Polymerization of acrylic acid and derivatives thereof

Abstract: Acrylic acid or water-soluble derivatives thereof can be polymerized effectively in a short time using as a polymerization initiator an inorganic acid salt or organic acid salt of 2,2'-azobis(2-methyl-propionamidoxime).

Description: BACKGROUND OF THE INVENTION This invention relates to a process for producing a homopolymer or copolymer of acrylic acid or a water-soluble derivative thereof. More in detail, the present invention relates to a process for producing a homopolymer or copolymer of acrylic acid or a water-soluble derivative thereof using a special polymerization initiator in a short time with high efficiency. Water-soluble vinyl homopolymers and copolymers such as poly(acrylic acid) or salts thereof, polyacrylamide and polyvinylpyrrolidone, e.g., have been noticed for their utilities. For example, polyacrylates and copolyacrylates are widely used, for example, as a thickener, a flocculant, a highly water-absorbing resin which is used in large amounts for disposal diaper, e.g. Acrylamide polymers are widely used, for example, as a flocculant, a thickener, a yield improving agent for paper-making, a fluidity adjusting agent for oil salvage, e.g. Such water-soluble homopolymers and copolymers used for such purposes have been obtained by homopolymerizing or copolymerizing acrylic acid, acrylamide, or derivatives thereof as a monomer or monomers in an aqueous solution or a suspension of water and water-insoluble organic solvent using a redox polymerization initiator which is a combination of an oxidizing agent (e.g. a peroxide) and a reducing agent, a peroxide polymerization initiator such as benzoyl peroxide, lauroyl peroxide or potassium persulfate, e.g., an azo polymerization initiator such as 2,2'-azobis(2-amidinopropane)dihydrochloride, e.g. But these known polymerization processes have various problems therein. For example, in the case of using the redox polymerization initiator and the peroxide polymerization initiator, since peroxides per se used therein are generally unstable for impact or heating, e.g., there is a danger of fire and explosion, e.g., during the storage of the peroxides or at the time of polymerization. Further, many problems also arise when applied to industrial production, for example, a long time being necessary for polymerization due to a long induction period, the temperature control at the time of reaction being difficult due to easy self-induced decomposition, e.g. In addition, according to the polymerization process using such polymerization initiators, since the polymer obtained has a small molecular weight, there is a problem of failing to obtain a sufficient aggregating effect when used as a flocculant. On the other hand, in a process using an azo polymerization initiator such as 2,2'-azobis(2-amidinopropane) dihydrochloride, there is a merit of easy temperature control due to precise primary decomposition, not showing self-induced decomposition unlike the peroxides, but there is also a problem of easily bringing about the so-called dead-end phenomenon wherein the polymerization is stopped due to consumption of the polymerization initiator during the polymerization under preferable polymerization conditions. As azo polymerization initiators, the use of 2,2'-azobis(2-methylpropionamidoxime) is disclosed, for example, in Japanese Patent Unexamined Publication (JP-A) Nos. 62-172007, and 61-223009 (=EP 196588), U.S. Patent Nos. 4,528,347, and 4,644,042 (=JP-A 61-60707) for polymerization of monoallylamine (CH 2 = CHCH 2 NH 2 ) which is a basic allyl compound and in U.S.S.R. SU 927,802 for polymerization of acrylonitrile, which is not water-soluble. No prior art reference discloses the use of such an azo initiator for polymerization of acidic or neutral water-soluble vinyl compounds such as acrylic acid or acrylamide, e.g. SUMMARY OF THE INVENTION It is an object of the present invention to provide a process for producing a homopolymer or copolymer of acrylic acid or a water-soluble derivative thereof efficiently in a short time overcoming the problems of the redox polymerization initiators and peroxide polymerization initiators which cause a danger of explosion, self-induced decomposition at the time of polymerization, and also overcoming the problems of the dead-end phenomenon caused by the use of azo polymerization initiators such as 2,2'-azobis(2-amidinopropane) dihydrochloride, e.g. It is another object of the present invention to provide a water-soluble polymerization initiator used therein. The present invention provides a process for producing a homopolymer or copolymer of acrylic acid or a water-soluble derivative thereof, which comprises polymerizing a monomer or monomers selected from acrylic acid and water-soluble derivatives thereof in the presence of a catalytic amount of a polymerization initiator selected from (a) an inorganic acid salt and/or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime), (b) a mixture of 2,2'-azobis(2-methylpropionamidoxime) and an inorganic acid and/or organic acid, and (c) 2,2'-azobis(2-methylpropionamidoxime) when acrylic acid and/or a water-soluble derivative thereof showing acidity by itself is used as a monomer or monomers. As foreshadowed as a polymerization initiator there can be used an inorganic acid salt or an organic acid salt or a mixture of inorganic acid salt and organic acid salt of 2,2'-azobis(2-methylpropionamidoxime). The present invention also provides an inorganic acid salt or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime) obtained by reacting 2,2'-azobis (2-methylpropionamidoxime) with an inorganic acid or an organic acid having a pKa of 4.25 or less at 25°C, in an amount of 1 to 3 equivalents in a solvent. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a graph showing conversion-polymerization time curves obtained in Example 1 and Comparative Example 3. Fig. 2 is a graph showing conversion-polymerization time curves obtained in Examples 2, 3 and 4, and Comparative Example 4. Fig. 3 is a graph showing conversion-polymerization time curves obtained in Examples 5 and 6, and Comparative Examples 5 and 6. DESCRIPTION OF THE PREFERRED EMBODIMENTS The present inventors studied polymerization initiators for obtaining homopolymers and copolymers of acrylic acid and water-soluble derivatives thereof effectively in a short time using an azo polymerization initiator which is slight in danger of explosion and hardly causes self-induced decomposition during the polymerization, and is free from the dead-end phenomenon in contrast to the use of 2,2'-azobis(2-amidinopropane) dihydrochloride, and accomplished the present invention. One of the polymerization initiators used in the present invention is an inorganic or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime). It is possible to obtain 2,2'-azobis(2-methyl-propionamidoxime) for example, by reacting azobisisobutyronitrile (AIBN) with hydroxylamine in water (disclosed in U.S.S.R. Patent No. 301329), or reacting AIBN with hydroxylamine in ethanol as a solvent (Polish Patent No. 104742). Further, 2,2'-azobis(2-methyl-propionamidoxime) can be produced by reacting AIBN with hydroxylamine in an amount of 1 to 3 equivalent in dimethylsulfoxide (DMSO), N-methyl-2-pyrrolidone (NMP), or a solvent containing DMSO or NMP as a major component at 20° to 40°C for 4 to 8 hours (developed by the present inventors). Inorganic or organic acid salts of 2,2'-azobis(2-methylpropionamidoxime) can be produced by reacting 2,2'-azobis(2-methylpropionamidoxime) with an inorganic acid or organic acid having a pKa of 4.25 or less at 25°C in an amount of 1 to 3 equivalent in a solvent such as a lower alcohol, e.g. methanol, ethanol, isopropanol, or water, at 10° to 40°C for 1 to 10 hours. When the acid does not have a pKa of 4.25 or less at 25°C (e.g. acetic acid), it is impossible to obtain the desired salt of 2,2'-azobis(2-methylpropionamidoxime). As the inorganic acid, there can be used hydrochloric acid, sulfuric acid and phosphoric acid, e.g. As the organic acid, there can be used organic sulfonic acids such as methanesulfonic acid and p-toluenesulfonic acid, e.g.; carboxylic acids such as trifluoroacetic acid, oxalic acid, succinic acid, citric acid, tartaric acid, malic acid, glycolic acid and malonic acid, e.g. These acids can be used singly or as a mixture thereof. In some cases, the inorganic or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime) can be replaced by a mixture of 2,2'-azobis(2-methylpropionamidoxime) and an acid in an aqueous solution. As the acid, there is no particular limitation so long as an acid has a function for enhancing water-solubility of 2,2'-azobis(2-methylpropionamidoxime). Preferable examples of the acid are inorganic acids such as hydrochloric acid, sulfuric acid and phosphoric acid, e.g.; organic sulfonic acids such as methanesulfonic acid, p-toluenesulfonic acid, e.g.; carboxylic acids such as acetic acid, trifluoroacetic acid, oxalic acid, succinic acid, citric acid, tartaric acid, malic acid, glycolic acid and malonic acid, e.g. These acids can be used singly or as a mixture thereof. By adding an acid (preferably in an amount of 0.5 to 50, more preferably 1 to 20 equivalent) to 2,2'-azobis(2-methylpropionamidoxime) in the polymerization system, it seems to cause the same effects as the case of using the inorganic or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime). When monomer or monomers to be polymerized show acidity by themselves, e.g. acrylic acid, methacrylic acid and 2-acrylamide-2-methylpropanesulfonic acid, it is not necessary to add an acid to the reaction system. As the monomer to be polymerized, there can be used acrylic acid and water-soluble derivatives thereof such as acrylamide, methacrylamide, N-methylolacrylamide, N-methylolmethacrylamide, methacrylic acid, 2-acrylamide-2-methylpropanesulfonic acid, and salts thereof e.g. alkali metal (Na, K, Li) or ammonium salts thereof; dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate, N-dimethylaminopropylacrylamide, N-dimethylaminopropylmethacrylamide, or acid addition salts thereof wherein the acid is an inorganic acid such as HCl or H 2 SO 4 , e.g., or an organic acid such as acetic acid or p-toluenesulfonic acid, e.g., or quaternary salts thereof. These monomers can be used singly (to obtain homopolymers) or as a mixture thereof (to obtain copolymers). Among these monomers, the use of acrylic acid, methacrylic acid, acrylamide, and methacrylamide, is preferable. It is possible to use one or more comonomers which can be copolymerizable with the monomers mentioned above, for example, N,N'-methylenebisacrylamide, N,N'-methylenebismethacrylamide, trimethylolpropane diallyl ether, trimethylolpropane diacrylate, and oil-soluble monomers such as styrene or methyl methacrylate, e.g. in amounts not to give undesirable influences to the copolymerization. The concentration of the monomer such as acrylic acid or a water-soluble derivative thereof in the polymerization solution is not particularly limited so long as there is no trouble in the polymerization. From the viewpoint of exothermic heat at the time of polymerization and temperature control thereof and economy at the time of isolation of the obtained polymer, the concentration of 5 to 80% by weight/weight (w/w) is preferable and 10 to 50% by w/w is more preferable. The amount of the polymerization initiator is sufficient when the polymerization can be carried out desirably (i.e. the catalytic amount). Too low amount is undesirable due to too slow polymerization. On the other hand, too much amount is undesirable for lowering the conversion or making the temperature control difficult. Usually the inorganic or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime) is used in an amount of 0.001 to 5% by weight, preferably 0.01 to 2% by weight, based on the weight of the monomer or monomers. The polymerization can be carried out at a temperature below the boiling point of water, usually at 30° to 80°C, preferably 50° to 70°C, for 3 to 10 hours. The polymerization time can be changed depending on reaction conditions such as the polymerization temperature, the kind of monomer or monomers to be polymerized or the concentration of polymerization initiator, e.g. As the polymerization method, there can preferably be used reverse-phase suspension polymerization or aqueous solution polymerization, e.g. For example, the polymerization can be carried out by placing a monomer or monomers (e.g. acrylic acid, a water-soluble derivative thereof, and if necessary, other comonomer or comonomers) in a solvent (e.g. water, a mixed solvent of water and a water-soluble organic solvent), and polymerizing the monomer or monomers in the presence of a catalytic amount of an inorganic or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime), or a mixture of a catalytic amount of 2,2'-azobis(2-methylpropionamidoxime) and an acid in a nitrogen stream according to a conventional process. As the water-soluble organic solvent, there can be used water-soluble alcohols such as methanol or ethanol, e.g.; water-soluble cyclic ethers such as tetrahydrofuran (THF) or dioxane, e.g. ; acetone and dimethylsulfoxide (DMSO), e.g. The obtained homopolymer or copolymer can be isolated by a conventional process. The present invention is illustrated by way of the following Examples. Reference Example 1 To 100 ml of dimethylsulfoxide (DMSO), 32.8 g of azobisisobutyronitrile (AIBN) and 31.7 g of aqueous solution of 50% hydroxylamine were added and reacted at 30°C for 8 hours with stirring. After allowed to stand overnight, 115 ml of water was added to the reaction solution. Deposited crystals were filtered, washed with water and then methanol and dried to give 44.6 g of white 2,2'-azobis(2-methylpropionamidoxime) (yield 97.0%). The obtained 2,2'-azobis(2-methylpropionamidoxime) was subjected to analysis using high performance liquid chromatography (HPLC) [apparatus: 600 type, mfd. by Waters Co., Ltd.; column: wakosil™, a trade name, mfd. by Wako Pure Chemical Industries, Ltd., 5C18 4.6 mm in diameter and 150 mm long; eluent: tetra-n-butylammonium hydroxide 0.005 M, sodium 1-octane-sulfonate 0.005 M, pure water 860 ml and acetonitrile 140 ml were mixed, and dissolved, followed by adjustment of pH to 4.00 using phosphoric acid; flow rate of eluent: 1.0 ml/min]. The content of 2,2'-azobis(2-methylpropionamidoxime) was 99.1%. Reference Example 2 The process of Reference Example 1 was repeated in the same manner as described in Reference Example 1 except for using 100 ml of N-methyl-2-pyrrolidone (NMP) in place of DMSO to give 43.4 g of 2,2'-azobis(2-methylpropionamidoxime) (yield 94.4%). After subjected to analysis using HPLC in the same manner as described in Reference Example 1, the content of 2,2'-azobis(2-methylpropionamidoxime) was 98.1%. Synthesis Example 1 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) dihydrochloride To 450 ml of methanol, 90.1 g of 2,2'-azobis(2-methylpropionamidoxime) was added, followed by addition of a solution obtained by dissolving 37.2 g of hydrogen chloride gas in 50 ml of methanol to carry out the reaction at room temperature for 2 hours with stirring. After the reaction, the methanol was removed by distillation. The residue was purified with water-acetone to give 104.2 g of 2,2'-azobis(2-methylpropionamidoxime) dihydrochloride (yield 87.8%), having a melting point (m.p.) of 139°C (decomposed). IR (KBr) υ cm -1 : 1660 (C=N-) 1 HNMR δ ppm (D 2 O): 1.46 (12H, s, C H 3 ) UV (H 2 O): λmax 365 nm (ε=23.8) Synthesis Example 2 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) disuccinate To 50 ml of ethanol, 4.7 g of succinic acid [pKa = 4.207 (pK 1 ) (25°C)] and 2.3 g of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 30°C for 3.5 hours. After the reaction, deposited crystals were filtered, washed with 10 ml of ethanol and dried to give 3.46 g of 2,2'-azobis(2-methylpropionamidoxime) disuccinate (yield 74.3%) having a m.p. of 126.5°C (decomposed). IR (KBr) υ cm -1 : 1710 (C=O), 1640 (C=N-) 1 HNMR δ ppm (D 2 O): 1.47 (12H, s, C H 3 ), 2.59 (8H, s, C H 2 ) UV (H 2 O): λmax 365 nm (ε=26.6) Synthesis Example 3 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) dicitrate To 60 ml of isopropanol, 7.7 g of citric acid [pKa = 3.128 (pK 1 ) (25°C)] and 2.3 g of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 25°C for 6.5 hours with stirring. After the reaction, deposited crystals were filtered, washed with 10 ml of ethanol, and dried to give 5.43 g of 2,2'-azobis(2-methylpropionamidoxime) dicitrate (yield 88%) having a m.p. of 122.5°C (decomposed). IR (KBr) υ cm -1 : 1720 (C=O), 1640 (C=N-) 1 HNMR δ ppm (D 2 O): 1.52 (12H, s, C H 3 ), 2.75 - 2.95 (8H, d x 2, C H 2 ) UV (H 2 O): λmax 365 nm (ε=26.7) Synthesis Example 4 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) dioxalate To 30 ml of methanol, 2 g of oxalic acid [pKa = 1.271 (25°C)] and 2.3 g of 2,2'-azobis(2-methyl-propionamidoxime) were added and reacted at 30°C for 1.5 hours with stirring. After the reaction, deposited crystals were filtered, washed with 10 ml of methanol, and dried to give 3.75 g of 2,2'-azobis(2-methyl-propionamidoxime) dioxalate (yield 91.5%) having a m.p. of 146.5°C (decomposed). IR (KBr) υ cm -1 : 1700 (C=O), 1625 (C=N-) 1 HNMR δ ppm (D 2 O): 1.53 (12H, s, C H 3 ) UV (H 2 O): λmax 366 nm (e=23.9) Synthesis Example 5 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) monotartarate To 50 ml of ethanol, 6.0 g of tartaric acid [pKa = 3.831 (pK 1 ) (25°C)] and 2.3 g of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 30°C for 5 hours with stirring. After the reaction, deposited crystals were filtered, washed with 10 ml of ethanol, and dried to give 2.96 g 2,2'-azobis(2-methylpropionamidoxime) monotartarate (yield 77.9%) having a m.p. of 112°C (decomposed). IR (KBr) υ cm -1 : 1710 (C=O), 1660 (C=N-) 1 HNMR δ ppm (D 2 O): 1.49 (12H, s, C H 3 ), 4.45 (2H, s, C H ) UV (H 2 O): λmax 365 nm (ε=27.6) Synthesis Example 6 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) dimalate To 50 ml of ethanol, 5.36 g of malic acid [pKa = 3.40 (pK 1 ) (25°C)] and 2.3 g of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 30°C for 4 hours with stirring. After the reaction, deposited crystals were filtered, washed with 10 ml of ethanol and dried to give 4.21 g of 2,2'-azobis(2-methylpropionamidoxime) dimalate (yield 84.6%) having a m.p. of 116°C (decomposed). IR (KBr) υ cm -1 : 1710 (C=O), 1650 (C=N-) 1 HNMR δ ppm (D 2 O): 1.50 (12H, s, C H 3 ), 2.65 - 2.89 (4H, m, C H 2 ), 4.41 - 4.46 (2H, m, C H ) UV (H 2 O): λmax 365 nm (e=27.6) Synthesis Example 7 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) di-p-toluenesulfonate To 100 ml of ethanol, 19 g of p-toluene-sulfonic acid [pKa = 1.7 (25°C)] and 11.5 g of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 25°C for 3 hours with stirring. After the reaction, the ethanol was removed by distillation under reduced pressure. The residue was washed with 300 ml of acetone and dried to give 26.8 g of 2,2'-azobis(2-methylpropionamidoxime) di-p-toluenesulfonate (yield 93.2%) having a m.p. of 130°C (decomposed). IR (KBr) υ cm -1 : 1210 (-SO 3 H), 1460 (C 6 H 4 ), 1670 (C=N-) 1 HNMR δ ppm (D 2 O): 1.41 (12H, s, C H 3 ), 2.27 (6H, s, -C H 3 ), 7.11 (4H, d, Ar-H(o-)), 7.49 (4H, d, Ar-H(m-)) UV (H 2 O): λmax 365 nm (ε=23.7) Synthesis Example 8 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) dimethanesulfonate To 125 ml of ethanol, 9.6 g (0.1 mole) of methanesulfonic acid and 11.5 g (0.05 mole) of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 20-25°C for 4 hours with stirring. After the reaction, deposited crystals were filtered, washed with ethanol, and then acetone, and dried under reduced pressure to give 19.4 g of white 2,2'-azobis(2-methylpropionamidoxime) dimethanesulfonate (yield 91.8%) having a m.p. of 135°C (decomposed). IR (KBr) υ cm -1 : 1709 (C=O), 1647 (C=N-) 1 HNMR δ ppm (D 2 O): 1.55 (12H, s, C-C H 3 ), 2.49 (6H, s, S-C H 3 ) UV (H 2 O): λmax 365 nm (e=24.1) Synthesis Example 9 Synthesis of 2,2'-azobis(2-methylpropionamidoxime) diglycolate To 125 ml of ethanol, 7.6 g (0.1 mole) of glycolic acid [pKa = 3.831 (25°C)] and 11.5 g (0.05 mole) of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 20°C for 4 hours with stirring. After the reaction, deposited crystals were filtered, washed with ethanol, and then acetone, and dried under reduced pressure to give 16.6 g of white 2,2'-azobis(2-methylpropionamidoxime) diglycolate (yield 86.8%) having a m.p. of 125°C (decomposed). IR (KBr) υ cm -1 : 1716 (C=O), 1664 (C=N-) 1 HNMR δ ppm (D 2 O): 1.34 (12H, s, C H 3 ), 3.99 (4H, s, C H 2 ) UV (H 2 O): λmax 365 nm (ε=31.1) Reference Examples 3 and 4 To 125 ml of ethanol, 6.0 g (0.1 mole) of acetic acid [pKa = 4.756 (25°C)] or 7.2 g (0.1 mole) of acrylic acid [pKa = 4.26 (25°C)] and 11.5 g (0.05 mole) of 2,2'-azobis(2-methylpropionamidoxime) were added and reacted at 20°C for 4 hours with stirring. After the reaction, the same after-treatment as in Synthesis Examples 1 to 9 was carried out to give white powders. In any cases, the obtained compound was 2,2'-azobis(2-methylpropionamidoxime) (free form), and a salt of 2,2'-azobis(2-methylpropionamidoxime) was not isolated. Example 1 To 380 g of deionized water, 20 g of acrylamide and 0.01 g of 2,2'-azobis(2-methylpropionamidoxime) dihydrochloride were added and polymerized at 50°C in a nitrogen atmosphere. The results are shown in Table 1. In Fig. 1, the results of Table 1 are shown by a conversion-polymerization time curve (-O-). Comparative Example 1 The process of Example 1 was repeated except for using 0.01 g of 2,2'-azobis(2-amidinopropane) dichloride (V-50, a trade name, mfd. by Wako Pure Chemical Industries, Ltd.) in place of 2,2'-azobis(2-methylpropionamidoxime) dihydrochloride. The results are shown in Table 1. In Fig. 1, the results of Table 1 are shown by a conversion-polymerization time curve (--). Polymerization time (hrs) 0.5 1.0 1.5 2.0 3.0 4.0 5.0 6.0 Example 1 26.0 43.5 54.4 66.7 78.5 83.5 82.7 87.6 Comparative Example 1 14.9 33.3 47.4 53.8 66.2 67.9 68.1 68.0 In Table 1, values are conversion (%) per unit time. As is clear from the results of Table 1 and Fig. 1, when V-50 is used as the polymerization initiator, the phenomenon of dead-end (i.e. saturation of polymerization) is observed after about 3 hours from the beginning of polymerization. In contrast, according to the process of the present invention, no dead-end phenomenon takes place and acrylamide can be polymerized effectively in a short time. Example 2 To 380 g of deionized water, 20 g of acrylamide, 0.01 g of 2,2'-azobis(2-methylpropionamidoxime) and 0.0052 g of acetic acid were added and polymerized at 50°C in a nitrogen atmosphere. The results are shown in Table 2. In Fig. 2, the results of Table 2 are shown by a conversion-polymerization time curve (-O-). Example 3 The process of Example 2 was repeated except for using 0.05 g of acetic acid in place of 0.0052 g of acetic acid. The results are shown in Table 2. In Fig. 2, the results of Table 2 are shown by a conversion-polymerization time curve (-Δ-). Example 4 The process of Example 2 was repeated except for using 0.0052 g of sulfuric acid in place of acetic acid. The results are shown in Table 2. In Fig. 2, the results of Table 2 are shown by a conversion-polymerization time curve (-□-). Comparative Example 2 The process of Example 2 was repeated except for not using acetic acid. The results are shown in Table 2. In Fig. 2, the results of Table 2 are shown by a conversion-polymerization time curve (--). Polymerization time (hrs) 0.5 1.0 1.5 2.0 3.0 4.0 5.0 6.0 Example 2 25.8 44.7 57.9 67.5 75.8 82.4 84.6 85.4 Example 3 36.4 59.4 72.2 80.4 83.8 89.4 93.3 93.1 Example 4 36.1 59.3 69.5 75.6 83.9 88.9 90.2 91.4 Comparative Example 2 0 0 1.9 3.8 5.2 5.8 6.5 7.8 In Table 2, values are conversion (%) per unit time. As is clear from the results of Table 2 and Fig. 2, when 2,2'-azobis(2-methylpropionamidoxime) is used together with an acid, acrylamide can be polymerized effectively in a short time as in the case of Example 1. Example 5 To 360 g of deionized water, 40 g of acrylic acid and 0.0085 g (3.7 x 10 -5 mole) of 2,2'-azobis(2-methylpropionamidoxime) were added and polymerized at 50°C in a nitrogen atmosphere. The results are shown in Table 3. In Fig. 3, the results of Table 3 are shown by a conversion-polymerization time curve (-O-). Example 6 The process of Example 5 was repeated except for using 0.0112 g (3.7 x 10 -5 mole) of 2,2'-azobis(2-methylpropionamidoxime) dihydrochloride in place of 0.0085 g (3.7 x 10 -5 mole) of 2,2'-azobis(2-methylpropionamidoxime). The results are shown in Table 3. In Fig. 3, the results of Table 3 are shown by a conversion-polymerization time curve (-Δ-). Comparative Example 3 The process of Example 5 was repeated except for using 0.01 g (3.7 x 10 -5 mole) of V-50 in place of 2,2'-azobis(2-methylpropionamidoxime). The results are shown in Table 3. In Fig. 3, the results of Table 3 are shown by a conversion-polymerization time curve (--). Comparative Example 4 The process of Example 5 was repeated except for using 0.01 g (3.7 x 10 -5 mole) of potassium persulfate in place of 0.0085 g (3.7 x 10 -5 mole) of 2,2'-azobis(2-methylpropionamidoxime). The results are shown in Table 3. In Fig. 3, the results of Table 3 are shown by a conversion-polymerization time curve (-□-). Polymerization time (hrs) 0.5 1.0 1.5 2.0 3.0 4.0 5.0 6.0 Example 5 32.5 50.0 61.5 69.0 78.3 84.1 87.6 89.2 Example 6 28.9 47.1 57.6 66.3 75.2 82.4 86.8 88.0 Comparative Example 3 22.4 40.1 52.0 59.9 71.2 77.3 81.1 83.9 Comparative Example 4 7.7 16.0 21.6 27.4 37.4 46.1 52.5 59.6 In Table 3, values are conversion (%) per unit time. As is clear from Table 3 and Fig. 3, acrylic acid can be polymerized effectively in a short time according to the process of the present invention compared with the cases of using V-50 and potassium persulfate as a polymerization initiator. Example 7 To 380 g of deionized water, 20 g of acrylamide and 3.7 x 10 -5 mole of 2,2'-azobis(2-methylpropionamidoxime) disuccinate were added and polymerized at 50°C in a nitrogen atmosphere. The results are shown in Table 4. Examples 8 to 14 The process of Example 7 was repeated except for using various salts of 2,2'-azobis(2-methyl-propionamidoxime) as listed in Table 4 in place of 2,2'-azobis(2-methylpropionamidoxime) disuccinate. The results are shown in Table 4. As is clear from the results of Table 4, acrylamide can be polymerized effectively in a short time by using various acid salts of 2,2'-azobis(2-methylpropionamidoxime). As mentioned above, acrylic acid and water-soluble derivatives thereof can be homopolymerized or copolymerized effectively in a short time by using an inorganic or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime) as a polymerization initiator or a mixture of 2,2'-azobis(2-methylpropionamidoxime) and an inorganic acid or organic acid. Further, according to the present invention, since an amidoxime group can be introduced into a terminal of polymer, the resulting polymer can have a function as a metal chelate.

Claims: A process for producing a homopolymer or copolymer of acrylic acid or a water-soluble derivative thereof, which comprises polymerizing a monomer or monomers selected from acrylic acid and water-soluble derivatives thereof in the presence of a catalytic amount of a polymerization initiator selected from (a) an inorganic acid salt and/or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime), (b) a mixture of 2,2'-azobis(2-methylpropionamidoxime) and an inorganic acid and/or organic acid, and (c) 2,2'-azobis(2-methylpropionamidoxime) when acrylic acid and/or a water-soluble derivative thereof showing acidity by itself is used as a monomer or monomers. A process according to Claim 1, wherein acrylic acid, methacrylic acid, acrylamide or methacrylamide is polymerized. A process according to claim 1, wherein the water-soluble derivative of acrylic acid is acrylamide, methacrylamide, N-methylolacrylamide, N-methylolmethacrylamide, methacrylic acid, 2-acrylamide-2-methylpropanesulfonic acid, alkali metal salts thereof, ammonium salts thereof, dimethylaminoethyl acrylate, dimethylaminoethyl methacrylate, N,N-dimethylaminopropylacrylamide, N,N-dimethylaminopropyl-methacrylamide, acid addition salts thereof or quaternary salts thereof. A process according to any preceding claim wherein the polymerization initiator is obtained by reacting 2,2'-azobis(2-methylpropionamidoxime) with an inorganic acid and/or an organic acid having a pKa of 4.25 or less at 25°C, in an amount of 1 to 3 equivalents in a solvent. A process according to any preceding claim wherein the inorganic acid is hydrochloric acid, sulfuric acid or phosphoric acid. A process according to any preceding claim wherein the organic acid is methanesulfonic acid, p-toluenesulfonic acid, trifluoracetic acid, oxalic acid, succinic acid, citric acid, tartaric acid, malic acid, glycolic acid or malonic acid. A process according to any one of preceding claims 1-4, wherein the initiator is the initiator defined in part (b) of claim 1 and wherein the organic acid is acetic acid. An inorganic acid salt or organic acid salt of 2,2'-azobis(2-methylpropionamidoxime) obtained by reacting 2,2'-azobis (2-methylpropionamidoxime) with an inorganic acid or an organic acid having a pKa of 4.25 or less at 25°C, in an amount of 1 to 3 equivalents in a solvent. An inorganic acid salt or organic acid salt according to claim 8, wherein the inorganic acid is hydrochloric acid or the organic acid is succinic acid, citric acid, oxalic acid, tartaric acid, malic acid, p-toluenesulfonic acid, methanesulfonic acid or glycolic acid.

Inventors: ITO TOSHIYASU, KOJIMA YUTAKA, TAKEUCHI HIDEO, ITO, TOSHIYASU, KOJIMA, YUTAKA, TAKEUCHI, HIDEO, ITO, TOSHIYASU, C/O TOKYO KENKYUSHO, KOJIMA, YUTAKA, C/O HARIMA KOJO, TAKEUCHI, HIDEO, C/O TOKYO KENKYUSHO
Applicants: WAKO PURE CHEM IND LTD, WAKO PURE CHEMICAL INDUSTRIES, LTD
Application year: 1995
Main classification: C08F20
IPC codes: C07C245, C08F4, C08F20