Polymers containing malonic (meth)acrylamide units

Abstract: New homopolymers formed by malonic (met)acrylamide monomer units according to the following formula: wherein R is H or CH₃; X is H or an alcaline metal or NH₄; and copolymers formed by (met)acrylamide monomer units (I) and monomer units (II).

Description: This invention concerns new homopolymers formed by malonic (meth) acrylamide monomers of the following formula: wherein R is H or CH₃; X is H or alcaline metal, preferably sodium or potassium, or is NH₄; and copolymers formed by (meth)acrylamide monomer units (I) and monomer units (II), the molar ratio between units (I) and units (II) varying between 1:99 and 99:1. Acrylamide-type polymers are known in the art, said polymers containing units bearing radicals of monocarboxylic acids or hydroxylated alkyl radicals, linked with the amide nitrogen. As an example, English Patent GB1310613 describes homopolymers formed by units of N-carboxymethyl acrylamide or N,N di(carboxy methyl) acrylamide, useful to prevent the deposit of insoluble salts, particularly calcium salts on surfaces in contact with hot aqueous solutions. On the other hand, Patent GB1068037 describes copolymers having divalent and polyvalent metal-complexing properties, containing either units bearing N-carboxymethyl amides or N,N-dicarboxymethyl amides or units bearing N-hydroxyethyl amide groups. The document US-A-3,589,792 discloses diesters of dicarboxymethyl acrylamide, the corresponding diacids, and the polymers made therefrom, for use as water treatment agents: "boiler descalants, coagulants and chelants". The obtained polymer, however, bears ester groups, so that the obtention of the corresponding copolymer bearing free or salified carboxyls is compulsory subordinate to a saponification reaction. With this invention, new and effective polymers have been found, featuring the presence in the polymer chain of units responding to formula I, bearing a bicarboxylic acid radical linked with the amide nitrogen, viz. malonic acid. Such polymers, being homopolymers formed exclusively of formula I units or copolymers with (meth)acrylamide, can be effectively used in various sectors. As an example they may be used advantageously in water treatment, to eliminate and/or recover metals or to inhibit the formation of incrustations due to deposits of insoluble salts, for instance calcium salts. For that purpose those copolymers are used preferably with a molar ratio between formula (I) monomer units and (met)acrylamide monomer (II) units which varies between 70:30 and 99:1. Copolymers in this invention may also be used with flocculants to precipitate solids in aqueous suspension. Copolymers are then used preferably with a molar ratio of (I):(II) between 1:99 and 30:70. These may also be used in the paperboard industry and as components of adhesive mixtures. Both homopolymers and copolymers in this invention are water-soluble even in very high concentrations having an weight average molecular weight varying between 1000 and 20,000,000 preferably 1,000,000 to 10,000,000. These may be prepared by homopolymerisation of monomers according to the following formula: wherein: R is H or CH₃; X is H or an alcaline metal or NH₄; or in the case of copolymers, by copolymerisation of the above monomers with (meth)acrylamide, using the radical polymerisation methods known in present technique. Polymerisation may generally be effected by operating in solution, emulsion or suspension, and is preferably achieved in solution. An aqueous solution is used in practice, with a pH going from 2 to 10 approximately, using radical initiators, for instance peroxides, persulphates or nitrogen compounds. Homopolymers and copolymers in which X is alcaline metal or NH₄, may be obtained by polymerising relevant formula III monomers in which X is an alcaline metal or NH₄, or by polymerising the monomer in the acid form (X=H) and adding to the final polymer solution the inorganic base adapted to obtain the required salt, for instance NaOH, KOH or NH₄OH. In the same manner the copolymers in which X=H can be obtained by polymerising the relevant formula II monomer wherein X=H or by polymerising the monomer in salt form (X= alcaline metal, NH₄) then acidifying the polymer final solution, adding hydrochloric acid or sulphuric acid for instance. The temperature of the copolymerisation reaction may generally vary between ambient temperature (15°-25°C) and 90°C approximately and conversion of the monomers is practically completed within a period of 30 minutes to 24 hours depending on the temperature used, usual procedure generally featuring a 50°-70° temperature for a period of 1-2 hours. The molar ratio of the monomers thus introduced is also maintained unchanged in the final copolymer. Monomers complying with formula (III), used to produce polymers according to the present invention, are new and may be obtained quite simply according to known organic chemistry methodology. For example they are prepared by the reaction of 2-amino diethyl malonate dissolved in aqueous inorganic base, for example sodium hydroxyde, with acryloyl chloride or methacryloyl chloride, adding the chloride at low temperature, around 5°C, in the presence of polymerisation inhibitors, such as 3-methoxy phenol. The reaction occurs at ambient temperature and a high product yield is achieved. The following examples are for information purposes, and are not to be considered restrictive of the scope of the invention. EXAMPLE 1 Preparation of 2-acrylamide malonic acid (as in formula I:R, X=H). 10,5 g (0,05 moles) of 2-amino diethyl malonate are dissolved in 200 ml of 2N Na0H containing 50 mg of 3-methoxy phenol, a polymerisation inhibitor. 13,75 g (0,152 moles) of acryloyl chloride are then slowly added to the solution protected against the light and cooled to 5°C. On completion of the addition, the solution thus obtained is then kept stirred for one hour at ambient temperature, and on completion, extracted with ethyl acetate to remove any non-reacted acryloyl chloride. The aqueous phase, containing the bisodium 2-acrylamide malonic acid salt, is then passed over a column charged with a cationic resin DOWEX® H⁺ 50X8 to convert the product into the acid form and exclude excess soda. The fractions containing the product are then freeze-dried, thus obtaining 7.5 g of 2-acrylamide malonic acid, which represents an 87% yield. Product structure was confirmed by ¹HNMR spectroscope and mass spectrometer analyses. EXAMPLE 2 Using a 500 ml reactor with mechanical stirrer and condenser, 20 g (0,115 moles) of malonic 2-acrylamide acid and 200 ml of de-ionised water are added, and the pH is adjusted to pH 9 with a 2 N soda addition. The resulting solution is placed under nitrogen flow for 2 hours to eliminate any contained air; on completion it is heated to 60° and a slow addition is made of a solution of 31,1 mg (0,115 mmoles) of K₂S₂0₈ in 5 ml of de-ionised water. The mixture is then left to react 90 minutes at 60°C. It is finally cooled to ambient temperature, then diluted with de-ionised water and the polymer obtained in sodium salt form (as in formula I:X=Na) is recovered and purified by two successive precipitations with the addition of methanol at pH 10. After drying at reduced pressure, the product is 18 g of poles (sodium 2-acrylamide) a 90% conversion rate. The homopolymer weight average molecular weight thus obtained (assessed by GPC) is 2,700,000 g/mole. EXAMPLE 3 In a 500 ml reactor with mechanical stirrer and condenser, add 20 g (0,282 moles) of acrylamide, 1,50g (0,0087 moles) of 2-acrylamide malonic acid (equal to 97:3 molar ratio of acrylamide:2-acrylamide malonic acid), 200 ml of de-ionised water, then adding soda to adjust the pH to 9. The mixture is placed under nitrogen flow to remove any contained air; on completion it is heated to 60°C. A solution of 78,4 mg (0,29 mmoles) of K₂S₂0₈ in 5 ml of de-ionised water is quickly added and the reaction is allowed to continue for 75 minutes, the temperature being maintained at 60°C. On completion the mixture thus obtained is cooled to ambient temperature and the polymer is recovered and refined with two successive precipitations using methanol at pH 10. After drying under low pressure 20,7 g of copolymers are obtained representing a practically complete conversion of the monomers. The molar ratio between acrylamide and 2-acrylamide malonic acid units (in the form of bisodium salt) assessed by ¹³CNMR spectroscope analyses, was 97,1:2,9. The copolymer properties obtained were as follows: Weight average molecular weight (GPC): 3,300,000 g/mole Intrinsic viscosity (in aqueous 2M NaCl solution at 25°C): 802 cm³/g EXAMPLE 4 The procedure is as in example 3, with the exception that polymerisation is effected with a pH of 4, adding hydrochloric acid to the initial solution and the copolymer being recovered on completion by means of an addition of methanol at an acid pH. The monomer conversion rate is around 95% and the molar ratio between malonic acrylamide units and acrylamide units is practically equal with the input. The copolymer properties were as follows: Weight average molecular weight: 3,400,000 g/mole Intrinsic viscosity: 795 cm³/g EXAMPLE 5 The procedure is as described in example 3, with the exception that the input features a molar ratio of 2-acrylamide malonic acid : acrylamide representing 5:95 and that the polymerisation time is 1 hour. The monomer conversion rate is around 90% and properties of the copolymer obtained are as follows: Molar ratio between 2-acrylamide malonic units and acrylamide units: 5:95; Weight average molecular weight: 3,600,000 g/mole Intrinsic viscosity: 802 cm³/g EXAMPLE 6 The procedure is as described in example 5, with the exception that the polymerisation is effected at pH 4. The copolymer is obtained in the form of sodium salt, by the addition of 2N Na0H to the final solution and precipitation with methanol. The monomer conversion rate is around 90% and the properties of the copolymer obtained are as follows: Molar ratio between 2-acrylamide malonic units and acrylamide units: 4,4 : 95,6 Weight average molecular weight: 3,900,000 g/mole Intrinsic viscosity: 970 cm³/g

Claims: Claims for the following Contracting States : FR, GB, NL, DK Homopolymers formed by monomer units complying with the following formula: wherein R is H or CH₃; X is H or an alcaline metal, or NH₄; and copolymers formed by monomer (I) units and monomer (II) units of acrylamide or methacrylamide, the molar ratio of units (I) to units (II) varying between 1:99 and 99:1. Homopolymers and copolymers according to claim 1, characterised in that their weight average molecular weight goes from 1000 to 20,000,000 Homopolymers and copolymers according to claim 2, characterised in that their weight average molecular weight goes from 1,000,000 to 20,000,000 Copolymers according to claim 1, characterised in that the molar ratio of units (I) to units (II) varies between 70:30 and 99:1 Copolymers according to claim 1, characterised in that the molar ratio of units (I) to units (II) varies between 1:99 and 30:70 Homopolymers and copolymers according to claim 1, characterised in that the alcaline metal is sodium or potassium. Compounds according to the following formula: wherein R is H or CH₃; X is H or an alcaline metal, or NH₄. Claims for the following Contracting State : ES Process for preparing homopolymers and copolymers characterized in that said homopolymers are formed by radical homopolymerization of monomer units complying with the following formula: wherein R is H or CH3 , X is H or an alkaline metal or NH4; and said copolymers are formed by radical copolymerization of the monomer units (III) and monomer units (II) of acrylamide or methacrylamide, the molar ratio of unit (III) to units (II) varying between 1,99 and 99,1. Process according to claim 1, characterised in that the weight average molecular weight of said homopolymers and copolymers goes from 1000 to 20,000,000 Process according to claim 2, characterised in that the weight average molecular weight of said homopolymers and copolymers goes from 1,000,000 to 20,000,000 Process according to claim 1, characterised in that the molar ratio of units (III) to units (II) varies between 70:30 and 99:1 Process according to claim 1, characterised in that the molar ratio of units (III) to units (II) varies between 1:99 and 30:70 Process according to claim 1, characterised in that the alcaline metal is sodium or potassium.

Inventors: BONACCORSI FABRIZIO, LOCKHART THOMAS PAUL, PAPPA ROSARIO, RIOCCI MARIO, ROGGERO ARNALDO, BONACCORSI, FABRIZIO, LOCKHART, THOMAS PAUL, PAPPA, ROSARIO, RIOCCI, MARIO, ROGGERO, ARNALDO
Applicants: AGIP SPA, ENIRICERCHE SPA, AGIP S.P.A., ENIRICERCHE S.P.A.
Application year: 1990
Main classification: C08F20
IPC codes: C08F20, C07C233