA 30 4.5 50 1.4 52 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 10.0 % IPA 30 4.5 50 1.0 53 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 15% IPA 30 4.5 50 0.6 54 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 10 % TGA21 30 4.5 50 0.38 55 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS 12 % TGA 30 4.5 50 0.36 56 DMDAAC/AA/AM 10/70/20 .003 SPS/6.4x10-4 SMBS 8 % TGA 30 4.5 70 0.30 57 DMDAAC/AA/AM 10/70/20 .003 SPS/6.4x10-4 SMBS 12% TGA 30 4.5 70 0.23 58 DMDAAC/AA/AM 10/47/43 .003 SPS/6.4x10-4 SMBS --- 30 4.5 50 2.0 1DMDAAC = dimethyldiellyl ammonlum chloride 2AA = acrylic @cid 3AM = acrylemlde 4 = SPS = sodium persulfate 5SMBS = sodium metsbisulfite 6DMAM = N,N-dimettry 1 scdrylemide 7APS = @@@onium persulfate 8AOH = 2,2'-eroble-(2,4-disethyl-4-methoxyvaleronitrile) 9MA = methacrylemide 10A 50/50 dimethylformmeide/mater zolvent was used 11MAA = methscrylic scid 12MAPTAC = methecrylemido propyl trimethyl emonium chioride 13 METAMS = methacryloyloxyethyl trimethyl ammonlum methylsulfate 14 VTPPB = vinyl-triphenyl phosphoniom bromide 15AMPS = acrylamido methylpropane sulfonic @cid 16IPA = lsopropyl alcohol 17TEA = triethenol smine 18HPA = hydroxypropyl acrylete 19dl/g in 1.0 M soditm chlorlde, measured on a 75 Cannon @bbelchde Capillery Viscometer 20TBP = t-buty 1 peroxy pivalate 21 TGA = thio glycolic acid Polymer 59: A 90/10 acrylamide/dimethyldiallyl ammonium chloride copolymer was prepared in the same manner as Polymers 1 to 30 gnd 38 to 58. The copolymer was then hydrolysed by adding a stoichiometric amount of sodium hydroxide to achieve a 70/20/10 terpolymer of acrylic acid/acrylamide/dimethyldiallyl ammonium chloride. Examples 1-31 (Cooling Water) Calcium phosphate inhibition was tested using 250 ppm Ca++ and 6.0 mg/l POZ with 10 ppm of inhibitor, at a pH of 8.5 and at 600C for 24 hours. The percent inhibition, as reportedtin Table II, was determined by measuring the PO4= concentration in solution before and after the 24 hour period. TABLE II Percent Example Polymer Inhibition 1 19 10 2 13 40 3 18 80 4 5 60 5 4 5 6 12 90 7 15 90 8 8 90 9 17 95 10 3 90 11 14 90 12 7 95 13 10 90 14 16 90 15 2 95 16 38 92 17 39 78 18 40 85 19 41 92 20 42 100 21 43 94 22 44 100 23 45 0 The percent inhibition of calcium phosphate was measured using 2.5 ppm and 5 ppm inhibitor, by the method outlined in Examples 1-23. The results are reported in TABLE III. TABLE III Percent Inhibition Example Polymer 2.5 ppm 5 ppm 24 46 25 100 25 47 - 30 26 48 25 100 27 49 20 100 28 50 0 100 29 51 70 100 30 52 25 100 31 53 30 100 1DMDAAC = dimethyldiallylammonium chloride 2IPA = isopropyl alcohol Examples 32 - 40 (Desalination) Steam was passed through a metal U tube to maintain the temperature at 2400F. The U tube was immersed in a cylindrical cell. Seawater, with a concentration factor of 1.6 times normal seawater, (pH 8.2) was passed through the cell at a rate of. 600 ml/hr. After 24 hours, the scale deposited on the U tube was removed, weighed and analyzed. The effectiveness is reported as % inhibition, defined by the equation: % inhibition = blank scale rate - inhibition scale rate x 100. blank scale rate The scaling rates were determined by the equation: scale rate = weight of scale on tube (mg) test volume throughput (1). The % inhibition of various scale inhibitor mixtures is indicated in TABLE IV. TABLE IV Percent Example Polymer Active Inhibition 32 54 5 85 33 55 5 95 34 56 5 76 35 57 5 70 36 55 2.5 79 37 55 7.5 78 38 58 5 62 39 13 5 0 (90% Increase) 40 19 5 0 (70% Increase) Examples 41 - 56 (Boiler Water) Polymer 11 was added in the amount indicated in TABLE V to samples of synthetic boiler water containing varying amounts of PO4#, OH , SiO2, Mg++ and chelant (sodium nitrilotriacetic acid). Each Example was tested under three conditions; without any terpolymer, with 1 mg/l and with 10 mg/l of terpolymer. The mixtures were heated to 900C. and held at that temperature throughout the tests. The pH was maintained between 10 to 12. Each sample was observed after 1 hour, 4 or 5 hours, and 21 or 22 hours. The observations are described in TABLE V. The test is used to predict the effectiveness of the inhibitors in boiler water systems. Under the observation rankings, A is the most preferred result, whereas F is the least preferred result. TABLE V EMI26.1 <SEP> Observations <tb> <SEP> Dosage <SEP> (mg/l) <SEP> Hp <SEP> inhibitor <SEP> terpolymer <SEP> (1 <SEP> mp/l) <SEP> terpolymer <SEP> (10 <SEP> mg/l) <tb> Exemple <SEP> Na3NTR <SEP> PO4+ <SEP> OH- <SEP> SiO2 <SEP> mE++ <SEP> 1 <SEP> hr. <SEP> 4 <SEP> hrs. <SEP> 21 <SEP> hrs <SEP> 1 <SEP> hr. <SEP> 5 <SEP> hrs <SEP> 22 <SEP> hrs. <SEP> 1 <SEP> hr <SEP> 5 <SEP> hrs. <SEP> 22 <SEP> hrs <tb> <SEP> 41 <SEP> 36 <SEP> 20 <SEP> 306 <SEP> 100 <SEP> 10 <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> A <SEP> D <SEP> F <tb> <SEP> 42 <SEP> 36 <SEP> 5 <SEP> 306 <SEP> 100 <SEP> 10 <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> D <SEP> D <SEP> F <tb> <SEP> 43 <SEP> 36 <SEP> 30 <SEP> 30 <SEP> 100 <SEP> 10 <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> A <SEP> A <SEP> A <tb> <SEP> 44 <SEP> 36 <SEP> 5 <SEP> 10 <SEP> 100 <SEP> 10 <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> F <SEP> A <SEP> A <SEP> A <tb> <SEP> 45 <SEP> 36 <SEP> 20 <SEP> 306 <SEP> 10 <SEP> 10 <SEP> F <SEP> m/C <SEP> m/C <SEP> C <SEP> C <SEP> C <SEP> A <SEP> A <SEP> A <tb> <SEP> 46 <SEP> 36 <SEP> 5 <SEP> 306 <SEP> 10 <SEP> 10 <SEP> F <SEP> m/C <SEP> m/C <SEP> C <SEP> C <SEP> C <SEP> A <SEP> A <SEP> A <tb> <SEP> 47 <SEP> 36 <SEP> 20 <SEP> 25 <SEP> 10 <SEP> 10 <SEP> m/C <SEP> C <SEP> C <SEP> C <SEP> F <SEP> C <SEP> A <SEP> A <SEP> A <tb> <SEP> 48 <SEP> 3.6 <SEP> 5 <SEP> 25 <SEP> 10 <SEP> 1 <SEP> C <SEP> D <SEP> D <SEP> C <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 49 <SEP> 3.6 <SEP> 20 <SEP> 306 <SEP> 100 <SEP> 1 <SEP> D <SEP> C <SEP> C <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 50 <SEP> 3.6 <SEP> 5 <SEP> 306 <SEP> 100 <SEP> 1 <SEP> C <SEP> C <SEP> F <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 51 <SEP> 5.6 <SEP> 20 <SEP> 25 <SEP> 100 <SEP> 1 <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 52 <SEP> 3.6 <SEP> 5 <SEP> 10 <SEP> 100 <SEP> 1 <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 53 <SEP> 3.6 <SEP> 30 <SEP> 306 <SEP> 10 <SEP> 1 <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 54 <SEP> 3.6 <SEP> 5 <SEP> 306 <SEP> 10 <SEP> 1 <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 55 <SEP> 3.6 <SEP> 30 <SEP> 56 <SEP> 10 <SEP> 1 <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> <SEP> 56 <SEP> 3.6 <SEP> 5 <SEP> 56 <SEP> 10 <SEP> 1 <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> A <SEP> clear <tb> B <SEP> small <SEP> particulates <SEP> disapeared <SEP> thromphout <SEP> the <SEP> misture <tb> C <SEP> small <SEP> particulates <SEP> nettled <SEP> on <SEP> the <SEP> bottom <tb> D <SEP> particulates <SEP> agglomerated <SEP> on <SEP> the <SEP> bottom <SEP> to <SEP> the <SEP> size <SEP> of <SEP> a <SEP> small <SEP> motton <SEP> bail <tb> E <SEP> particulates <SEP> agglomerated <SEP> on <SEP> the <SEP> bottom <SEP> to <SEP> the <SEP> size <SEP> of <SEP> a <SEP> medium <SEP> motton <SEP> bail <tb> F <SEP> particulates <SEP> agglomerated <SEP> on <SEP> the <SEP> bottom <SEP> to <SEP> the <SEP> size <SEP> of <SEP> a <SEP> large <SEP> motton <SEP> bail <tb> Examples 57 - 72 (Gas Scrubbers) Zeta potential is a measure of particle surface charge at the particle/water shear surface. An effective inhibitor will increase the charge, thus increasing the repulsive forces between particles. This will increase the dispersibility of the particles and decrease the coagulation, precipitation and subsequent scaling. The zeta potentials of magnetite (iron oxide) particles and of calcium carbonate and magnetite in a 70/30 weight blend were determined for 1,000 ppm suspensions in deionized water at varying pHs. 0.5 ppm and 5 ppm of various polymers were added to the suspensions and the zeta potential was remeasured. The change in the zeta potential after inhibitor addition, or zeta potential increase, is noted in TABLE VI. When the zeta potential increased, more stable suspensions were created. Mixed deposits of magnetite and calcium carbonate are particularly typical of deposits found in many gas scrubbing systems. TABLE VI Zeta Potential Increase (mV) Concen- 70/30 tration Carbonate/ Example Polymer (ppm) pH Magnetite Magnetite 57 17 5.0 8 -0.2 21.5 58 17 5.0 10 3.5 15.0 59 17 0.5 8 1.4 24.5 60 17 0.5 10 -1.6 11.9 61 19 5.0 8 11.1 21.4 62 19 5.0 10 11.4 27.4 63 19 0.5 8 2.1 27.2 64 19 0.5 10 1.6 26.8 65 13 5.0 8 10.2 31.9 66 13 5.0 10 8.6 41.4 67 13 0.5 8 3.4 27.2 68 13 0.5 10 7.4 38.1 69 6 5.0 8 9.1 36.9 70 6 5.0 10 13.4 39.0 71 6 0.5 8 5.9 39.1 72 6 0.5 10 6.6 t 32.5 EXAMPLES 73 to 75 (Silica Inhibition) 20.0 cc of 1.0 M sodium chloride, 8 cc of 0.1 M sodium silicate solution, and a predetermined amount of inhibitor, if any, were mixed and diluted with distilled water to give 100 mls final volume. The temperature of the mixture was held at about 400C. throughout the experiment and the pH was adjusted to 8.0 by the addition of hydrochloric acid. The silica monomer concentration was determined after 5.0 minutes by the molybdate method (Alexander, C.8.; J.A.C.S. 75, 5055 (1953)] and at subsequent time intervals. The data were analysed by use of a second order kinetic plot and the polymerization rate was determined. TABLE VII records the effects of inhibitor on the silica polymerization process. A reduction in this polymerization rate is indicative of an expected reduction in the rate of silica deposition onto heat transfer and water transport surfaces in aqueous systems. TABLE VII Dosage SiO2 Polmer ization Rate Example Polymer (ppm) (M-Minute-1) 73 None --- 1.7 74 16 100 0.6 75 30 50 0.12 Example 76 (Corrosion) The coupon immersion test consisted of a cylindrical battery jar with a capacity of 8 liters. A Haake constant temperature immersion circulator (Model E-52) was used to control the solution temperature and agitate the controlled bath. The unit contained a 1000 watt fully adjustable stainless steel heater which permitted temperature control to +0.Ol0C., and a 10 liter per minute pump with a built-in pressure nozzle agitator that ensured high temperature uniformity in the bath. A measured contact thermoregulator was used as the temperature sensing element. The pH of the solution was controlled with a Kruger and Eckels Model 440 pH Controller. This unit was capable of turning power on and off to a Dias minipump whenever the pH of the corrosive liquid environment fell below the set point. The peristaltic Dias pump, with a pumping capacity of 20 ml per hour, maintained the solution pH with the addition of sulfuric acid. Standard glass and saturated calomel electrodes were used as the sensing elements. The bath was continuously aerated at the rate of 60 cc. per minute through a medium porosity plastic gas dispersion tube to ensure air saturation. Two SAE 1010 steel coupons, each having a surface area of 4.2 square inches, were suspended by a glass hook. The solution volume to test metal surface area ratio for the test was approximately 1000:1. The composition of the synthetic water used in the test was as follows; indicating content per liter of distilled water: Ion: Ca++ Mg++ HC03 Cl SO: ppm: 88 24 40 70 328 The total hardness as CaCO3 was 318 ppm and the pH was 7.5. The temperature was 50 C. The test was conducted on the basis of a 2-3 day cycle: the system was treated with the corrosion inhibitor compositions indicated in TABLE I. After every second or third day, the test solution was discharged and a fresh solution was prepared. At the end of a 14 day cycle, the coupons were removed and analyzed and the test was terminated. The corrosion rate of the coupons was measured by their weight loss during the 14 day cycle, and the result was calculated as mils per year (mpy). The test results are summarized in TABLE VIII. TABLE VIII Turbidity Dosage Corrosion Rate (mpy) (NTU) Polymer (ppm) Steel Copper Admirality Steel -- 0 78.7 0.58 0.79 145 9 10 60.0 0.56 0.39 41 Examples 77 Through 93 (Drilling Muds) The polymers indicated in TABLE VIII were added to an aqueous clay dispersion and the viscosity and fluid loss measured. Ten grams of Bentonite clay were added to 200 cc of deionized water and sheared for 15 minutes. The 105 g of a (180 g KCl)/(1000 g total) solution were added to the slurry and sheared for 5 minutes. For the sea water evaluation, 15 g of Bentonite clay were added to 200 cc of deionized water and sheared for 15 minutes. Then 105 g of 175 g sea salt 1000 g total sheared for 5 minutes. The sea salt used was Instant OceanR, a product manufactured by Aquarium Systems. To both mixtures, 2 g of active polymer dissolved in 50 g total solution (pH adjusted to 8.5 with NaOH) were added with continued shearing for 15 minutes. The viscosity of this slurry was measured on a FANN Viscometer (Model 35) at 600 rpm and 300 rpm. The 30-minute fluid loss (FL), in mls, was measured on a FANN (Model 12) BC Filter Press under 100 psi of nitrogen. TABLE IX Performance Performance (KC1) (Sea Salt) Example Polymer 600 300 FL 600 300 FL [n] 77 -- 29 28 131.0 20 16 60 - 78 20 23 13 9.5 -- -- -- > 4.3 79 21 12 6.5 31.5 -- -- -- > 4.3 80 25 22 17 60.0 -- -- -- 4.3 81 29 7 4 15.0 -- -- -- 1.1 82 26 10 5 18.9 -- -- -- 2.25 83 27 22 15 10.5 -- -- -- )4.3 84 22 13 6 10.5 -- -- -- - 85 23 14 8 48.0 -- -- -- - 86 24 66 52 82 -- -- -- - 87 1 13 7 11.5 10 5 8 1.8 88 16 13 6 13.8 14 7 27 1.0 89 6 8 5 25 13 10 42 0.82 90 19 16 9 7.9 40 34 84 4.3 91 2 8 4 17.0 15 7 12 1.3 92 28 15 9 25.9 -- -- -- )4.3 93 59 10 5 11.0 -- -- -- - Examples 94 Through 105 (Enhanced Oil Recovery) Polyampholytes were dissolved at 600 mg/l polymer concentration in deionized water and, in the lower half of the table, 2% sodium chloride Brookfield viscosities were measured at room temperature (250C). The viscosities at varying RPM are summarized in TABLE X. TABLE V Viscosity of Polymer In Deionized Water Centipoise Brookfield Viscozity, $1 Apindle 600 mg/l, 25 C. Example: 94* 95* 96* 97 98 99 100 101 102 103 104 105 25% BOLIDE KPAM1 70% KPAN KPAM Polymer: RFN 35% SOLIDE 30% DMDAACê 10% SOLIDE 13 11 31 32 33 34 35 36 37 0.3 2520 366 460 709 500 120 3060 50 20 60 320 1459 0.6 1730 160 350 560 400 90 2130 50 20 20 320 1140 1.5 1004 274 292 440 320 84 1246 24 12 16 260 820 3.0 636 210 220 330 240 86 816 14 10 14 240 630 6.0 399 156 174 249 106 73 502 17 14 15 190 470 12.0 249 112 125 176 113 65 317 22 22 15 142 336 30.0 133 69 60 106 85 43 165 16 19 15 97 194 60.0 88 49 57 72 59 43 Off scale 17 19 9 70 Off scale ( > 100) ( > 100) Viscosity of Polymer In 2% NaCl, Centipoise Brookfield Viscosity, UL Adapter 600 mg/l, 25 C 1.5 5.1 3.4 2.6 6.0 5.0 4.4 6.4 3.6 5.6 4.4 4.0 Sample did 3.0 4.9 3.2 2.5 4.0 4.0 3.4 5.4 2.0 4.4 3.4 2.6 Not dissolve, 4.0 4.4 2.5 2.4 4.2 3.3 3.3 4.3 2.4 3.7 2.7 1.9 Presumably 12.0 4.0 2.3 2.2 3.6 2.3 2.3 3.7 1.0 3.0 2.2 1.6 due to Highly 30.0 3.0 2.1 2.0 3.1 2.1 2.1 1.3 1.5 1.6 1.7 1.2 Cross-Linked 60.0 3.6 2.2 1. 1.1 2.4 1.9 1.1 1.3 2.6 1.6 1.1 Polymer *Comparison Examples 1KPAM = hydrolysed polymeryiamide 2DMDAAC = dimethyldiellyl ammonium chloride

Claims: CL AIMS 1. A method of inhibiting corrosion and scale in an aqueous system comprising adding an effective amount of a polyampholyte or a salt thereof to the aqueous system. 2. A method as claimed in Claim 1, in which the polyampholyte has been prepared from: (i) at least one carboxylic functional monomer of the formula: EMI34.1 in which each R, which may be the same as or different from the other, is hydrogen, phenyl, C13 alkyl or -COOX, R1 is a straight or branched chain of from 0 to 12 carbon atoms, and X is hydrogen or an alkali or alkaline-earth metal; (ii) at least one cationic-containing monomer; and (iii) optionally, at least one non-ionic monomer. 3. A method as claimed in Claim 2, in which the carboxylic functional polyampholyte is a terpolymer prepared from: (i) a carboxylic functional monomer of the formula set forth in Claim 1, except that R is not -COOX; (ii) at least one non-ionic monomer of the formula: EMI35.1 where each R6, which may be the same as or different from the other, is hydrogen, phenyl or C1 3 alkyl, and each R2, which may be the same as or different from the other, is hydrogen or C1 3 alkyl, and (iii) a cationic-containing monomer containing a quaternary ammonium, phosphonium or sulfonium ion. 4. An aqueous drilling fluid comprising an aqueous clay dispersion; and a carboxylic functional polyampholyte or a salt thereof. 5. A fluid as claimed in Claim 4, in which the polyampholyte is as defined in Claim 2. 6. A fluid as claimed in Claim 4, in which the polyampholyte is as defined in Claim 3. 7. A method for drilling a well in a subterranean formation, comprising circulating into the well, during drilling, an aqueous drilling fluid as claimed in Claim 4, 5, or 6. 8. A method of recovering oil and/or gas from a subterranean formation penetrated by a well bore and for reducing the concomitant production of reservoir water from it, comprising injecting into the formation through the well bore an aqueous treating solution or emulsion containing a polyampholyte prepared from (ii) 0.5 to 60%, by weight, of at least one cationic-containing monomer; and (iii) 0 to 59.5%, by weight, of at least one non-ionic monomer. 9. A polyampholyte polymer having an intrinsic viscosity of 0.05 to 4.5 in 1.0 M NaCI and prepared from (i) 20 to 90% by weight of at least one carboxylic functional monomer of the formula set forth in Claim 2; (ii) 1.5 to 85%, by weight, of at least one non-ionic monomer of the formula set forth in Claim 3; and (iii) 0.5 to 40%, by weight, of at least one cationic-containing monomer as defined in Claim 3.

Inventors: AMJAD, ZAHID, BOFFARDI, BENNETT P., COSTELLO, CHRISTINE A., MATZ, GARY F., SHERWOOD, NANCY S., YORKE, MONICA A.
Applicants: CALGON CORPORATION
Application year: 1982
Main classification: C02F5
IPC codes: C09K8, C08F2, C08F26, C08F220, C08L33, C08F20, C08F228, C08F30, C08F226, C09K3, C02F5, H01B1, C23F11, C08F28, E21B21, C23F14, C08F230