Imported: 13 Feb '17 | Published: 18 Jan '11
USPTO - Utility Patents
Grafted polymers which are the reaction products of:
The present application claims priority under 35 U.S.C. Section 119 of EP07000741.4 filed Jan. 16, 2007, the contents of which are incorporated herein by reference in its entirety.
The present invention relates to the area of polymers and refers to novel grafted polymers, a process for their production and their use as super-plasticizers for concrete or plaster retarders.
Polyolefinic acids, particularly polyacrylic acids, grafted with polyglycolethers and monomethylpolyglycolethers (MPEG) and their use as super-plasticizers are well known from literature. They provide high fluidity to high-strength cement and concrete compositions combined with an extremely low water-to-cement or concrete ratio. In addition they reduce the decrease in fluidity, which takes place after a certain time, and control the generation of foam during the making of the final preparations. Examples for the state of the art can be found inter alia in FR 2776285 B1 (Chryso), EP 1260536 A1 (BASF) or WO 97/039037 A1 (Mbt). Usually, manufacture of the grafted polymers takes place in two steps: firstly, the free-radical polymerization is carried out in water, and then the esterification is conducted. Of course, prior to esterification the water has to be removed, which makes the process time-consuming and not very efficient.
In this context, reference is also made to international patent application WO 06/050850 A1 (Cognis) disclosing anionic polymers useful as super-plasticizers for concrete, which are obtained by polymerization of (meth)acrylic acid or their esters with dipropylendiglycolacrylate (DPGDA), tripropylenglycoldiacrylate (TPGDA), acrylamidomethyl propanesulfonic acid (AMPS) and/or acryl acetate (AA) and subsequent treatment of the intermediates with mixtures of short- and long-chain alkylpolyalkyleneglycols. Another group of concrete plasticizers obtained from the polymerization of maleic acid (anhydride) and (meth)acrylic acid is known from EP 1319676 A1 (Cognis). Polyacrylic acids grafted by polyethyleneglycols and their use as superplasticizers for concrete is also known from EP 1396506 A1 (Cognis). Finally, WO 97/39037 A1 (Sandoz) describes the use of a styrene/maleic acid anhydride co-polymer, post-esterified with a mono-methoxy polyglycol ether for the same purpose; the maleate moiety, however, has a symmetric structure. Nevertheless, none of the polymers known from the state of the art simultaneously fulfil all requirements of the proposed application.
Therefore, the present invention is directed to providing novel polymers with improved super-plasticizing and retarding properties in order to overcome the disadvantages known from the state of the art. In particular, the polymers of the invention provide for an extremely low water-to-cement or concrete ratio, high slump retention while maintaining good flowability, as well as low foam formation during the preparation of the cement or concrete.
The present invention provides novel grafted polymers, which are the reaction products of:
Components (a) and (b) described above are subjected to copolymerization. The reaction products thus obtained are subsequently neutralized with an alkaline base and solubilized in an aqueous solution such as water.
Surprisingly it has been found that due to the particular structure of the maleate moiety, both the polyglycolether chains and the alkyl chains are located on the grafted polymer leading to improved super-plasticizing properties in cement and concrete, in particular with respect to
In addition, the non-symmetric maleate allows the incorporation of polyglycolether groups and also alkyl chains into the polymer, which is generally rather difficult due to their poor solubility in water.
Another embodiment of the present invention is directed to a process for the manufacture of grafted polymers comprising;
Firstly, the non-symmetric maleate is prepared by a two-step esterification by a methyl-capped polyglycolether, which is followed by a fatty alcohol. Suitable methyl-capped polyglycolethers possess average molecular weights of 100 to 10000, preferably 200 to 6000 and most preferably 350 to 5000 Daltons. The polyether can be ethylene oxide or propylene oxide units only, however, it is also desirous to have mixtures present, either in random or in block distribution. If mixed methyl-capped polyglycolethers are used as starting materials, the number of ethylene oxide units is preferably between 0 and 120 and the number of propylene oxide units between 0 and 120. The maleic acid semi-ester thus obtained is subsequently esterified with a saturated or unsaturated synthetic or natural fatty alcohol having 1 to 22 carbon atoms, and preferably 6 to 16 carbon atoms. Suitable examples are capryl alcohol, 2-ethyl hexyl alcohol, lauryl alcohol, isotridecyl alcohol, myristyl alcohol, cetyl alcohol, stearyl alcohol, cetearyl alcohol, oleyl alcohol, elaidyl alcohol, gadoleyl alcohol, arachidonyl alcohol, erucyl alcohol, behenyl alcohol and their technical mixtures. The preferred alcohols are lauryl and coco fatty alcohol. The esterification is conducted according to the state of the art at elevated temperatures of about 80° C. to about 130° C., and optionally under a reduced pressure of about 10 mbar. The water formed during the condensation can be removed continuously from the reaction mixture in order to shift the equilibrium to the product side.
Once the non-symmetric maleate has been prepared, it is transferred together with the (meth)acrylic acid into a second flask where the polymerization takes place. The two monomers can be used in a weight ratio (a):(b) of from 1:99 to 99:1, preferably 2:98 to 40:60, and most preferably 5:95 to 25:75. The polymerization is conducted according to methods known in the art and usually takes place in aqueous solution at elevated temperatures of about 60° C. to about 100° C., and preferably about 80° C. and is commenced by the addition of a conventional initiator, such as, for example, ammonium persulfate. Once the polymerization is completed, the reaction mixture is cooled and treated with an alkaline base, preferably an aqueous sodium or potassium hydroxide solution in a quantity sufficient to neutralize the acidic functions in the polymer and to pre-pare salts thereof. The reaction products can then be diluted by addition of water in order to adjust to the desired active polymer content of typically 20 to 50% b.w., and preferably about 35% b.w.
The grafted polymers obtained according to the present invention provide high fluidity and better workability to cement, concrete and plaster compositions. Another object of the present invention is therefore the use of the polymers as so-called super-plasticizers for concrete or plaster retarders.
The following examples are illustrative of the invention and should not be construed in any manner whatsoever as limiting the scope of the present invention.
18 g of lauryl alcohol was placed in a 150-ml reactor at room temperature. The alcohol was heated to 90° C. and melted. Then 9.5 g maleic anhydride was added and the reaction temperature maintained at 90° C. until an acid value of 200 mg KOH/g (about 4 hours of reaction) was reached. Then 71.5 g of mono-methoxy poly(ethylene glycol) 750 Dalton and 1 g of the esterification catalyst sulphuric acid were added. The mixture was maintained under a reduced pressure of 10 mbar and at 90° C. for 6 hours. The final acid value was about 12 mg KOH/g.
8 g of lauryl alcohol was placed in a 150-ml reactor at room temperature. The alcohol was heated to 90° C. and melted. Then 4.3 g maleic anhydride was added and the reaction temperature maintained at 90° C. until an acid value of 200 mg KOH/g (about 4 hours of reaction) was reached. Then 86.7 g of mono-methoxy poly(ethylene glycol) 2000 Dalton and 1 g of the esterification catalyst sulphuric acid were added. The mixture was maintained under a reduced pressure of 10 mbar and at 90° C. for 6 hours. The final acid value was about 12 mg KOH/g.
32 g of the non-symmetric maleate obtained according to Example 1 and 8 g acrylic were placed in a 250-ml-polymerization flask at room temperature. The mixture was diluted with 58.6 ml water and set under nitrogen bubbling in order to remove all traces of oxygen. Then the mixture was heated to about 80° C. and 1.4 g initiator (ammonium persulfate) was added. Since the polymerization represents an exothermic reaction, the flask was cooled in order to maintain a reaction temperature of 80 to 90° C. Once the polymerization was completed, the product was cooled to room temperature and treated with aqueous sodium hydroxide solution to neutralize the acidic groups in the polymer and diluted with water to adjust to a polymer content of 30% b.w.
36 g of the non-symmetric maleate obtained according to Example 2 and 4 g acrylic were placed in a 250-ml-polymerization flask at room temperature. The mixture was diluted with 59.3 ml water and set under nitrogen bubbling in order to remove all traces of oxygen. Then the mixture was heated to about 80° C. and 0.7 g initiator (ammonium persulfate) was added. Since the polymerization represents an exothermic reaction, the flask was cooled in order to maintain a reaction temperature of 80 to 90° C. Once the polymerization was completed, the product was cooled to room temperature and treated with aqueous sodium hydroxide solution to neutralize the acidic groups in the polymer and diluted with water to adjust to a polymer content of 30% b.w.