PREPARATION OF VICINAL DIOL CONTAINING MONOMERS AND POLYMERS, AND SUBTERRANEAN USE THEREOF

Abstract: Vicinal diol-containing monomers are prepared by reacting, in aqueous solution, a monomer of formula where R₁ is H or CH₃; Y is 0 or NH; R₃ and R₄ are each CH₃ or C₂H₅; n is 2 or 3; X⁻ is halogen⁻, 1 / 2 SO₄ = , CH₃SO₄⁻, C₂H₃SO₄⁻ or CH₃COO⁻; with at least one reactive vicinal diol -forming or -containing compound selected from glycidol and the 3-halo-1,2-propane-­ diols. Vicinal diol-containing polymers made from these monomers can be cross-linked to form high viscosity gels.

Description: PREPARATION OF VICINAL DIOL CONTAINING MONOMERS AND POLYMERS, AND SUBTERRANEAN USE THEREOF The present invention relates generally to vicinal diol-containing monomers and polymers, and to high viscosity, high temperature stable aqueous gels formed with the polymers which are particularly useful in treating subterranean formations. Gelled aqueous fluids are used in a variety of industrial applications to bring about desired results. For example, in the oil indutry, gelled aqueous fluids are commonly utilized in carrying out completion, various production stimulation, enhanced production, conformance control and other treatments in subterranean formations containing hydrocarbons. Such gelled aqueous fluids have included both naturally occurring and synthetic watersoluble polymer gelling agents as well as agents which cause the polymers to crosslink. The term "aqueous fluid" is used herein to mean any fluid containing some water. The fluid can also contain other components such as alcohols, acids, salts and other miscible or partially miscible substances, gasifiable components such as CO2 and N2, and solids. The naturally occurring polymer gelling agents utilized heretofore include solvatable polysaccharides such as galactomannan gums, glucomannan gums and cellulose derivatives. The synthetic polymer gelling agents include polyacrylate, polymethacrylate, acrylamide-acrylate copolymers , and others . The cross linking agents utilized include compounds containing multivalent metals which are capable of releasing metal ions in an aqueous fluid such as multivalent metal salts. Examples of the multivalent metal ions are chromium, zirconium, antimony, titanium, iron, tin, zinc and aluminum. While the heretofore utilized gelled aqueous fluids have been effective at temperatures below about 820C (1800F), at temperatures above about 93dC (2000F), and particularly where the aqueous fluids are brines or otherwise contain calcium ions, such gelled aqueous fluids are unstable in that they precipitate or rapidly degrade and revert to thin fluids Since many subterranean formations requiring procedures or treatments utilizing gelled aqueous fluids exist at temperatures above about 930C (2000F), there is a need for gelled aqueous fluids which are stable at such high temperatures. The terms "stable at high temperatures" and "high temperature stability' are used herein with respect to gelled aqueous fluids to mean that the gelled aqueous fluids retain substantial viscosity for times greater than about 6 to 8 hours at temperatures in the range of from about 820C (1800F) to in excess of 1490C (3000F). By the present invention, monomers containing vicinal diol groups, polymers formed therefrom and high viscosity gelled aqueous fluids formed with such polymers which are stable at high temperatures are provided. The monomers of the present invention have the formula: EMI3.1 wherein: R is oxygen or EMI3.2 R1 is hydrogen or methyl; R3 and R4 are independently methyl or ethyl; Y is oxygen or NH; X- is a halogen, 1/2(SO4)-, CH3SO4-, C2H3SO4- or CH3COO- ; and n is 2 or 3. These monomers are prepared by reacting in an aqueous solution a water-soluble vinyl monomer of formula: EMI3.3 wherein R1 is hydrogen or methyl; Y is oxygen or NH; R3 and R4 are independently methyl or ethyl; n is 2 or 3; and X is a halogen, 2(SO4)=, CH3SO4 , CH2H3SO4 or CH3COO-; with at least one reactive vicinal diol-forming or -containing compound selected from glycidol and the 3-halo-1,2-propanediols. Particularly suitable starting water soluble vinyl monomers containing tertiary amine groups are dimethyl aminopropyl methacrylamide (hereinafter referred to as DMAPMA), dimethylaminoethyl methacrylamide (hereinafter referred to as DMAEMA), dimethylaminopropyl acrylate (hereinafter referred to as DMAPA), dimethylaminoethyl methacrylate (hereinafter referred to as DMAEM), dimethylamino ethyl methacrylate (hereinafter referred to as DEAEM) and diethylaminoethyl acrylate (hereinafter referred to as DEAEA). Of these, DMAPMA is the most preferred. The reactive vicinal diol-forming or -containing compounds which can be utilized are glycidol and the 3-halo-1,2-propanediols such as 3-chloro-1,2-propanediol (alpha;-chlorohydrin) and 2-bromo-1.2-propandiol. In one technique glycidol, an epoxide, is reacted with the starting vinyl monomer. The ¯¯¯¯¯¯¯¯¯¯¯¯¯¯¯¯¯¯¯¯ nucleophilic amine cleaves the epoxide ring and a proton is consumed in the reaction. Therefore, the addition of a neutralizing acid or other proton source is required as the reaction proceeds. More specifically, the starting vinyl monomer and glycidol reactants are diluted with equal parts of water to make 508 active solutions. The glycidol solution and starting vinyl monomer solution are slowly combined in equal molar amounts while enough of the proton source used, e.g. a 50% by weight acid solution to maintain the pH of the reaction mixture in the range of from about 7.5 to about 12 is simultaneously added. The temperature of the reaction mixture is preferably controlled in the range of from about 100 to 200awhile the glycidol and proton source are added to the vinyl monomer solution and then raised to about 400C. When the starting vinyl monomer is DMAPITA and the proton source is sulfuric acid, the vicinal diol containing monomer formed by the procedure described above is methacrylamidopropyldimethyl-2, 3-dihydroxypropylammonium sulfate (hereinafter referred to as MAPDMDHPAS). The procedure and reaction are represented schematically as follows: EMI6.1 <tb> <SEP> CH3 <tb> <SEP> CIH3 <tb> <SEP> CH3 <SEP> CH2 <SEP> = <SEP> C <tb> <SEP> I <SEP> I <tb> CH2 <SEP> = <SEP> C <SEP> O <SEP> C <SEP> = <SEP> O <tb> <SEP> 1. <SEP> 10"-20"C <SEP> ! <tb> <SEP> CI <SEP> = <SEP> 0 <SEP> + <SEP> CH2 <SEP> - <SEP> CH <SEP> - <SEP> CH20H1 <SEP> ffTh200C <SEP> Nill <tb> <SEP> 1 <SEP> 1 <SEP> mole <SEP> 2. <SEP> 1 <SEP> mole <SEP> H+ <tb> <SEP> NH <SEP> glycidol <SEP> 3. <SEP> 400C <SEP> (CH2)3 <tb> <SEP> H2)3 <SEP> g(S04)= <tb> <SEP> (H2)3 <SEP> (SO4)= <tb> <SEP> CH3CH3 <tb> CH3 <SEP> CH3 <SEP> CH2 <tb> <SEP> CR2 <tb> <SEP> 1 <SEP> mole <tb> <SEP> DIIAPIA <SEP> I <tb> <SEP> CR2OH <tb> 1 mole MAPDMDHPAS A similar synthesis procedure is to convert the starting amine group containing monomer to the amine salt before reacting it with glycidol. For example, one mole of the starting monomer in a 50t aqueous solution can be combined with one mole of proton source prior to combining glycidol therewith. Glycidol is then combined with the salt formed at a temperature of about 10 to 200C followed by raising the temperature to about 40"C while the reaction goes to completion. When the starting monomer is D.MAPMA and the proton source is sulfuric acid, MAPDMDHPAS is formed. Another synthesis procedure which can be utilized to form the quaternary ammonium type of vicinal diol containing monomer is to react the starting vinyl monomer with 3-halo-1,2-propanediol. For example, a 50% aqueous solution of the starting monomer can be combined with an equal molar quantity of 3-halo-1,2-propanediol at a temperature of about 400C to form the vicinal diol containing monomer. When the starting monomer is DMAPMA and the vicinal diol containing compound is 3-chloro1,2-propanediol (a-chlorohydrin), the vicinal diol containing monomer formed is methacrylamidopropyldimethyl-2,3-dihydroxypropylammonium chloride (hereinafter referred to as MAPDMDHPAC). This procedure and reaction are represented schematically as follows: EMI7.1 <tb> 5 <SEP> CH3 <tb> <SEP> CH2 <SEP> = <SEP> C <tb> <SEP> CH3 <tb> <SEP> C=o <tb> CH2 <SEP> = <SEP> C <tb> <SEP> OH <SEP> OH <SEP> OH <SEP> NH <tb> <SEP> C=O <SEP> I <SEP> I <tb> <SEP> | <SEP> + <SEP> CH2 <SEP> - <SEP> CH <SEP> - <SEP> CH2C1 <SEP> 400C <SEP> (CH2)3 <tb> <SEP> NH <SEP> 1 <SEP> mole <SEP> > <SEP> I <SEP> | <SEP> Cl <tb> <SEP> | <SEP> 3-chloro-1,2-propanediol <SEP> N+ <SEP> X <tb> <SEP> (CR2)3 <SEP> CR3 <SEP> I <SEP> CR3 <tb> <SEP> CH2 <tb> CII3 <SEP> ",N <SEP> X <SEP> CH3 <SEP> CHOR <tb> <SEP> 1 <SEP> mole <SEP> CH2OH <tb> <SEP> DMAPMA <tb> 1 mole MAPDMDHPAC Vicinal diol containing monomers represented by the above structural formula wherein R is oxygen can be prepared by reacting glycidyl methacrylate (hereinafter referred to as GMA) with a proton source and a hydroxyl group to form 2-3 dihydroxylpropyl methacrylate (hereinafter referred to as DHPMA). The reaction can be carried out in the presence of an acid as a proton source and water as a hydroxyl source. This procedure and reaction are represented schematically as follows: EMI8.1 1 mole GMA 1 mole DHPIA In an alternate procedure for forming vicinal diol containing monomers wherein R is oxy gen, methacrylic acid (hereinafter referred to as MAA) is reacted with glycidol in the presence of triethylamine (hereinafter referred to as ET3N) to form DRPMA. This procedure and reaction are repre sented schematically as follows: : EMI9.1 <tb> <SEP> 0 <tb> CH2 <SEP> = <SEP> C <SEP> - <SEP> CH3 <SEP> + <SEP> CH2 <SEP> - <SEP> CH <SEP> - <SEP> CH2OH <SEP> ET3N <SEP> H2C <SEP> = <SEP> C <SEP> - <SEP> CH3 <tb> <SEP> C <SEP> = <SEP> 0 <SEP> ) <SEP> C <SEP> = <SEP> 0 <tb> <SEP> 0 <SEP> 1 <SEP> mole <SEP> 115-1160C <SEP> 0 <tb> <SEP> I <tb> <SEP> H <SEP> glycidol <SEP> H2C <tb> <SEP> HC <SEP> - <SEP> OH <tb> <SEP> I <tb> <SEP> 1 <SEP> mole <SEP> MAA <SEP> H2C <SEP> - <SEP> OH <tb> 1 mole DHPMA In another aspect of the present invention, water soluble polymers containing crosslinkable vicinal diol groups are provided. Such polymers can be formed from the vicinal diol containing monomers of this invention described above. That is, a vicinal diol containing vinyl monomer is polymerized with one or more other monomers to form a high molecular weight (above about 100,000) polymer containing crosslinkable vicinal diol groups. The polymerization reaction can be carried out utilizing known water-in-oil emulsion techniques or aqueous solution techniques. Examples of monomers which can be utilized with the vicinal diol containing monomers in the polymerization reaction to form copolymers or terpolymers are DMAPMA, methacrylamidopropyltri methylammonium chloride (hereinafter referred to as MAPTAC), N,N-dimethylacrylamide (hereinafter referred to as NNDMA), acrylamide, methacrylamide, 2-acrylamido-2-methylpropanesulfonic acid (hereinafter referred to as AMPS), sodium styrene sulfonate, N-vinyl-2-pyrrolidone and acrylic acid. Preferably, the vicinal diol containing vinyl monomer MAPDMDHPAS is polymerized with NNDMA to form a copolymer with a mole ratio of 9 moles of NNDMA to 1 mole of MAPDMDHPAS. However, other copolymers and terpolymers of other mole ratios using a variety of other monomers can be formed and utilized in accordance with this invention as illustrated in the examples which follow. In an alternate procedure for forming the vicinal diol containing polymers of this invention, a polymer starting material can be reacted with glycidol to add the vicinal diol group to the polymer. For example, a copolymer of DMAEM and acrylamide can be reacted with glycidol at a pH of about 10 to form a vicinal diol containing polymer equivalent to a polymer containing equivalent mole amounts of acrylamide, DMAEM and the quaternization product of D:lAE:i and glycidol formed from monomer starting materials. As mentioned above, the polymers of this invention containing vicinal diol groups are water soluble and hydrate in aqueous fluids. Upon being crosslinked by way of the diol groups, a high viscosity, high temperature stable, crosslinked aqueous fluid results. In forming a high viscosity gelled aqueous fluid of. this invention which is stable at high temperatures, a polymer containing crosslinkable vicinol diol groups is dissolved in an aqueous fluid. Generally, the polymer is dissolved in the aqueous fluid in an amount in the range of from about 0.48 to about 96 kg/m3 (0.004 to about 0.8 pounds of active.polymer per gallon) of solution, preferably in the range of from about 2.4 to about 9.6 kg/m3 (0.02 to about 0.08 pounds per gallon) of solution. A cross linking agent is combined with the aqueous fluidpolymer solution to thereby crosslink the vicinal diol groups of the polymer whereby a high viscosity, high temperature stable, gelled aqueous fluid is formed. The crosslinking agent is combined with the aqueous fluid-polymer solution in an amount in the range of from about 0.12 kg/m3 (0.001 pounds/gallon) of solution to about 24 kg/m3 (0.2 pounds/gallon) of solution. The crosslinking agents that can be utilized in the present invention can generally be described as water soluble salts and complexes of multivalent cations which are capable of forming a crosslinked gel with vicinal diol groups of the polymer. Examples of the multivalent metal cations are zirconium, antimony, titanium, iron, tin, chro mium and aluminum. In addition to the metal cations, boron can be utilized as a crosslinking agent. Particularly preferred such crosslinking agents are zirconium salts, such as zirconium lac- tate, zirconium acetate, and zirconium oxychloride, chrome citrate, and titanium triethanolamine, the most preferred being a zirconium lactate crosslinking composition. A particularly suitable zirconium lactate crosslinking composition can be prepared by adding about 2 moles of lactic acid to a quantity of water sufficient to allow mixing of ingredients and adjusting the pR of the resulting acid solution to about 7 with ammonium hydroxide. About one mole of zirconium metal ion having a valence of *4, preferably as zirconium oxychloride, is then added to the solution to form the crosslinking composition. Another similar suitable zirconium lactate crosslinking composition includes 2 moles of triethanolamine in addition to the lactic acid and zirconium oxychloride added at a pH of about 7. The high viscosity, high temperature stable, gelled aqueous fluids formed in accordance with the present invention utilizing polymers containing vicinal diol groups are particularly suitable for carrying out completion, stimulation, enhanced production and other treatments in high temperature subterranean formations, e.g., formations existing at temperatures above about 820C (1800F) Examples of such treatments where high viscosity gelled aqueous fluids are utilized are treatments for consolidating loose sands in formations, acidizing formations, fracturing formations, and enhancing production from formations. In accordance with the present invention, such treatments and others are carried out in high temperature subterrenean formations by contacting the formations with highly viscous aqueous gels comprised of aqueous fluids, water soluble polymers containing vicinal diol groups of the present invention and crosslinking agents. To further illustrate the present invention and facilitate a clear understanding thereof, the following examples are given. EXAMPLE 1 A water soluble vicinal diol containing vinyl monomer (MAPDMDRPAS) is prepared from DsIAP.IA and glycidol starting materials as follows. 170.26 g (1 mole) of dimethylaminoDro- pyl methacrylamide (DMAPMA) are placed in a glass vessel containing a magnetic stirrer and mixed with 294.91 g of deionized water. Two addition funnels are suspended above the vessel; one containing 75.6 g of glycidol and the other containing 49.05 g of concentrated H2S04. The pR and temperature of the reaction mixture are monitored continuously while the H2S04 is added dropwise over a period of about 30 minutes. Prior to the H2S04 addition, the solution is cooled to 190C and the solution has a pH of 11.3. After the H2S04 addition, the solution is cooled to 150C and has a pH of 7.5. The glycidol is next added dropwise and the vessel is warmed to about 210C using a hotplate. The glycidol addition time is 1 hour and 35 minutes and the final pH is 7.41. The reaction mixture is heated to and maintained at 400C for 40 hours. The final pH is 9.5. Analysis of the reaction indicates a trace of DMAPMA along with MAPDMDHPAS monomer. The structure of the synthesized MAPDMDHPAS monomer is indicated to be as follows: EMI14.1 EXAMPLE 2 DHPMA is prepared by placing lOg of concentrated sulfuric acid in 80g of deionized water. 90g of GMA are slowly added to the acid solutions while being stirred. The reaction mixture gra dually increases in temperature to 820C (1800F). The solution is then placed in an ice bath to maintain the reaction temperature between 230 and 820C (740 and 1800F). This procedure is continued until all GMA is added. The resulting DHPMA monomer is then ready for use. EXAMPLE 3 DRAMA is prepared by placing the following materials in a 100 ml round bottom flask with side arm, condensor, and addition funnel: 10.5 g methacrylic acid 0.03 g hydroquinone 0.41 ml ET3N (triethylamine with micro pipette). The flask and contents are heated in an oil bath to 1180C and then cooled to 114.50C. 7.43 g glycidol are next added to the flask. The glycidol is added at a one-drop per 4-5 second rate over the next 10-minute period while keeping the temperature at 115-1160C. The reaction product in the flask changes from clear to slight yellow in color during addition and is slowly cooled to 890C during the next 15 minutes. Vacuum is applied until boiling commences at 830C. After the boiling stops the temperature is raised to 95-1000C and boiling and vacuum are again continued for one hour to remove excess acid. An NMR analysis of the final reaction mixture reveals that 2,3-dihydroxypropyl methacrylate is the major component. EXAMPLE 4 Homopolymers, copolymers and terpolymers are prepared using the vicinal diol containing monomer (MAPDMDHPAS) prepared as described in Example 1 and other monomers. A water-in-oil emulsion technique is used which is illustrated by the following procedure wherein a copolymer of acrylamide (90 mole %) and M PDMDHPAS (10 mole t) is prepared. The following ingredients are mixed with stirring until homogeneous to form an:aqueous phase: 50% aqueous MAPDMDRPAS - 58.67 g 46% aqueous acrylamide - 139.23 g deionized water - 20.0 g ethylenediamine tetracetic acid, disodium salt, dihydrate (Na2 EDTA) - @.05 g sodium chloride - 6.0 g The pH of the aqueous phase is adjusted to 7.42 with .15 ml 50% NaOH. The following ingredients are mixed to form an oil phase. a mixture of isoparaffinic hydrocarbons (ISOPAR M) - 81 g sorbitan monooleate - 6 g The oil phase is added to a 500 ml Waring blendor jar fitted with a lid containing two ope nings for an N2 inlet tube and an addition funnel. The oil phase and waring blendor jar are sparged with N2 gas. The aqueous phase is introduced into the oil phase over a 1i minute period while stirring at about 4000 rpm. The resulting emulsion is stirred for an additional 5 minutes at the same rate. The emulsion is added to a presparged one-liter glass kettle fitted with a stirrer, a N2 inlet tube, a N2 exit tube, and a thermocouple probe with a digital readout. The water-in-oil comonomer emulsion is stirred at an rpm of from about 500 to about 1500 and sparged with N2 gas while heating to 400C in about 30 minutes, followed by the addition of 0.2 g sodium bisulfite. Stirring and sparging are continued while maintaining the temperature at about 400C for 15 minutes, followed by the addition of 0.1 g 2,2 -azobis (2,4 -dimethyl- valeronitrile) initiator. After about 45 minutes, a mild exotherm starts which continues for about 3 hours. The temperature is maintained for one additional hour and an additional 0.1 g of 2,2-azobis (2,4,dime,thyLvaleronitrile) is added. The temperature is increased to about 600C and held for about one hour after which the emulsion is cooled to room temperature. This emulsion is homogeneous and stable. The inversion of the emulsion is caused by adding 3.33 g of the emulsion to a Waring blendor containing 100 g of API brine and 0.3 ml of a 50% solution of dimethylbenzyltallow ammonium chloride. "API brine is a laboratory brine formulation comprised of 1350 g NaCI and 150 g CaC12 dissolved in 13500 g of deionized water and filtered through E-D grade 617 filter paper or equivalent. Inversion of the polymer into the brine occurs in seconds as evidenced by a large increase in viscosity. A number of polymers are prepared utilizing the general procedure described above. The identification of the polymers and synthesis reaction conditions involved are set forth in Tables I and II below. The polymers are identified using a code that gives the mole % of the various monomers used in their preparation. That is, three numbers are used (0.0.0) representing, in order, mole % acrylamide, mole % NNDMA, and mole % of a termonomer. These are followed by a letter which represents the termonomer or a monomer substituted for the NNDMA, where A is dimethylaminopropyl methacrylamide (DMAP), DS is methacrylamidopropyldimethyl-2, 3-dihydroxypropylammonium sulfate (MAPDMDHPAS), DC is methacrylamidopropyldimethyl-2 ,3-dihydroxypropyl ammonium chloride (MAPDMDHPAC), Q is methacrylamidopropyltrimethyl ammonium chloride (MAPTAC) and M is methacrylamide. Sometimes a fourth number is used which represents the particular polymer synthesis. The presence of a P indicates that it is an emulsion polymer. The presence of a K or the absence of P indicates a solution polymer. The number of the polymer sometimes follows the P in the polymer identification code. TABLE I Polymer Synthesis Mole % of Monomer Feed Polymer Polymer Monomer Mole Monomer Mole Monomer Mole Polymer No. Identification 1 % 2 % 3 % Activity % 1-5 90.0.10Q.P1-5 AcAm 90 MAPTAC 10 ---- ---- 30.6 6 90.0.10DC.P6 AcAm 90 MAPDMDHPAC 10 ---- ---- 30.6 7 90.0.100A.P7 AcAm 90 DMAPMA 10 ---- ---- 29.9 8 90.0.10A.P8 AcAm 90 DMAPMA.1/2H2SO4 10 ---- ---- 30.6 9 90.0.10DS.P9 AcAm 90 MAPDMDHPAS 10 ---- ---- 31.0 10 90.3.0.9.7DS.P10 AcAm 90.3 MAPDMDHPAS 9.7 ---- ---- 31.5 11 100.0.0.P11 AcAm 100 --- --- ---- ---- 30.7 12 0.0.100DS.P12 --- --- MAPDMDHPAS 100 ---- ---- 30.6 13 50.0.50DS.P13 AcAm 50 MAPDMDHPAS 50 ---- ---- 32.8 14 90.0.10DS.P14 AcAm 90 MAPDMDHPAs 10 ---- ---- 25.0 15 80.0.20DS.P15 AcAm 80 MAPDMDHPAS 20 ---- ---- 30.0 16 80.0.20DS.P16 AcAm 80 MAPDMDHPAS 20 ---- ---- 30.8 17 90.0.10DS.P17 AcAm 90 MAPDMDHPAS 10 ---- ---- 30.0 18 50.40M.10DS.P18 AcAm 50 MAPDMDHPAS 10 MAA 40 30.0 19 90.0.10Q.P19 AcAm 90 MAPTAC 10 ---- ---- 30.0 20 90.0 10DS.P20 AcAm 90 MAPDMDHPAS 10 ---- ---- 30.0 21 80.100.10DS.P21 AcAm 80 MAPDMDHPAS 10 MAPTAC 10 30.0 AcAm - Acrylamide MAPTAC - Methacrylamidopropyltrimethylammonium chloride MAPDMDHPAC - Methacrylamidopropyldimethyldihydroxypropylammonium chloride DMAPMA - Dimethylaminopropyl methacrylamide MAPDMDHPAS - Methacrylamidopropyldimethyldihydroxypropylammonium sulfate MAA - Methacrylamide TABLE II Polymer Synthesis Reaction Conditions Isoparaffinic Hydro Na2, carbons Sorbitan Polymer Monomers H2O NaCl EDTA NaHSO3 (Isopar M) Monooleate InitiatorÚ Temp. Time No. (g) (g) (g) (g) pH (g) (g) (g) (g) ( C) Hours 1 172.3 208.3 --- .1 4.7 --- 162 18.4 .5 49-51 2 2 96.15 104 --- .05 4.7 .25 81 9.2 .25+.25 50-60 4 3 86.39 104 --- .1 4.7 .1 81 9.2 .25 50-60 2 4 86.39 104 --- .05 4.7 .4 81 9.2 .25+.1 50-53 3 5 86.20 104.15 --- .05 4.6 .5 81 9.2 .25+.25 46-62 4 6 86.20 104.15 --- .05 7.8 .25 81 9.2 .25 45-51 3 7ê 81.14 99.1 --- .05 10.1 .5 81 9.2 .25 45-90 4 8 85.95 103.9 0.2 .05 --- --- 81 9.2 .25 45#.3 3 9 93.39 111.34 0.2 .05 4.9 --- 81 9.2 .25 45#.3 3 10 92.37 110.32 0.2 .05 4.9 --- 81 9.2 .20 45#.3 4 11 91.03 106.87 0.2 .05 4.8 --- 81 9.2 .20 45#.4 3 12 91.0 113.74 0.2 .05 4.9 .4 81 9.2 .20 45#.3 4 13 91.11 96.14 0.2 .05 4.9 --- 81 9.2 .20 45#.2 3 14 93.99 111.34 20. .05 7.8 --- 81 9.2 .1+.1 40.6-43.7 5 15 115.53 169.31 10. .05 8.9 .35 81 9.2 .1+.1 45-50 6 16 115.53 156.82 10. .05 7.7 .3 81 9.2 .1+.1 40.7-42.7 8 17 93.39 124.47 6. .05 7.5 .2 81 6 .1+.1 42-45 7 18 98.88 137.06 6. .05 7.9 .2 81 6 .2+.2 41-49 6 19 86.20 107.65 6. .05 8.3 .2 81 6 .1+.1 40-45 4 20 93.39 124.46 6. .05 7.4 .2 81 6 .1+.1 37-41 6 21 108.28 159.26 6. .05 7.6 .2 81 6 .1+.1 39-43 6 1 2,2' Azobis (2,4-dimethylvaleronitrile); +means 2 separate additions 2 Reaction exotherm uncontrollable 3. Reaction incomplete, little to no exotherm The polymers described above can be prepared using a solution technique instead of the water-in-oil emulsion technique. The solution technique involves reacting the monomers with initiators and' buffer in an aqueous solution in the absence of oxygen. A reaction pE in the range of from about 6 to about 9 and a reaction temperature in the range of from about OOC to about 49 C (320F to abort 120 F) can be utilized to form the polymer solution. EXAMPLE 5 The polymer emulsions formed as described in Example 4 are inverted in API brine, hydrated, crosslinked and evaluated for stability at 1210C (2500F). E. EMULSION INVERSION AND POLYMER HYDRATION A quantity of API brine is placed in a Waring blendor jar and mixed at low speed. An inverter such as a 50% by weight aqueous solution of dimethylbenzyltallow ammonium chloride is added in an amount of 10% by weight of emulsion to be inverted. The mixing rate is increased to about 1500 rpm and the amount of polymer emulsion used is added and-mixed for one minute. The resulting viscosity is measured on a Model 35 FANN VG Meter with No. 1 spring and standard bob and sleeve to determine when complete hydration has occurred. For example, 300 ml of API brine are added to a one-liter Waring blendor jar and mixed at a low rate followed by adding one ml of the above described inverter. Ten grams of polymer emulsion are added while mixing at 1500 rpm. Mixing is con tinued for one minute and viscosity is measured. The results of these tests are shown in Table III. TABLE III Viscosity Properties of Inverted Polymers Polymer Concentration: 1% by Weight of Fluid Temperature: Ambient Conditions Steady State FANN Dial Readings &commat; 100, 200 and 300 rpm Polymer Deionized Water API Brine No. 100 200 300 100 200 300 8 84 116 141 17 27 35 9 71 101 126 7 12 16 10 74 107 137 7 11 14 11 47 62 78 51 72 91 13 92 126 152 , 4 7 9 14 50 75 93 19 28 37 16 61 91 115 12 19 25 17 48 66 80 28 42 53 18 15 25 33 13 21 29 19 53 69 82 40 57 72 20 55 75 91 29 44 56 21 53 72 86 28 41 53 F. TEMPERATURE STABILITY 100 g of the hydrated polymer are placed in a glass pressure vessel. A desired amount of crosslinker such as 0.2% zirconium oxychloride is added to the vessel. The vessel is sealed and agitated to thoroughly mix the polymer and crosslinker. The vessel is then heated to the desired temperature by placing it in a heated oil bath. At desired intervals the sample is inspected and the stability of the crosslinked polymer visually noted. The results of these tests are given in Table IV below. TABLE IV Crosslinked Polymer Stability at 250 F Polymer Concentration: 1% Base Fluid: API Brine Polumer N21 Crosslinker Stability Final No. Purged Name %ê hrs pH4 Observations 215 No Potassium 0.4 < 24 8.4 homogeneous - no crosslinked gel Pyroantimonate 21 No Formic Acid 0.1 homogeneous - no crosslinked gel Potassium 0.4 < 24 4.2 Pyroantimonate 21 No Potassium 0.4 homogeneous - no crosslinked gel &commat; 48 hrs. Pyroanti- monate Zicronium 0.1 > 48 < 96 8.1 Oxychloride 206 No Potassium 0.4 < 24 8.4 homogeneous - no crosslinked gel Pyroanti- monate 20 No Formic Acid 0.1 homogeneous - no crosslinked gel Potassium 0.4 < 24 4.5 Pyroantimonate 20 No Potassium 0.4 homogeneous - no crosslinked gel &commat; 48 hrs. Pyroantimonate Zirconium 0.1 > 48 < 96 7.8 Oxychloride 197 No Potassium 0.4 < 24 8.3 homogeneous - no crosslinked gel Pyroantimonate 19 No Formic Acid 0.1 homogeneous - no crosslinked gel Potassium 0.4 < 24 4.4 Pyroantimonate (TABLE IV CONTINUED) 19 No Potassium 0.4 homogeneous - less viscosity than Pyroanti- 21 or 20 monate Zirconium 0.1 > 48 < 96 7.4 Oxychloride 21 No Zirconium 0.2 > 72 6.0 croasslinked gel - some free H2O Oxychloride 21 No Zirconium 0.2 < 16 8.58 gel separated Oxychloride 21 No Zirconium 0.3 > 48 < 72 8.0 crosslinked gel - 1/2 free H2O Lactate with Triethanolamine 21 No Zirconium 0.3 > 24 < 48 8.78 slight crosslink - free H2O Lactate with Triethanolamine 20 No Zirconium 0.2 > 48 < 72 6.3 rigid crosslinked gel &commat; 48 hrs. Oxychloride 20 No Zirconium 0.2 < 16 8.48 no crosslink - phase separation Oxychloride 20 No Zirconium 0.3 > 24 < 48 8.1 slight crosslink - rehealed on cooling Lactate with Triethanolamine 20 No Zirconium 0.3 > 24 < 48 8.78 slightly better than above gel Lactate with Triethanolamine 19 No Zirconium 0.2 > 24 < 48 5.3 crosslinked gel - 1/2 free H2O Oxychloride 19 No Zirconium 0.2 < 16 8.38 homogeneous - no crosslinked gel Oxychloride 19 No Zirconium 0.3 > 16 < 24 8.0 homogeneous - no crosslinked gel Lactate with Triethanolamine (TABLE IV CONTINUED) 19 No Zirconium 0.3 < 16 8.78 homogeneous - no crosslinked gel Lactate with Trietanolamine 18 Yes Zirconium 0.1 < 19 --- polymer flocculared Oxychloride 18 Yes Zirconium 0.2 < 19 --- polymer flocculated Oxychloride 18 Zirconium 0.1 > 48 < 72 --- polymer separated - best &commat; 72 hrs. Lactate 18 Yes Zirconium 0.2 > 48 < 72 --- polymer separated Lactate 18 Yes Zirconium 0.3 > 48 < 72 --- polymer separated - best at 48 hrs. Lactate 18 Yes Zirconium 0.2 < 19 polymer flocculated Acetate 17 Yes Zirconium 0.1 > 72 < 144 rigid crosslinked &commat; 72 hrs. Oxychloride 17 Yes Zirconium 0.2 > 72 < 144 same as above - trace free H2O Oxychloride 17 Yes Zirconium 0.1 > 72 < 144 slight crosslinked gel - trace free H2O Lactate 17 Yes Zirconium 0.2 > 72 < 144 moderate crosslinked gel - trace free H2O Lactate 17 Yes Zirconium 0.3 > 72 < 144 rigid crosslinked gel - trace free H2O Lactate 17 Yes Zirconium 0.2 > 72 < 144 less rigid than above test Acetate polymer flocculated - free H2O 18 Yes Zirconium 0.1 > 6 < 24 Lactate with Trithanolamine 18 Yes Zirconium 0.2 > 6 sample lost, broke sample jar Lactate with Triethanolamine 18 YesZirconium 0.3 > 24 < 48 more flocculated polymer than above Lactate with Triethanolamine (TABLE IV CONTINUED) 17 Yes Zirconium 0.2 > 72 crosslinked gel - free H2O Lactate with Triethanolamine 17 Yes Zirconium 0.3 > 72 weak crosslinked gel - free H2O Lactate With Triethanolamine 17 Yes Zirconium 0.4 > 72 same as above with less free H2O Lactate with Triethanolamine 13 Yes Zirconium 0.3 --- no indication of crosslink - base gel Lactate with viscosity 7 cps Triethanolamine 13 Yes Zirconium 0.6 --- no indication of crosslink - base gel Lactate with viscosity 7 cps Triethanolamine 16 Yes Zirconium 0.3 > 1; < 66 poor crosslink - base gel viscosity 12 cps Lactate with Triethanolamine 16 Yes Zirconium 0.6 > 1 < 66 porr crosslink - base gel viscosity 12 cps Lactate with Triethanolamine 17 Yes Zirconium 0.3 > 96 < 240 crosslinked gel with free H2O &commat; 96 hrs Lactate with Triethanolamine 17 Yes Zirconium 0.3 > 1 < 66 overcrosslinked - majority free H2O Oxychloride 17 Yes Zirconium 0.6 > 1 < 66 same as above test Oxychloride 18 Yes Zirconium 0.3 > 1 < 66 crosslinked gel with free H2O &commat; 66 hrs Lactate with Triethanol- (TABLE IV CONTINUED) 18 Yes Zirconium 0.6 gt;1 < 66 same as above test Lactate with Triethanolamine 18 Yes Zirconium 0.3 > 1 < 66 majority free H2O with crosslinked gel Oxychloride 1 to reduce oxygen level N2 was bubbled through gels and pressure vessels were purged 2 % = volume % based on total weight of gel 3 stability hrs. - the majority of the gel had some crosslinked character. Some free H2O may be present. No precipitate noted. 4 final pH - pH was obtained after test was completed and sample cooled to ambient condition 5 initial pH of base gel 6.73 6 initial pH of base gel 7.0 7 initial pH of base gel 6.9 8 pH adjusted to this value with NaOH Steady state viscosity properties of polymers 8 through 21 in deionized water and API brine are shown in Table III. The relative molecular weights and degrees of ionic character of the prepared copolymers are utilized to evaluate the synthesis conditions. Viscosity properties in deionized water are a function of molecular weight and degree of ionic character while the viscosity difference in these two base fluids is predominantly a function of the degree of ionic character. Preliminary stability data at 1210C (2500F) for several polymers crosslinked with various metal crosslinkers are presented in Table IV. Gel stability is dependent upon the polymer, crosslinker, crosslinker concentration, pH and oxygen content. In general, the most stable gels are formed with polymers 17, 20 and 21 when crosslinked with 0.1 or 0.2% of zirconium oxychloride or 0.38 of zirconium lactate with triethanolamine. EXAMPLE 6 Vinyl monomers containing vicinal diol groups are prepared as follows. A. Methacrylamidopropyldimethyl-2 ,3-dihydroxypropyl- ammonium sulfate (MAPDMDAPAS). To a l-liter glass beaker containing a magnetic stirrer is added 170.26 g (1 mole) of DMAPMA and 170.26 g of deionized water while stirring. Initial pH and temperature are 11.2 and 23.1"C, respectively. Two addition funnels are suspended above the beaker; one contains 75.6 g (1 mole) of glycidol and the other contains 98.2 g of 508 H2SO4. The pH and temperature are monitored continuously during the drop-wise addition of glycidol. Temperature is maintained between 19.50 and 27.5doc by placing the beaker in an ice bath. The, pH is maintained between 10.6 and 11.2 by adding 50% H2SO4 as, needed. All of the glycidol is added within 1 hour and 4 minutes. An additional 75.6 g of water is added to the reaction mixture; a portion is flowed through the addition funnel which contained the glycidol and the remainder is added to the addition funnel containing the remaining H2S04. The ice bath surrounding the reaction vessel is removed and replaced with a warm water bath in order to raise the reaction temperature to 400C. The remaining acid and water mixture is added to the reaction vessel over a period of 2 hours and 41 minutes. During this stepwise addition the temperature is held at about 400C and the pH is maintained between 11.3 and 10.1 until the last portion of acid is added. The final pH is 4.55. The reaction mixture is then placed in a sealed brown bottle and submerged in a 42"C bath. The reaction mixture is removed at 16 hours. The final pH of the product is 5.2 at room temperature. B. Methacrylamidopropyldimethyl-2 ,3-dihydroxypropyl- ammonium chloride (MAPDMDHPAC) To a l-quart brown bottle is added 170.3 g (1 mole) DMAPMA and 280.8 g of deionized water. Mixing is accomplished by swirling the bottle. To this mixture is added 110.5 g 11 mole) of 3-chloro-1,2-propanediol. A small exotherm is observed. -The sealed bottle containing the reaction mixture is submerged in a water bath controlled to about 400C. After reacting at this temperature for 20 hours the reaction mixture is removed. The quaternary ammonium chloride monomer (prepared according to Procedure B) is formed by substitution of the chloride of a-chlorohydrin with the nitrogen of the tertiary amine. The quantity of chloride ion produced during the reaction is determined by titration with silver nitrate. Based on this analysis, it is calculated that 99.6% of the a-chlorohydrin is reacted and therefore, the percent of conversion is 99.6%. The vicinal diol content of MAPDMDHPAS and MAPDMDHPAC are determined to be 53.0% and 50.6%, respectively. The theoretical diol content of each monomer is 50.0%, since each is prepared as a 50% aqueous solution. EXAMPLE 7 A variety of polymers containing vicinal diol groups are prepared. The polymers are hydrated and the resulting gels are evaluated for stability at high temperature. The hydrated polymers are then crosslinked and evaluated for stability at high temperatures. Thermal stability tests of hydrated emulsion polymers at 2500F in API brine are summarized in Tables V and VI. Thermal stability tests of hydrated solution polymers at 2800F in API brine are summarized in Tables V and VI. Thermal stability tests of hydrated solution polymers at 280"F in API brine are summarized in Table VII. The solution polymers are prepared by reacting the starting materials and initiators in a 2% potassium chloride solution. PROCEDURE To obtain a 100 g sample of hydrated polymer gel, 97.7 g of deionized water is added to a 500 ml Waring blendor. An inverter such as a 50% by weight aqueous solution of dimethylbenzyltallowammonium chloride is added in an amount of 0.33 ml to the water with gentle mixing. The emulsion polymer (3.33 g) is quickly added with a syringe while mixing at about 1500 rpm. Mixing is continued for 2 minutes. The sample is left static at least one hour at ambient temperature to fully hydrate before use or evaluation. A 100 g sample of hydrated base gel is placed in a 250 ml (8 oz.) glass jar. The sample is purged 30 minutes by bubbling N2 through the sample. The jar is sealed and then placed inside a purged pressure vessel. The vessel is placed into an oil bath at the desired temperature for the required time period. The vessel is then removed and cooled to ambient temperature. The sample is removed and evaluated. Data such as pH, viscosity and gel conditions are recorded. TABLE V Thermal Stability of 1% Emulsion Polymers at 1210C (2500F) in API Brine Time at Initial-'- Final-'- 1210C Viscosity Viscosity Viscosity (2500F) Retained Polymer Pa s (cp) Pa s (cp) (days) % 80.10Q.10DS.P21 .2 200 .012 12.0 2.25 6 50.40.10DS.P24 .085 85 .019 19.0 5.0 22 50.40.10DS.P24 .085 85 .008 7.5 12.0 9 50.40Q.1ODS.P23 .075 75 .007 6.5 5.0 9 50.40Q.1ODS.P25 .085 85 .010 10.0 5.0 12 90.0.10DS.P20 .019 19.0 2.25 90.0.10Q.P19 .006 6.0 2.25 Viscosity measured on a Brookfield LVT using a number 1 spindle at 6 rpm. TABLE VI Thermal Stability of 1% Emulsion Polymers in API Brine Initial* Final* Retained Time at Viscosity Viscosity Viscosity Temperature Temperature Polymer Pa s (cp) pa s (cp) % C ( F) (days) 70.20.10DS.P43 .13 130 .02 20 14 121 250 5.0 70.20.10DS.P43 .13 130 .055 55 42 121 250 7.0 70.20.10DS.P43 .13 130 .15 150 115 121 250 10.0 50.40.10DS.P41 .272 272 .826 826 304** 138 280 0.9 50.40.10DS.P41 .345 345 .03 30 8 138 280 0.9 50.40.10DS.P40 .18 180 .13 130 72 121 250 3 50.40.10DS.P40 .18 180 .10 100 565 121 250 5 50.40.10DS.P40 .18 180 .035 35 20 121 250 7 50.40.10DS.P40 .18 180 .01 10 6 121 250 10 50.40.10DS.P41 .19 190 .23 230 120 121 250 3 50.40.10DS.P41 .19 190 .065 65 34 121 250 5 50.40.10DS.P41 .19 190 .021 21 11 121 250 7 50.40.10DS.P41 .19 190 .025 25 13 121 250 10 60.30.10DS.P42 .15 150 .1 100 67 121 250 3 60.30.10DS.P42 .15 150.025 25 17 121 250 5 60.30.10DS.P42 .15 150 .03 30 20 121 250 7 *Viscosity measured on a Brookfield LVT using a number 1 spindle at 6 rpm. ** Sample believed to be contaminated wiyh metal ions during test. TABLE VII Thermal Stability of 1% Solution Polymers at 1380C (2800F) in API Brine for 22 Hours Initial ' Finalt Viscosity Viscosity Viscosity Retained Polymer Pa s (cp) pa s (cp) 75.20.5DS.9K .617 617 .320 320 52 70.20.10DS.7K .087 87 .049 49 56 70.20.10DS.76 .058 58 .054 54 93 70.20.10DS.7K .101 101 .042 42 42 70.20.10Q.80 .121 121 .079 79 65 70.20.10Q.80 .119 119 .026 26 22 70.20.10Q.78 .094 94 .043 43 46 70.20.10A.106 .067 67 .028 28 42 50.40.10DS.8K .074 74 .049 49 66 50.40.10DS.8K .078 78 .047 47 60 50.40.10DS.8K .082 82 .044 44 54 0.90.10DS.87 .036 36 .055 55 152 0.90.10DS.12K .025 25 .024 24 96 0.90.10DS.12K .024 24 .023 23 96 0.90.10DS.12K .021 21 .016 16 76 Viscosity measured on a Brookfield LVT using a number 1 spindle at 6 rpm. Tables V, VI and VII show the superiority of the 0.90.10DS polymer formulation over other polymer formulations. The stability testing of inverse emulsion polymers at 1210 and 1380C (250 and 2800F) shows a loss of viscosity with time except in the case of 70.20.10DS.P43 (see Table IV). This polymer at 1% concentration at 1210C (2500F) in API brine gives a decrease in viscosity with time until 10 days when a viscosity increase is observed. This viscosity increase is supported by the 1380C (2800F) studies. The 70.20.10DS.P43 solutions appear to crosslink or get thicker after 22 hours. This phenomena is not observed using the equivalent solution polymer, 70.20.10DS.7K. This indicates that there may be some differences in the emulsion and solution polymers. The visual evaluation of crosslinked polymers for thermal stability is more difficult than the evaluation of the base hydrated polymers. The stability of the crosslinked gel is sensitive to the crosslinker, crosslinker concentration and polymer concentration in addition to the temperature. The crosslinked gels are evaluated on a scale as follows: 1. failure - no viscosity or precipitate forms; 2. 2 phase - separation of polymer and free fluid; 3. homogeneous - viscosity present but not a lipping gel; 4. lipping - crosslinked fluid which forms a tongue upon transfer; 5. rigid - crosslinked fluid hich tries to retain its shape. The initial testing of the thermal stability oE the crosslinked gels is performed at 820C (1800F) and is summarized in Table VIII. The polymers react with a variety of crosslinkers and are stable for extended periods of time at 820C (1800F). The crosslinked polymers are evaluated at 138C and 1490C (2800F and 3000F) in API brine at 1 and 0.5% polymer concentrations. A concentration range of zirconium lactate crosslinker of 0.075 to 0.6 volume/volume % is used to evaluate these polymers. The results of these tests are given in Tables IX and X. PROCEDURE Stability tests on crosslinked polymers are performed by placing 100 g samples of hydrated base gels in 250ml (8 oz.) glass jars. The designated amount and type of crosslinker is added with a micropipette syringe. The jars are each sealed and then placed inside a purged pressure vessel with enough water placed inside the vessel to cover the sample level in the jar. The vessel is placed. in an oil bath of the desired temperature for the required time period. The vessel is then removed and cooled to ambient temperature. The samples are removed and visually evaluated. TABLE VIII Thermal Stability of Crosslinked Gels at 820C (1800F) in API Brine Polymer Crosslinker Time at Concentration Concentration Temperature Gel Polymer (%) Crosslinker (%) (days) Evaluation 50.40.10DS.6K 1.0 Potassium .4 8 homogeneous Pyroanti monate 50.40.10DS.6K 1.0 Zirconium .2 8 rigid Acetate 50.40.lODS.6K 1.0 Zirconium .4 8 homogeneous Lactate with Amine 50.40.10DS.P24 1.0 Potassium .4 .75 2 phase Pyroanti donate 50.40.10DS.P24 1.0 Zirconium .2 .75 rigid - Acetate 50.40.10DS.P24 1.0 Zirconium .4 .75 rigid Lactate 50.40.10DS.P24 1.0 Basic .4 .75 2 phase Aluminum Acetate 50.40.10DS.P24 1.0 Zirconium .2 .75 rigid Osychioride 50.40.lDDS.P24 1.0 Zirconium .4 3 rigid Lactate <RTI ID=40.8> SO.40.10DS.P24 1.0 Zirconium .4 5 rigid Lactate 50.40.10DS.P24 1.0 Zirconium .4 10 rigid Lactate 50.40.10DS.P26 1.0 Zirconium .4 3 rigid Lactate 50.40.10DS.26 1.0 Zirconium .4 5 rigid Lactate 50.40.10DS.26 1.0 Zirconium .4 10 rigid Lactate 55.40.5DS.5K 1.0 Potassium .4 8 homogeneous Pyroanti monate Table VIII (Continued) 55.40.5DS.5K 1.0 Zirconium .2 8 rigid Acetate 55.40.5DS. 5K 1.0 Zirconium .4 8 homogeneous Lactate with Amine 55.40.5DS.P27 1.0 Zirconium .4 3 rigid Lactate 55.40.5DS.P27 1.0 Zirconium .4 5 rigid Lactate 55.40.5DS.P27 1.0 Zirconium .4 10 rigid Lactate 0.90.10DC.124 0.5 Zirconium .2 2.8 homogeneous Lactate 0.90.10DC.124 0.5 Zirconium .6 2.8 rigid Lactate 0.90.10DC.129 0.5 Zirconium .2 2.8 lipping Lactate 0.90.10DS.123 0.5 Zirconium .2 2.8 lipping Lactate TABLE IX Thermal Stability of Crosslinked Gels at 138 C (280 F) in API Brine Zirconium Polymer Lactate Time at Concentration Concentration Temperature Gel Polymer (%) (%) (days) Evaluation 50.40.10DS.8K .5 .15 2.8 2 phase 0.90.10DS.118 .5 .6 2 2 phase 0.90.10DS.118 .5 .6 1 2 phase 0.90.10DS.118 .5 .4 1 2 phase 0.90.10DS.118 .5 .2 1 lipping 0.90.10DS.118 .5 .3 .9 2 phase 0.90.10DS.118 .5 .15 .9 homogeneous 0.90.10DS.118 .5 .075 .9 homogeneous 0.90.10DS.118 .5 .2 7 homogeneous 0.90.10DS.118 .5 .2 14 homogeneous 0.90.10DS.118 .5 .2 21 2 phase 0.90.10DS.118 .5 .15 7 homogeneous 0.90.10DS.118 .5 .15 10 lipping 0.90.10DS.118 .5 .15 14 2 phase 0.90.10DS.118 .5 .1 7 homogeneous 0.90.10DS.118 1.0 .6 .9 lipping 0.90.10DS.118 1.0 .4 .9 lipping 0.90.10DS.118 1.0 .3 .9 lipping 0.90.10DS.118 1.0 .15 .9 lipping TABLE X Thermal Stability of Crosslinked Gels at 138 C (300 F) in API Brine Zirconium Polymer Lactate Time at Concentration Concentration Temperature Gel Polymer (%) (%) (days) Evaluation 0.90.10DS.118 .5 .3 0.9 lipping 0.90.10DS.118 .5 .3 1.8 2 phase 0.90.10DS.118 .5 .25 0.9 lipping 0.90.10DS.118 .5 .25 1.8 2 phase 0.90.10DS.118 .5 .2 0.9 lipping 0.90.10DS.118 .5 .2 1.8 lipping 0.90.10DS.118 .5 .2 4.0 lipping 0.90.10DS.118 .5 .15 0.9 lipping 0.90.10DS.118 .5 .15 1.8 lipping 0.90.10DS.118 .5 .15 4.0 lipping 0.90.10DS.118 .5 .1 0.9 homogeneous 0.90.10DS.118 .5 .1 1.8 lipping 0.90.10DS.118 .5 .1 4.0 homogeneous 0.90.10DS.118 .5 .05 0.9 homogeneous 0.90.10DS.118 .5 .05 1.8 homogeneous 0.90.10DS.123 .5 .2 0.9 lipping 0.90.10DS.123 .5 .2 1.8 lipping 0.90.10DS.123 .5 .2 3.7 lipping 0.90.10DS.131 .5 .2 6.0 lipping 0.90.10DS.131 .5 .2 10.0 lipping 0.90.10DS.131 .5 .2 14.0 lipping 0.90.10DS.131 .5 .6 4.0 2 phase 0.90.15DS.132 .5 .2 4.0 lipping 0.95.5DS.130 .5 .2 4.0 homogeneous* 0.95.5DS.130 .5 .2 4.0 2 phase * The sample contained 10% by weight 12-200 mesh dolomite. EXAMPLE 8 A vicinal diol containing polymer is prepared as follows. 100 g of a 1% active solution of a copolymer of DMAEMA and acrylamide in equal mole percentages are adjusted to a pH of 10 with sodium hydroxide. This solution is reacted for one hour at ambient temperature with 0.15 g of glycidol. The resulting reaction mixture (gel) is crosslinkable with zirconium lactate and shows better thermal stability than the starting DMAEMA-acrylamide copolymer when crosslinked with zirconium lactate.

Claims: CLAIMS: 1. A method of preparing a water-soluble vinyl monomer containing a vicinal diol group, which method comprises reacting in an aqueous solution a water-soluble vinyl monomer containing a tertiary amine having the formula: EMI45.1 wherein R1 is hydrogen or methyl; Y is oxygen or NH; R3 and R4 are independently methyl or ethyl; and n is 2 or 3; with at least one reactive vicinal diol-forming or -containing compound selected from glycidol and the 3-halo-1,2-propanediols. 2. A method of preparing a water-soluble vinyl monomer containing a vicinal diol group which method comprises reacting in an aqueous solution a water-soluble vinyl monomer containing a tertiary amine salt and having the formula: EMI45.2 wherein R1 is hydrogen or methyl; Y is oxygen or NH; R3 and R4 are independently methyl or ethyl; n is 2 or 3; and X is a halogen, 1/2(SO4)=, CH3S04 , C2H3SO4 or CH3COO ; with at least one reactive vicinal diol 3 forming or -containing compound selected from glycidol and the 3-halo-1,2-propanediols. 3. A method according to claim 1 or 2, wherein R1 is methyl, R3 and R4 are each methyl, n is 3 and X is 1/2(SO4)=. 4. A method according to claim 1 or 2, wherein R1 ¯ is methyl, R3 and R4 are each methyl, n is 3 and X is Cl 5. A method according to claim 1,2,3 or 4, wherein R1 in said structural is methyl. 6. A method of treating a high temperature subterranean formation, which comprises contacting said formation with a highly viscous gel formed of an aqueous fluid, a water-soluble polymer containing crosslinkable vicinal diol groups and derived from a monomer made by the method of any of claims 1 to 5, and a crosslinking agent. 7. A method according to claim 6, wherein said water-soluble polymer is a copolymer or a terpolymer of said monomer with other monomer copolymerisable therewith. 8. A method according to claim 7, wherein said other monomer is one or more of N,N-dimethylacrylamide, acrylamide, methacrylamide, 2-acrylamido-2-methylpropanesulfonic acid, sodium styrene sulfonate, N-vinyl-2pyrrolidone and acrylic acid. 9. A method of claim 6,7 or 8, wherein said crosslinking agent is selected from water-soluble salts and complexes of multivalent cations. 10. A method according to any of claims 6 to 9, wherein said water-soluble polymer is a copolymer of MAPDMDHPAS and NNDMA, or of MAPDMDHPAC and NNDMA.

Inventors: CONWAY, MICHAEL WAYNE, HANLON, DAVID JAMES, HOLTMYER, MARLIN DEAN, HUNT, CHARLES VERNON
Applicants: HALLIBURTON COMPANY
Application year: 1987
Main classification: C09K7
IPC codes: C09K8, C08F20