Patent Application
20190135694
The present invention relates to a novel formulation and to the use of this formulation for the production of construction products with improved acid and heat resistance.
Portland cement was first mentioned in British patent BP 5022 and has since been continuously further developed. Modern Portland cement contains about 70% by weight of CaO+MgO, about 20% by weight of SiO2 and about 10% by weight of Al2O3+Fe2O3. Owing to its high CaO content, it hardens hydraulically. Hardened Portland cement is alkali-resistant but not acid-resistant.
As latent hydraulic binders, certain slags from metallurgical processes can be activated with strong alkalis, such as, for example, waterglasses or alkali hydroxides, or can be used as admixtures to Portland cement. By mixing with fillers (quartz sand or aggregate having a corresponding grain size) and additives, they can be used as mortars or concretes. Blast furnace slag, a typical latent hydraulic binder, has as a rule 30 to 45% by weight of CaO, about 4 to 17% by weight of MgO, about 30 to 45% by weight of SiO2 and about 5 to 15% by weight of Al2O3, typically about 40% by weight of CaO, about 10% by weight of MgO, about 35% by weight of SiO2 and about 12% by weight of Al2O3. Activated latent hydraulic binders generally harden hydraulically, i.e. through crystallization.
Hydraulically hardened systems regularly exhibit a high compressive strength but often very low resistance towards acids.
Inorganic binder systems based on reactive water-insoluble oxides based on SiO2 in combination with Al2O3, which harden in an aqueous alkaline medium, are generally known. Such binder systems are also referred to as geopolymers and are described, for example, in U.S. Pat. No. 4,349,386, WO 85/03699 and U.S. Pat. No. 4,472,199. Such systems comprise as a rule 50 to 60% by weight of SiO2, 20 to 25% by weight of Al2O3, no CaO and 15 to 30% by weight of M2O (M=Na, K).
Metakaolin, slag, fly ash, calcined clay or mixtures thereof may be used as reactive oxide mixture. The alkaline medium for activating the binder usually consists of aqueous solutions of alkali metal carbonates, alkali metal fluorides, alkali metal aluminates, alkali metal hydroxides and/or soluble waterglass. Also alkali metals sulfates may be used. The hardened binders have high mechanical stability. In comparison with cement, they may be more economical and more resistant to chemicals and fire and may have a more advantageous CO2 emission balance.
WO 08/012438 describes a further geopolymer cement based on low-CaO fly ash class F, blast furnace slag and aqueous alkali metal silicate having a SiO2:M2O ratio of more than 1.28, preferably of more than 1.45. In the examples calculated on the basis of anhydrous oxides, about 45 to 50% by weight of SiO2, about 20 to 26% by weight of Al2O3, about 9 to 10% by weight of CaO and about 3 to 4% by weight of K2O are present.
Our WO 2011/064005 A1 (corresponding to EP 2504296 B1) describes a novel inorganic binder system, the use of that binder system for the production of a hydraulically setting mortar, and a mortar which contains that binder system. The binder system hardens in the form of a hybrid matrix which is acid-resistant, water-resistant and alkali-resistant. However, no useful dispersants for that system have been disclosed.
Our WO 2013/152963 A1 (corresponding to EP 2836529 A1) describes a polycondensation product comprising, as monomer components, at least one aryl polyoxyalkylene ether, at least one vicinally disubstituted aromatic compound, at least one aldehyde, and optionally further aromatic compounds. The invention also relates to a method for the preparation thereof, and to the use as a dispersant for aqueous suspensions of alternative inorganic binders. However, when it comes to alkali metal silicates as activators, the workability improvement is very poor (cf. Example 16 of WO 2013/152963 A1).
Moreover, L. Nicoleau, M. Pulkin and T. Mitkina in “PLASTICIZING GEOPOLYMER-TYPE SUSPENSIONS: A CHALLENGE”, CANMET 2015), report that anionic polycondensation products work very poorly in the presence of alkali silicates (“[i]ndeed, the plasticizing efficiency decreases when the binder is a class F fly-ash instead of a slag, and, drops dramatically when an alkali-silicate activator is used instead of KOH.”; p. 479, 1.36-38.)
The inventors have set themselves the object of substantially avoiding at least some of the disadvantages of the prior art as discussed above. In particular, it was the object of the invention to provide a formulation exhibiting at least some of the following properties: high flowability, even if alkali metal silicate is used as an activator, low water-to-binder (w/b) ratio, high density, high early and final compressive strength high heat resistance and enhanced acid resistance.
The abovementioned object is achieved by the features of the independent claims. The dependent claims relate to preferred embodiments.
It was surprisingly found that the formulation of the present invention allows the production of acid and heat-resistant construction products. Moreover, it was surprisingly found that the polycondensation product of the invention works well even with alkali metal silicates as activator.
The present invention provides a formulation comprising:
at least two inorganic binders, wherein the first inorganic binder is selected from hydraulic binders, latent hydraulic binders, and mixtures thereof, and the second inorganic binder is selected from pozzolanic binders;
at least one activator selected from alkali metal silicates, alkali metal carbonates, alkali metal hydroxides, alkali metal aluminates, alkali metal sulfates, and mixtures thereof; and
at least one polycondensation product comprising as monomer components:
a) at least one aromatic compound of the formula
Ar—V—[CHR1—CHR2—(O—CHR1—CHR2)m—R3]n, wherein
The use of at least two inorganic binders is owed to the fact that, as taught in EP 2504296 B1, such binder systems harden in the form of a hybrid matrix which is acid-resistant, water-resistant and alkali-resistant.
The CaO content of the formulation of the invention should preferably be in the range of 2 to 40%, more preferably 5 to 35% and most preferably 12 to 25%, by weight since this range appears to facilitate the formation of such hybrid matrix.
For X being the molar amount of the aromatic carboxylic acid b), there should be generally 0.1X to 10.0X of the aromatic compound a) and 0.6X to 16.5X of the aldehyde present as monomer components in the polycondensation product of the invention (the latter ratio corresponding to about 50% excess of either the combined aromatic compounds or the aldehyde).
The formulation of the invention may contain hydraulic binder(s). These hydraulic binders can be selected from portland cements, aluminate cements, sulfoaluminate cements, and mixtures thereof, and the content of portland cements, aluminate cements and/or sulfoaluminate cements in the binder system is ≤30% by weight, preferably ≤20% by weight and in particular ≤10% by weight. If the amount of the hydraulic binder(s) is too high, the formation of a desired hybrid matrix may no longer be possible.
The term “% by weight” as used throughout this specification is based on the total amount of binders, activators and polycondensation products as defined hereinabove, each calculated as dry substance. With other words, percentages are based on the “water-free formulation”.
In the formulation of the invention the latent hydraulic binder can be selected from blast furnace slag, granulated blast furnace slag, ground granulated blast furnace slag, electrothermal phosphorus slag, steel slag and mixtures thereof.
In the context of the present invention, a latent hydraulic binder is preferably to be understood as meaning a binder in which the molar (CaO+MgO):SiO2 ratio is between 0.8 and 2.5 and particularly preferably between 1.0 and 2.0. In particular, the latent hydraulic binder is selected from blast furnace slag, slag sand, ground slag, electrothermal phosphorus slag and steel slag.
Blast furnace slag is a waste product of the blast furnace process. It may be granulated (“granulated blast furnace slag”) or finely pulverized (“ground granulated blast furnace slag”). The ground granulated blast furnace slag varies in its fineness of grinding and particle size distribution according to origin and preparation form, the fineness of grinding having an influence on the reactivity. The so-called Blaine value, which is typically of the order of magnitude of 200 to 1000, often between 300 and 500 m2 kg−1, is used as a characteristic for the fineness of milling. A typical composition of blast furnace slag was mentioned hereinabove.
Electrothermal phosphorus slag is a waste product of electrothermal phosphorus production. It is less reactive than blast furnace slag and contains about 45 to 50% by weight of CaO, about 0.5 to 3% by weight of MgO, about 38 to 43% by weight of SiO2, about 2 to 5% by weight of Al2O3 and about 0.2 to 3% by weight of Fe2O3 as well as fluoride and phosphate.
Steel slag is a waste product of various steel production processes with strongly varying composition (cf. Caijun Shi, Pavel V. Krivenko, Della Roy, Alkali-Activated Cements and Concretes, Taylor & Francis, London & New York, 2006, pages 42-51).
In the formulation of the invention the pozzolanic binder can be selected from precipitated silica, pyrogenic silica, microsilica, glass powder, brown coal fly ash, mineral coal fly ash, rice husk ash, metakaolin, volcanic ash, tuff, trass, pozzolana and zeolites and mixtures thereof.
The test for pozzolanic activity can be effected according to DIN EN 196 part 5. An overview of pozzolans suitable according to the invention is to be found in Caijun Shi, Pavel V. Krivenko, Della Roy, Alkali-Activated Cements and Concretes, Taylor & Francis, London & New York, 2006, pages 51-60, and pages 61-63.
The silica according to the invention as a rule has a content of at least 80% by weight, preferably at least 90% by weight, of SiO2. Precipitated silica is obtained industrially via precipitation processes starting from waterglass. Precipitated silica is also referred to as silica gel, depending on the production process. Pyrogenic silica is produced by reacting chlorosilanes, such as, for example, silicon tetrachloride, in an oxyhydrogen flame. Pyrogenic silica is an amorphous SiO2 powder having a particle diameter of 5 to 50 nm and a specific surface area of 50 to 600 m2 g−1.
Microsilica (also referred to as silica fume) is a by-product of silicon or ferrosilicon production and likewise comprises for the most part amorphous SiO2 powder. The particles have diameters of the order of magnitude of 0.1 μm. The specific surface area is of the order of magnitude of 20 to 25 m2 g−1 (cf. Caijun Shi, Pavel V. Krivenko, Della Roy, Alkali-Activated Cements and Concretes, Taylor & Francis, London & New York, 2006, pages 60-61). Glass powder, for the purpose of the present invention, reacts similar to amorphous SiO2 powder. In contrast, commercially available quartz sand is crystalline, has comparatively large particles and a comparatively small specific surface area. It serves according to the invention merely as an inert aggregate.
Metakaolin forms in the dehydration of kaolin. While kaolin releases physically bound water at 100 to 200° C., a dehydroxylation takes place at 500 to 800° C. or above with a collapse of the lattice structure and formation of metakaolin (Al2Si2O7). Pure metakaolin accordingly contains about 54% by weight of SiO2 and about 46% by weight of Al2O3. Fly ashes form, inter alia, in the combustion of coal in power stations. According to WO 08/012438, fly ash of class C contains about 10% by weight of CaO while fly ashes of class F contain less than 8% by weight, preferably less than 4% by weight and typically about 2% by weight of CaO. The teaching of WO 08/012438 is hereby incorporated by reference to this extent.
In the formulation of the invention the ratio of the first inorganic binder to the second inorganic binder should preferably be from 1:50 to 50:1 by weight, more preferably from 1:10 to 10:1 by weight.
Moreover, in the formulation of the invention the activator is preferably an alkaline activator and in particular an alkali metal silicate. That alkali metal silicate can be selected from compounds having the empirical formula m SiO2.nM2O, in which the alkali metal M represents Li, Na or K, or a mixture thereof, preferably Na and/or K, and the molar ratio m:n is from 1.0 to 4.0, preferably 1.0 to 3.8 and in particular 2.0 to 3.6.
The alkali metal silicate is preferably a waterglass. In the case of liquid (i.e. aqueous) waterglasses, the abovementioned percentages by weight are calculated on the basis of the solids contents of these waterglasses, which as a rule are 20% by weight to 60% by weight, preferably 30% to 50% by weight, of the liquid waterglass.
According to a preferred embodiment of the invention, at least two activators are present in the formulation, wherein the first activator is selected from powdered alkali metal silicates, and the second activator is selected from alkali metal carbonates, alkali metal hydroxides, alkali metal aluminates, alkali metal sulfates, and mixtures thereof, the alkali metal having the above meaning, and preferably from alkali metal hydroxides such as NaOH, KOH and mixtures thereof. Again, even in case that the second activator is used in liquid (i.e. aqueous) form, the amounts thereof are calculated on the basis of its solid content.
In the formulation of the invention the ratio of the powdered alkali metal silicate to the second activator should preferably be from 1:100 to 100:1 by weight, more preferably from 1:10 to 10:1 even more preferably from 1:5 to 5:1 and most preferably from 1:3 to 3:1, by weight.
Inert fillers and/or further additives may additionally be comprised in the formulation of the invention. The inert fillers and/or further additives are not counted as constituents of the formulation. These optional components can either be present in the formulation or can be added later on upon the preparation of a mortar or concrete.
Generally known gravels, sands and/or powders, for example based on quartz, limestone, barite, basalt or clay, in particular quartz sand, are suitable as inert fillers. Light fillers, such as perlite, kieselguhr (diatomaceous earth), exfoliated mica (vermiculite) and foamed sand, can also be used.
Suitable additives are, for example, generally known flow agents, antifoams, air entrainers, water retention agents, plasticizers, pigments, fibers, dispersion powders, wetting agents, retardants, accelerators, complexing agents, aqueous dispersions and rheology modifiers. More specifically, the additives can be selected from glycols, polyalcohols, organic acids, amino acids, sugars, molasses, lignosulfonate, organic and inorganic salts, polycarboxylate ethers, naphthalenesulfonate, melamine/formaldehyde polycondensation products, and also mixtures thereof.
According to a preferred embodiment of the invention the polycondensation product comprises as monomer components:
a) at least one aromatic compound of the formula
Ar—O—CHR1—CHR2—(O—CHR1—CHR2)m—R3, wherein
In the above definition Ar is preferably an aryl group having 6 to 10 carbon atoms in the ring system, and more particularly is a phenyl group or a naphthyl group.
Both R1 and R2 may represent H. The index m can be an integer from 0 to 280, preferably from 10 to 160 and more particularly from 12 to 120. Another preferred range of m is 0 to 43 (corresponding to PhPEG2000), more preferred 0 to 20 (corresponding to PhPEG1000).
In the polycondensation product of the invention R3 can selected from the group consisting of OH, C1-10-alkoxy, C6-10-aryloxy, C7-11-arylalkoxy, C7-11-alkylaryloxy, phosphate and mixtures thereof.
The above mentioned aromatic carboxylic acid can be selected from 2-hydroxybenzoic acid, 3-hydroxybenzoic acid, 4-hydroxybenzoic acid, 2,3-dihydroxybenzoic acid, 2,4-dihydroxybenzoic acid, 2,5-dihydroxybenzoic acid, 2,6-dihydroxybenzoic acid, 3,4-dihydroxybenzoic acid, 3,5-dihydroxybenzoic acid, gallic acid, and mixtures thereof, and is preferably salicylic acid.
Moreover, the aldehyde can be selected from the group consisting of formaldehyde, paraformaldehyde, glyoxylic acid, benzaldehyde, benzaldehydesulfonic acid, benzaldehydedisulfonic acid, vanillin, isovanillin, and also mixtures thereof.
The polycondensation product of the invention has preferably the form of a comb polymer, wherein the main chain exhibits a novolak structure, e.g. (—CH2—Ar—)n in the case of formaldehyde).
The polycondensation product of the invention can have a molecular weight in the range of from 1000 to 100 000, preferably 2000 to 75 000 and more particularly 4000 to 50 000 g/mol.
Finally, the present invention provides the use of the formulation as defined hereinabove for the production of an acid-resistant and/or a heat-resistant construction product.
The present invention is now elucidated with greater precision by means of the examples below.
The starting materials were mixed in a laboratory mortar mixing device according to DIN EN 196-1. Mixing was carried out as described in DIN EN 196-1, except that the quartz sand was first placed in the mixing vessel. Sodium hydroxide dissolved in the mixing water was used as one alkaline activator. Melflux DF 93 (4 wt.-% solids, based on the dispersant, of an aqueous emulsion of polyalkylene glycols, modified with polycarboxylate ethers, of BASF SE) was used as a defoamer. The dispersants were used in aqueous solution.
The dispersant was prepared according to the modified procedure from the Example 30 of WO 2013/152963 A1. 787.5 weight parts of poly(ethyleneoxide) monophenyl ether (number average molecular weight Mn=750 g/mol) and 145.07 parts of 2-phenoxyethanol were placed into a heatable glass reactor equipped with mechanical stirrer, reflux condenser and dosage pump. 231 parts of polyphosphoric acid were added to the reaction mixture under vigorous stirring over 25 min, while the temperature of reaction mixture was maintained below 30° C., followed by heating of the resulting mixture at 95° C. for 1 hour. Thereafter 290.05 parts of 2-hydroxybenzoic acid, 139.38 parts of paraformaldehyde and 150 parts of water were added under stirring and constant nitrogen flow, followed by the adjustment of the reaction temperature to 90° C. 201.81 parts of methanesulfonic acid (70% aqueous solution) were dosed to the reaction mixture over 1 hour under maintaining the reaction temperature below 110° C., followed by further heating and stirring the reaction mixture at ca. 100-105° C. over 2 hours. The reaction was stopped by the addition of 2911 parts of cold water and subsequently neutralized with 680 parts NaOH (50% aqueous solution) to pH value˜7. The resulting polymer solution was analyzed by gel permeation chromatography (GPC) (PEG/PEO calibration, RI detection, column combination OH-Pak SB-G, OH-20 Pak SB 804 HQ and OH-Pak SB 802.5 HQ from Shodex, Japan; eluent 80 Vol.-% aqueous ammonium formate solution (0.05 mol/l) and 20 Vol.-% acetonitrile; injection volume 100 μl; flow rate 0.5 ml/min). GPC Data: Mw=11.2 kDa; Mn=6.1 kDa; PDI=1.8.
Mixtures as described below were used for chemical resistance tests. After six minutes of resting, the mortars were again stirred and applied to forms that were impressed in a silicone mat, thus giving cylindrical specimen of 25 mm diameter and 25 mm height. The specimen were removed from the forms after 24 hours of storage (23° C., 50% rel. hum.) and subsequently stored for 27 days (23° C., 50% rel. hum.). After a total of 28 days the specimen were tested for chemical resistance.
Chemical resistance tests were carried out by weighing a specimen and placing it in a plastic bottle (250 ml) that was filled with 200 ml of a medium. 50 g of coarse quartz sand was additionally placed inside that bottle. The bottle was subsequently rotated for 2.5 hours in an overhead mixer. This simulates an accelerated attack of the specimen by the medium through mechanical wear. The specimen was then removed from the bottle, dried and weighted again. The percentage of mass loss during the test was used to assess the resistance of the specimen. The resistance was assessed in three different media: water, H2SO4 (pH=2) and lactic acid (pH=2).
Four different mortars were prepared, i.e. reference mortars M1.1 and M2.1 (without dispersant) and mortars M1.2 and M2.2 (with dispersant and thus less water). The formulations are given in Table 1 and 2. The spread was measured after 6 and 30 minutes, applying each time 15 lifts on a Hägermann table after removing the conus (DIN EN 1015-3). The compressive strength values after 7 and 28 days (DIN EN 197-1) (prisms of 40×40×160 mm) are also listed in Tables 1 and 2.
The chemical resistance (i.e. the weight loss) of specimen cured for 28 days are given in Table 3 hereinbelow. Especially the chemical resistance in acids is significantly improved for the formulations M1.2 and M2.2.
Cylindrical specimens of 25 mm diameter and 25 mm height were used for testing of heat resistance. Samples of M1.2 and M2.2, after 35 days of curing, were heat treated to 400° C. for half an hour (heating rate 2 K/min) and cooled down. Compressive strength was measured after cooling. Table 4 summarizes compressive strength values of samples before and after heat treatment. The samples had essentially maintained their strengths during heating.
| Number | Date | Country | Kind |
|---|---|---|---|
| 16169979.8 | May 2016 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2017/061296 | 5/11/2017 | WO | 00 |
