Process for the Preparation of Cement, Mortars, Concrete Compositions Containing a Calcium Carbonate - Based Filler Containing an Organosiliceous Material, the Said "Filler(s) Blend" Being Treated with a Superplastifier, Cement Compositions and Cement Products Obtained, and their Applications

Information

  • Patent Application
  • 20160115077
  • Publication Number
    20160115077
  • Date Filed
    November 16, 2015
    9 years ago
  • Date Published
    April 28, 2016
    8 years ago
Abstract
PROCESS for the preparation of cement/mortar/concrete compositions or systems, (for simplicity hereafter “cement” compositions or systems), featuring an improved compressive strength Rc namely at 28 days and 90 days, containing at least a “carbonate-based filler”, comprising at least one step where the said at least one “carbonate-based filler” is mixed or blended with at least one aluminosiliceous material, and the obtained “fillers blend” is treated with an efficient treating amount of at least one treating agent consisting of or comprising superplastifier(s);
Description
TECHNICAL FIELD OF THE INVENTION

The present invention relates to the field of cement compositions, cementitious compositions, hydraulic binders compositions, mortar compositions, concrete “compositions” (or hereafter equivalently “systems”), namely of the type compositions (or “systems”) of cement/hydraulic binders, mortars, concrete, containing at least one particulate mineral of the calcium carbonate(s) type as a filler, and their applications, as well as the corresponding cement, mortar, concrete products or elements, the said filler containing at least one carbonate-based filler replaced at least partially with at least on organosiliceous material, what forms a “fillers blend” which is then treated with a superplastifier.


The invention relates to a specific process for producing the said compositions or “systems” (those terms are going to be used as equivalents in this application and claims) for cement, hydraulic binder, mortar, concrete, the obtained compositions, the cement, mortars and concrete products obtained therefrom, and their applications.


PRIOR ART

It is reminded that a cement system (or equivalently “composition”) is a system comprising cement particles, mixing water (or equivalently a mixing aqueous composition not interfering with the said system, as known to the skilled man), filler(s), various optional and usual additives such as air entrainment agents, setting retarders, setting accelerators and the like, and any such routine additives as well known to the skilled man.


A mortar system additionally contains an inert aggregate material, usually a sand.


A concrete system still additionally contains gravel.


The above is abundantly known and common knowledge.


DEFINITION





    • cement systems or compositions or slurries: as a matter of simplicity, and also because the invention relates to the use of additives adapted to improve the properties of any of those three systems, the terms “cement systems” (or “compositions”) (or “slurries”) (or “cement”) will be used in the following to encompass ANY of the above cited main kinds of compositions or “systems”, that is a cement, cementitious, hydraulic binder, mortar or concrete composition or system. The skilled man will be able to appreciate if the system is a cement, a mortar or a concrete composition in view of the presence, or the absence, of sand and/or gravel. This simplification is made possible since sand and gravel are inert materials, and therefore do not noticeably interfere with the invention.





It is also pointed out that, even if, in the following, an information is provided regarding “cement systems” or “cements” for example, it ALSO applies mutatis mutandis to any of the other kinds of systems, namely mortars and concretes. The only difference between the above main types of “compositions” (or equivalently “systems”) being the presence, or not, of sand and/or gravel.


In such compositions, fluidifier(s) is/are often used.


In that domain, the EP 0 663 892 to CHRYSO is certainly the most relevant document, which discloses fluidifier polymers for mineral suspensions with no hydraulic setting, or hydraulic binders slurries.


Cited applications are paper coating, paints, and synthetic resins or rubber compositions.


According to the said prior art, it was known to add fluidifiers in mineral, particular suspensions to lower their viscosity, and, especially for paper applications, this leads to high mineral concentrations, a better workability, and this reduces the drying energy. For example, this is used in connection with suspensions of calcium carbonate.


It is also known to add such fluidifiers to “cement” (in the wide sense explained hereabove) slurries, with the purpose this time of reducing their water content “water-reducing additives” (Chryso Premia 196™) and to obtain a “cement” composition with a “more dense structure” after setting.


Encountered problems are: the influence of electrolytes, which reduces the fluidifying effect and forces to increase the amount of fluidifier (with an increase in cost), as well as, for “cement”, the need not to negatively alter the setting characteristics of the cement composition not its final properties.


Some well-known fluidifiers are superplastifiers or plastifiers.


In that domain, the EP 0 663 892 to CHRYSO is relevant, as well as FR 2 815 627, FR 2 815 629 and WO2008/107790 which also disclose interesting superplastifiers.


Some known fluidifiers affect less the setting time, but are still unsatisfactory, such as condensation products of sulfonated naphtalene and formaldehyde or melamine-formaldehyde with a sulfonated compound. Some of those products are also superplastifiers, but much less preferred.


Also, EP 0 099 954 relates to fluidifiers made by condensation of amino-sulfonic acid comprising at least an aromatic ring with nitrogenated compounds bearing several amine functions and formaldehyde.


Such are said not to delay too much the setting of cement compositions, but they are highly sensitive to electrolytes when it comes to their “activity”. They also can be obtained with low concentrations, usually no more than about 40% by dry weight, since any concentration increase in turn increases their viscosity to inadmissible levels.


The summary of the desired properties is listed page 3 lines 15 ff of the above-mentioned EP.


It is also known to add filler(s) in cement, hydraulic binders, cementitious or concrete or mortars compositions or “systems”.


The purpose of adding such filler(s) is to fill the voids between particles, to reduce the overall costs, and to greatly improve a property called “consistency” (consistency being the capacity or ability for the considered systems to easily flow or “self-level”, or not) and a property called “compacity” (that is the percentage of dry material in the final composition (the higher the percentage, the better the compacity)).


Finally, EP 10 008 803.8 describes the treatment of calcium carbonate based filler(s) (see definition herebelow) with certain superplastifiers optionally admixed with certain plasticizers and optionally fluidifiers in order to upgrade “low” or “dry” grade (or “standard”) “cement systems” (not usable in the modern industry as explained in detail in the said application and herebelow for completeness) to at least “plastic” and most preferably “fluid” “cement systems” which can be used with great advantages in the modern industry.


Superplastifiers and namely products A and B are disclosed in WO2004/041882, and especially with reference to the polymers disclosed in the Examples.


DEFINITION





    • calcium carbonate-based filler(s): in the present application, the said filler(s) are defined as “calcium carbonate-based filler(s)” that is, in this application and claims, fillers that contain(s) only calcium carbonate(s) (possibly of various origins, such as various natural rocks or various PCCs)—which means with no other filler of a different type, such as kaolin, bentonite, etc. . . . known to the skilled man—and is/are preferably provided (when the filler(s) is/are or contain(s) GCC(s)) by a carbonated rock or more generally mineral material(s) comprising at least 50-65% by weight (dry) of CaCO3, preferably more than 80%, still more preferably more than 90%; those carbonate-based filler(s) s are selected among:

    • natural calcium carbonate(s) or ground calcium carbonate(s) (GCC(s)) such as, non limitatively, GCC from marble, chalk, calcite, or from other natural and well-known forms of natural calcium carbonates, which most preferably meet the above % criteria;

    • PCC(s) which is a precipitated calcium carbonate, of fine or ultrafine granulometry, such as none limitatively 1.52 μm for d50, and exists under various well-known forms, depending on the well-known precipitation/preparation process.

    • or mixtures or blends of said CaCO3—containing rocks or mineral materials with each other as well as blends or mixtures of GCC(s) and PCC(s) and optionally blends of PCCs.





The GCC/PCC ratio can be chosen from 0-100 to 100-0% by dry weight, preferably from 30-70 to 70/30% by dry weight.


Usually a “filler” has the following properties:

    • Purity (methylene blue test) is lower than 10 g/kg, preferably below 3-5 g/kg, preferably below 1-1.5 g, with a most interesting value at 1.2 g/kg.
    • Mean diameter or d50 is about in the range of 1-3 to 30-50 micrometres measured by using the Malvern 2000 PSD equipment/methodology, or Sedigraph.
    • Blaine surface, which is a characteristic feature of FILLERS, as is well-known, is in the domain of 180-2000 m2/kg, preferably of 300 to 800 m2/kg, as measured under an EU Standard (European standard EN 196-6).


As will be seen below, the d50 range of 1-5-6 microns corresponds, for the fillers featuring a Blaine surface above about 1000 m2/g, to ultrafine fillers (UFs); above 6 is the domain of coarser or coarse fillers, hereafter “fillers”.


In this application, when ultrafine fillers are considered, the wording “ultrafine” or “ultrafine fillers” or “UF” will be used.


In the present application, the said carbonate-based filler(s) can be

    • ultrafine filler(s) (see definition herebelow) and/or
    • coarser or coarse filler(s) (of the calcium carbonate containing type as defined above).


DEFINITION





    • in the present application, “aluminosiliceous material” is a product or blend of products mainly made of siliceous product(s) and/or acuminous product(s). “Mainly” means that the said products may contain only a minor amount of non aluminosiliceous products, such as impurities etc. . . . , as a result of the industrial production, as is well known from the skilled man.





Such products are preferably selected among aluminum oxides such as various forms of Al2O3, silica fumes (SF) such as various forms of SiO2 or SiO2 fumes, calcined kaolin or “metakaolin” (MK), pozzolanic products (used by cement industry) such as blast furnace slags (see EN-197-1), ultrafine siliceous products from the industry etc., and preferably blends of globally speaking Al2O3/SiO2.


Non limitative examples are:

    • Sifraco™ C800 containing 98% SiO2 and a minor amount (0.71%) of Al2O3, and traces of CaO and MgO (this is an illustration of the above wording “mainly”); SSP=7.49 (surface measurement since the fineness is too high for a Blaine measurement); d50 (median diameter)=1.86 micron
    • Condensil™ S95 D which is a silica fume obtained while preparing silicium d50=1.2 micron Blaine>1600 m2/kg BET (specific surface area measured using nitrogen and BET method according to ISO 9277) BET=16 m2/g.
    • Pieri™ (Grace™) Premix MK: this product is a metakaolin of d50=3 microns Blaine: too fine BET=3.8 m2/g
    • Hauri™ Phonolit d50=14 microns BET=6.12 m2/g


“Ultrafines particles” or more simply “ultrafines” or still more simply “UFs” which can be used in the present invention can be defined by

    • a d50 from about 1 micron to about 5 or 6 microns, preferably from 1 to 3 microns, and still better of about 2-3 microns, usually <5 microns.
    • and
    • a high specific surface, usually defined as BLAINE>1000 m2/kg pref.>1500 m2/kg, pref. up to 2000 m2/kg.
    • Reference can be taken as to CaCO3 additives (“additions calcaires”) to a cement from NF P 18-508 (2012-01), see 4.3.1 (Blaine) (NF EN 196-6) and 4.3.2 which defines the “Highly Fine” additives as having namely a d50<5 microns; which also refers to the “bleu de méthylène” test (NF EN 13639)(4.2.6) and other interesting definitions.


Quite representative examples of such useful UFs are:

    • silica fumes (1-2 microns),
    • metakaolin (that is calcined kaolins, 3 to 5-6 microns), chalks of 1 to 5 microns d50,
    • calcites such as d50 about 1 micron,
    • Millicarb™ (about 3 microns d50), white limestone of about 1 to 5-6 microns d50,
    • Durcal 1 or 2 (d50 1 resp. 2 microns),
    • “Etiquette violette” (“EV”) (about 2.4 micron d50),
    • blast furnace slags d50=2.5 microns Blaine: too fine BET=2.7 m2/g


Preferred UFs to be used in the present invention are: EV™, silica fume SF, Condensil S95, metakaolin MK, namely Premix MK, Betocarb SL™ 1 or 2 and their mixtures.


Modified calcium carbonate (MCC) (such as of d50=2.29 μm) which is disclosed in U.S. Pat. No. 6,666,953 and ultrafine PCC (namely d50=1.52 μm) can also be used as UF(s).

    • As is known, a “cement” (in the above mentioned wide sense) composition or “system” is mainly made of:


Cement (or cementitious composition or hydraulic binder)+mixing water or mixing aqueous composition allowing setting but not interfering with the system)+optionally (usually inert) particulate and/or fibrous filler(s)+inert agglomerate(s) such as optionally sand+optionally inert gravel (plus optionally well known additives not to be mentioned in detail nor in full in the present application, such as setting accelerators, setting retarders, air entrainment agents, etc. . . . )+miscellaneous “routine” additives aimed at matching the precise need of the end-user.


As to the setting time the skilled man may refer to the DIN Standard EN 196-3.


Aggregates such as sand, inert gravel or “all-in” aggregates are known materials so commonly used that no description is needed here.


As discussed above, the invention relates also equivalently (under the generic term “cement” for simplicity) to mortars compositions or “systems” (like above including an aggregate like sand but no gravel) and cement compositions (same as above but no gravel and no sand).

    • “Mainly” means here that the system may contain some impurities or traces of additives or adjuvants, not to be mentioned in the present application, such as air entrainment agents, accelerators, retarders, etc.
    • “Mixing water” will mean in this patent application plain mix water or aqueous mixing compositions, that is mainly water plus usual additives, allowing the normal setting of the “cement” compositions, without interfering with the other properties of the overall composition, or only, via the additives, to improve some usual properties.


In this whole application and claims, “inert” shall mean a material which has no noticeable (or negligible) impact or interference with the process of the invention and the obtained compositions, products and applications. Given the involved ingredients, this will be easily appreciated by any skilled man.


The prior art “cement” (in the wide sense as defined above) systems to date are therefore mainly made of:


Cement (or hydraulic binders or cementitious compositions)+mixing water (or mixing aqueous compositions not interfering with the system)+optionally aggregate(s) such as sand+optionally gravel+FILLER(s)+“routine” additives.


It is also known that cement/hydraulic binders/cementitious compositions, cements, mortars and concrete compositions can be basically sorted out into:


DRY systems (poor quality or “low”) (casting is performed with high vibration and energy).


PLASTIC systems (medium quality) (medium vibration and energy).


(The two above categories may also be named “standard”)


FLUID systems (High performance or “HP”) (low vibration and low energy).


A very simple test is used to classify the systems, using a “mini cône à chape” known as “self-levelling test” or “screed flow cone test”.


The test is well known and is conducted according to the recognized Standard EN 196-1.


In order to provide the skilled man with useful guidelines and information about the meaning of “low”, “medium” or “HP” filler, we attach the TABLE A where ten fillers A to K of various origin and morphology (as indicated for characterization by the skilled man) have been tested for various properties and qualities, or drawbacks, with the classification “low” “medium” or “HP” being added on each line.


We also attach the TABLE A BIS which defines the time ranges a mixture is considered low medium or HP and the corresponding times for the V-funnel test.


This TABLE A BIS shows the ranges which define the low medium and High performance mixtures. Due to the ranges 30-120 sec, 10-30 second and <10 second the skilled person easily can recognize in which part of the ranges his mixture is i.e. in- or out-side and how to adapt accordingly.


The contributions of the microfiller to the rheological properties of the mortars were measured by slump flow with a mini cone and flow time through a V-Funnel. Table A BIS shows the microfiller performance evaluations for concrete. There in the Experimental methods * the LG16 test is described as well as the Slump flow and flow time, and the geometry of V-Funnel.


It is referred in the present application to standard NF EN-934-2 which defines the role of adjuvants. Reference should be made also to standard NF EN 206-1 which among other refers also to the 28 d compression resistance and to EN 197-1:2000 defining “aluminosiliceous” materials in sections 5.2.3. and 5.2.7, as well as standard EN 18-508 definition of “UF” in 4.3.2.









TABLE A







Characterization of “low”, “medium”, “HP” fillers and their aspect
















Treatment




Blue






Agent
geological



(Methylene



visual


Code
designation (age)
Type
d50
Blaine
Blue Test)
(3 g)
(4 g)
Evaluation
evaluation



















A
white chalk facies
chalk
1.0
>1400
2.0
plastic
220
low
slow, very



(90 Mi)




aspect


thick


B
white chalk facies
chalk
2.2
1120
2.7
280
340
medium
thick



(90 Mi)


C
urgonian facies
calcite
3.1
1171
0.3
200
290
low
slow, thick



(115 Mi)


D
bioclastic facies
calcite
6.0
720
1.0
plastic
338
medium
plastic



(160 Mi)




aspect


E
urgonian facies
calcite
6.5
395
0.3
460
475
HP
fluid



(115 Mi)


G
upper jurassic
marble
17.0
363
0.3
dry
365
medium
slow, heavy



(130 Mi)




aspect


H
upper jurassic
marble
13.4
385
0.3
337
413
low
slow, viscous



(120 Mi)


I
H + 5% B
X
X
X
X
190
390
medium
slow, viscous


J
H + 15% B
X
X
X
X
427
436
HP
fluid


K
H + 20% B
X
X
X
X
340
410
medium
fluid, thick
















TABLE A







BIS












Low
medium
HP




















A
C
H
B
D
G
I
K
E
J






















3 g
plastic
200 mm
337 mm
280 mm
plastic
dry
190 mm
340 mm
460 mm
427 mm
slump flow


4 g
200 mm
290 mm
413 mm
340 mm
338 mm
365 mm
390 mm
410 mm
475 mm
436 mm












V-funnel 4 g

30-120 sec
10-30 sec
<10 sec
flow time


















time
82
54
66
28
20
17
24
15
6
8









One uses 3 g or respectfully 4 g of fluidifier/superplastifier Premia 196™ commercialised by the Firm CHRYSO, and which is a commercial product said to be a “modified polycarboxylate” at a concentration of 25.3% by weight (dry extract measured along the Standard EN 480-8), by DRY weight of cement.


In the said Table A, “+15% B” evidently means an addition of 15% of the product B, to form a blend or mix, the % being in DRY WEIGHT/DRY MIX WEIGHT.


Equally, columns “3 g” and “4 g” means that 3 or respectfully 4 g of the said superplastifer have been added by DRY weight of the cement component alone.


“Mi” means “million years” (dating of the rock)


“Blue” means “methylene blue test” (purity test)


European patent applications in the name of the Applicant are filed on the same day as the present application and cover in great detail technical solutions aimed at upgrading a low or medium filler to an HP or fluid level.


Technical Problem

There exists a constant need for cement or mortar or concrete systems or compositions having a improved compacity (% of dry material, the highest possible), an improved flowability (that is forming a non sticky “galette” or “cone” of large diameter in the above described test, the larger the diameter, the better flowability), and globally speaking a definitely improved “workability” (workability being the ability of the cement or concrete composition to be prepared, processed, handled, and used to form a high performance or “technical” concrete) and a far better “regularity” in the final product properties especially at the end user level.


Clearly, some of those desired properties are antagonistic, and for example one should expect a high % dry material to perform poorly in a flowability test.


This being stated, the main purpose of this invention is to design new industrial products and to build a process aimed at providing improved mechanical strength properties at an “early age” or “short term” (“aux jeunes ages”) of 7 days (7 d), or over the long run such as after 28 to 90 days (28 d to 90 d).


BRIEF SUMMARY OF THE INVENTION

The use of the above aluminosiliceous material as fillers for cement composition is known on a theoretical basis. However, the skilled man knows above all that above 5%/dry weight of cement composition those fillers make it mandatory to increase the mix water content and to increase the proportion of water demand reducing fluidifier such as CHRYSO Premia 196™ otherwise, due to their high fineness, the viscosity of the cement composition increases and the cement composition becomes Unworkable. It is reminded that the viscosity must in practice remain <800 cps. To reach or maintain such a low viscosity would require the introduction of too high a proportion of fluidifier, up to a point of non compatibility between the cement and the fluidifier.


It has now been found according to the invention that it is possible to overcome those problems, and to reach high values for mechanical strength at, namely, 7 d, and especially at 28 d and 90 d, by preparing a new industrial PRODUCT characterized in that it comprises:


a) at least a carbonate-based “filler” and at least an aluminosiliceous material as defined above, what provides a “fillers blend”


b) the said “fillers blend” having been treated with at least a superplastifier of the polycarboxylate ether type.

    • It is to be understood that a part of the usual carbonate-based filler(s) is replaced by the alumino-siliceous material.


The said carbonate-based filler(s) comprises or consists of at least a coarse carbonate-based filler, see the definition above) such as GCC (coarse) and/or PCC (usually fine to ultrafine) and/or at least an UF.


UFs are usually “HP” fillers.


Coarse carbonate-based fillers can be “low, medium or HP” fillers.


According to the invention, on can use either low or medium, or HP carbonate-based fillers. If the carbonate-based filler or filler(s) is/are low or medium, they will basically remain low or medium. If HP, they will remain HP due to the combination with the superplastifier.


The invention resides first in a

    • PROCESS for the preparation of the above defined cement/mortar/concrete compositions or systems, (for simplicity hereafter “cement” compositions or systems), of a general known type as defined hereabove containing at least a carbonate-based filler, characterized in that it comprises at least one step where the said at least one carbonate-based filler is mixed with at least one aluminosiliceous material as defined hereabove, and the obtained “fillers blend” is treated with an efficient treating amount of at least one treating agent consisting of or comprising superplastifier(s).


The treatment with at least a superplastifier is believed to treat only the calcium carbonate(s) part of the filler(s), and for example not the alumino-siliceous material, other particulate or fibrous fillers, IF ANY, believed to be inert in this process.


By “comprising or consisting of” we mean that the fillers may consist of calcium carbonate(s), partially replaced as mentioned with at least an alumino-siliceous material, the said fillers blend being optionally mixed with non interfering fillers, and that the treating agent(s) can be: only superplastifier(s) or blends of superplastifier(s) with non-interfering plasticizer(s) (as defined herebelow) and/or routine, inert, additives, such as a routinely used “bottom-tank” fluidifier.


By “efficient treating (or “treatment”) amount” or “efficient surface coverage of the fillers particles or grains” or “efficiently treated”, we mean in this application that at least 50%, preferably at least 60, or better at least 80 or 90% or still better closer to 100% of the surface of the particles of the carbonate based filler(s) have been subjected to a physico-chemical interaction with the superplastifier(s). This physico-chemical interaction is not entirely understood as of the filing date, only the EFFECTS and RESULTS are duly identified and correlated to the treating superplastifier(s), but, without being tied by any theory, the applicant considers that the said interaction or “treatment” is a surface treatment or “surface-covering” treatment involving ionic, physical, mechanical and/or chemical, treatment(s) and via said interaction(s). This efficient treating or treatment amount must therefore be important enough to treat the said % of particle surfaces, as will be explained and disclosed in more detail below.


By “surface-covering” we mean that the superplasticizers are supposed by the applicant, without being tied by a theory, to engage in electrical charge potential interactions with the ionic charges of the surface of the fillers, which promotes the fixation of the superplastifier onto and/or closely around the surface and so reduces the “accessible” surface of the particle having no surface saturation of the grain by said treatment.


By “comprising” we mean in this application that the treating agent can be made only of superplastifier(s) (one or more mixed together, preferably one) or of blends of superplastifier(s) displaying mutual non-interference (that is, unable to noticeably degrade the above “treatment”) amount or proportion of known plasticizer(s) for the purpose of cost-saving, as explained in greater detail here-below


Process Options

1 According to the best mode of the invention, as defined to date, the said filler(s) blend is/are efficiently treated with the superplastifier(s) before being introduced in the kneading or mixing device (“pre-treatment” also named “initial”), such as in an outside mixing Laboratory equipment; in the industrial scale, such a pre-treatment can be performed in an industrial device such as the Lödige mixer or any other industrial kneading or mixing equipment known to the art.


2 According to a less preferred embodiment, the said filler(s) blend is/are treated with the superplastifier(s) after having being introduced in the kneading or mixing device (“inside treatment”). In such a case, the said filler(s) blend is/are efficiently treated with the superplastifier(s) after having being introduced in the kneading or mixing device (“inside treatment”) with the filler(s) blend and the efficient treating amount of the superfluidifier treating agent(s) being introduced in the kneading or mixing device either simultaneously or in a manner such that the filler(s) blend and the efficient amount of the superplastifer(s) treating agent(s) are introduced separately BUT at a very close location and time.


3 According to another embodiment, the said filler(s) blend is/are efficiently treated with the superplastifier(s) partially before being introduced in the kneading or mixing device (“partial pre-treatment”) (such as in a well-known Lödige equipment) and partially after having been introduced in the pre-treated state in the said mixing or kneading device, the total of the two partial superplastifier(s) treatments being “efficient” in terms of treatment, surface coverage etc. as defined above (“mixed treatment”), with the second part or amount of the superplastifier(s) treating agent(s) being introduced in the kneading or mixing device either simultaneously with the pre-treated fillers blend or in a manner such that the pretreated filler(s) blend and the second part of the superplastifier(s) treating agent(s) are introduced separately BUT at a very close location and time.


When the filler(s) blend is/are to be treated at least partially inside the kneading or mixing device, (“mixed treatment”), the skilled man will understand that a corresponding amount or proportion of treating superplastifier(s) has to be added directly into the said kneading or mixing device or in admixture with the considered fillers blend just before the introduction in the kneading or mixing device, in the latter case, for example, on the weighting device (“balance”) which is provided just before the powdered products are introduced into the kneading or mixing device. “Just before” will be easily understood as a place and time where the fillers blend and superplastifier(s) treating agents cannot or have no time to be mixed together, what would induce the beginning of the treatment. A good example is the balance where the two powders (fillers blend and superplastifier(s)) are placed together then almost immediately introduced, with no previous kneading or mixing, into the kneading or mixing device.


It is much preferred that the point and time of introduction of the said proportion of superplastifier(s) treating agent be as close as possible to the point and time of introduction of the partially treated filler(s), so as not to be diluted in the pre-existing products already present in the mixing or kneading device (such as sand, gravel, mix water, optionally routine additives, so that the treating agent be fully available for the filler(s).


This is also true in relation with the option “inside treatment”.


In both options, actually, if the fillers blend is added at a location and at a time too far form the location and time of the superplastifier(s) treating agent, whatever the order of introduction, one could shift to a treatment which would be too late: this would actually make possible for the treating agent to be “consumed” by other ingredients before the filler is introduced, or, in the case of a fillers blend introduced first, lead to a late treatment (“post-addition” of the treating agent(s) a certain time after the fillers blend has been introduced; the results are far lower than with a pre-treatment, a mixed treatment or an inside treatment according to the invention).


Any post ajout has to be avoided.


The invention also covers an industrial option characterized in that at least a portion of the efficient amount of treating superplastifier(s), or the totality of the said efficient amount, is mixed with the fillers blend on the weighting device (“balance”) leading to the kneading or mixing device. This can be regarded either as a simultaneous addition, or a “near-simultaneous” addition.


It is also possible to envision a process of the invention in which a portion of the fillers blend is efficiently “pretreated” and a second portion of the fillers blend is efficiently treated “inside” the kneading or mixing.


Some of the above options are evidently complicated and/or require additional equipments or modifications of the existing equipment. They are therefore far less preferred, the “pretreatment or initial mode being the most preferred.


The “best mode” to date to avoid those drawbacks is clearly to prepare a pre-treated fillers blend then to deliver it to the end user and to introduce it as such into the kneading or mixing device, most preferably after the mix water and sand and gravel, if any, have been introduced and allowed to be successively malaxed as is usual in this industry (the difference being that, in the present invention, the filler is actually a “the fillers blend” and it is TREATED with superplastifier(s), while it is NOT in the prior art).


The invention also covers the:

    • fillers blend of at least one carbonate-based filler with at least one aluminosiliceous material, per se, as well as the same treated with at least a superplastifier,
    • as novel industrial products,
    • to be delivered to an intermediate user or to the end user that way, optionally after any treatment allowing to ease the transportation.


It is known, in Laboratory trials, and due to the small volumes or loads involved, to sometimes first place some small amount of “fluidifiers” in the bottom of the laboratory mixing device: some of those fluidifiers may be superplastifiers, many are not. However, even when some small amounts of superplastifiers-“fluidifiers” are present, they cannot “treat” the fillers “efficiently” as in the invention, that is according to the definition given hereabove. They merely act as fluidifiers, so that they interact mainly with the other first constituents of the load, such as sand, gravel, mix water etc., which are malaxed together, alone, for a given period of time, so as to conveniently fluidize the particles or aggregates in the suspension; in this operation, they are “fixed” or “consumed” by the said aggregates particles that precisely need to be fluidized. If they were not, there would be no fluidification. Therefore, they are then no longer available for the fillers; even if, to be absolutely complete, we assume for a second that some (mandatorily very small amount) such fluidifier were quite partially and quite marginally available, it could only quite marginally interfere with the filler, that is in any case absolutely not with the “efficient” treatment effect generated by the superplastifiers deliberately added in the present invention.


In the industrial scale, one most generally uses NO fluidifiers, or in some exceptional cases in minute amounts, and in order to “fluidize” the mix: there again, the fluidifiers are “used” to fluidify sand, gravel, etc. and are not available for the fillers, and therefore can in no way “trigger” the “unblocking” of the system, the essential part of the invention.


As indicated hereabove, the said carbonate-based filler(s) are made of calcium carbonate(s) or blends thereof, that is mainly GCCs or PCCs or blends of GCCs or blends of PCCs or blends of GCCs and PCCs.


The invention also covers as new industrial PRODUCTS the said “fillers blend” of fillers and aluminosiliceous material, per se or after having been treated with at least a superplastifier.


The invention also resides in the said “CEMENT COMPOSITIONS” (in the wide sense defined above) comprising the said “fillers blend” of fillers and aluminosiliceous material, treated with at least a superplastifier, and their USE, and in the “CEMENT ELEMENTS or PRODUCTS” so obtained from the said compositions, and their USE in the “cement” industries.


By “CEMENT ELEMENTS or PRODUCTS” it is meant in this whole application each and any piece of building or construction (or any piece or product for any other industrial purpose known to the skilled man, including off-shore cementing, or oil wells cementing, using “cement” compositions) prepared from the said compositions, such as blocks, cement units or shapes etc.





BRIEF DESCRIPTION OF THE FIGURES


FIG. 1: Plot of compressive strength Rc at 28 days as function of % FS/FS+EV



FIG. 2: Plot of ratio of compressive strength Rc 90 days/28 days as function of % FS/FS+EV



FIG. 3: Plot of compressive strength Rc at 28 days as function of % MK/MK+EV



FIG. 4: Plot of ratio of compressive strength Rc 90 days/28 days as function of % MK/MK+EV



FIG. 5: Plot of compressive strength Rc at 28 days as function of % FS/FS+D15



FIG. 6: Plot of ratio of compressive strength Rc 90 days/28 days as function of % FS/FS+D15



FIG. 7: Plot of compressive strength Rc at 28 days as function of % MK/MK+D15



FIG. 8: Plot of ratio of compressive strength Rc 90 days/28 days as function of % MK/MK+D15



FIG. 9: Plot of compressive strength Rc at 28 days as function of % FS/FS+EV



FIG. 10: Plot of ratio of compressive strength Rc 90 days/28 days as function of % FS/FS+EV



FIG. 11: Plot of compressive strength Rc at 28 days as function of % MK/MK+EV



FIG. 12: Plot of ratio of compressive strength Rc 90 days/28 days as function of % MK/MK+EV



FIG. 13: Plot of compressive strength Rc at 28 days as function of % FS/FS+D15



FIG. 14: Plot of ratio of compressive strength Rc 90 days/28 days as function of % FS/FS+D15



FIG. 15: Plot of compressive strength Rc at 28 days as function of % MK/MK+D15



FIG. 16: Plot of ratio of compressive strength Rc 90 days/28 days as function of % MK/MK+D15



FIG. 17: Plot of Rc90/Rc28% verusus % AlSi/CaCO3+AlSi.





The invention will be detailed herebelow.


DETAILED DESCRIPTION OF THE INVENTION

In a detailed and most preferred (“best mode” as of today) embodiment, the said PROCESS for preparing the said “cement” compositions or systems is characterized by:

    • a) providing a powder of at least a dry calcium carbonate-based filler as defined above, hereafter “filler”;
    • b) mixing or blending the said filter or fillers with at least an aluminosiliceous material as described above, this material replacing a part of the usual filler or fillers;
    • c) treating the resulting “fillers blend” with an efficient treating amount of at least one superplastifier, thus producing a “treated fillers blend”,
    • d) introducing the said treated fillers blend into a kneading or mixing device already containing mix water or a composition of mix water possibly containing routine or “non-interfering” additives (“mix water composition”) (hereafter for simplicity “mixing water”)
    • e) optionally adding before or after the step c), preferably before, aggregates such as sand and/or gravel, and possibly other “non interfering” routine additives or adjuvants,
    • f) kneading or mixing the said load during an efficient period of time,
    • g) recovering the said “cement” composition.


Mix water can be optionally introduced at another point of the process, under a much less preferred option depending on the requisite of the end user.


By “not interfering”, it is meant not interfering or not noticeably with the said considered treatment or inventive process.


By “efficient period of time”, it is meant a total period of time leading to an homogeneous mixture or blend, in the order of 2-15 min, preferably, for the “standard” mixtures or blends, 30-60 s. This will be detailed hereafter.


An example of end-user application is as follows: if the end-user targets medium or “standard” properties for its final cement composition, for example with a final mixing within his facilities in a fixed installation etc. . . . , he will use compositions which are correspondingly simple that is not specifically complex or sensitive in terms of routine additives, superplastifier, fluidifier, filler etc. . . . ; therefore, the end user will have to mix for a relatively short time such as the above 35-65 s.


If to the contrary the end-user targets high-level or very HP properties, he will use correspondingly more complex compositions and more sensitive components, for example a more sensitive filler or superplastifier, or sensitive routine additives aimed at reaching a specific property, etc. . . . and usually he will use less or far less mixing water: therefore he will need to mix for a much longer time such as the above 1-3 to 10-15 min.


As mentioned above, a plastifier can be used as is routinely done, as well as the “bottom tank” fiuidifier also routinely used. That is, a fluidifier such as CHRYSO Premia 196 usually placed in the kneading tank or vessel before adding the other ingredients of the “cement”.


The optimum is a treatment in the presence of between 3 and 4 g of fluidifier, such as 3.4-3.7 g, preferably 3.5 g/dry weight of the total cement composition.


The main essential criteria for the final product must be homogeneous and “fluid” what can be easily checked by any skilled man by performing some routine cone tests.


The above working principals are well known to the skilled man and are for completeness only. The above values and examples are to provide guidelines only, which the skilled man will be able to easily use in order to meet the essential “main criteria”.


One will understand that it is impossible to provide examples or data for any type of ultimate composition or ingredient, since the interactions are complex, so are the kinetics etc. . . . but the skilled man knows about those parameters.


By “just after” it is meant that the treating agent can be introduced before of after the un-treated filler(s), but in the second case it must be introduced rapidly after the filler(s), say, in a matter of some seconds to 10 s or so, in order for the filler to remain fully available for the treating agents without any disturbance due to the kneading or mixing with sand, gravel etc.


It is usually most preferred to first introduce the aggregates such as sand and gravel into the kneading or mixing device, and mix them optionally with a small amount of water and/or of fluidifier (see above), before performing the other steps.


As treatment agent, is used at least one superplastifier (and possibly at least one superplasticizer with possibly some inert amount of plasticizer).


According to the above definition of the treating agent, the so called treating agents for the fillers consist of/or comprise superplastifier(s), or comprise at least one superplastifier (and optionally at least one plastifier in order to reduce the overall costs), and preferably consist of at least one superplastifier and optionally at least one efficiently cost-reducing amount of plastifier, and most preferably one superplastifier and optionally one efficiently cost-reducing amount of a plasticizer.


Superplastifiers are well-known agents and are to the best selected among the following products or families and their blends:


Polycarboxylates, polycarboxylate ethers, or much less preferred products manufactured from sulfonated naphthalene condensate or sulfonated melamine formaldehyde. The skilled man knows these products, which are additionally disclosed in the prior art as cited above.


One will use preferably sodium salts of polyether carboxylates which are disclosed, as well as their preparation, in U.S. Pat. No. 5,739,212.


In this invention, the best mode treating agents (product A and product B defined in the above EPA) appear to be, in the superplastifiers families, of the polycarboxylate ether formulae.


Superplastifier(s) and especially Products A and B are disclosed in WO 2004/041882.


To be noted, the products codes A to K in Table A are FILLERS to be characterized, NOT to create a confusion with the preferred treating agent(s) A and B above which are (superplastifiers(s)).


By “efficient period of time” it is meant here a period of time of about 35-65 s for the standard compositions, and from 1-3 to 10-15 min. for the more “technical” that is more complex and/or more sensitive compositions, as is known from the skilled man.


For a composition comprising a “low” carbonate-based filler, an example can be a kneading time of 10-15-20 s for the gravel and sand (dry kneading or mixing is preferred), then of 10 s for the kneading or mixing of the hydraulic binder and untreated filler, then 10-15 s for the kneading or mixing with the treatment agent(s) and mix water, then 5-15 s for the final kneading or mixing with the final “routine additives”.


The main and essential criteria for the said “period of mixing” is that the final product must be homogeneous and fluid at the cone test and the treating agent(s) be not absorbed or adsorbed onto the sand or gravel, or the the less possible extent.


By “efficient amount” of plasticizer (when present with the superplastifier) it is meant in this application an amount or proportion of plastifier which is able to reduce the cost of the treatment without interfering negatively with the system and namely the filler(s) behaviour, namely in terms of surface activity and reactivity) the same criteria applies to the “inert additives”.


By “comprising” we mean here that the said treatment agents consist essentially or entirely of superplastifier(s) as defined, and may contain as explained a cost-reducing efficient amount of at least one plastifier, and may also contain inert additives useful for the intended final application, such as anti foam agents, retarders, accelerators etc. absolutely known to the skilled man.


Usual additives of inert nature can be added at injection points known to the skilled man, as said earlier.


The mixing or kneading device can be operated in a batch mode, a semi-continuous mode, or a continuous mode, the adaptations being within the easy reach of an average skilled man.


Dosage of Superplastifier(s) Used for the Pre-Treatment and Treatment of the Filler(s)

At the end-user location, the dosage in superplastifier(s) is ranging from 0.03 or 0.05 to 0.1% to 2-3% dry weight of cement, or 0.3 to 2-3 kg for 100 kg of cement, preferably 0.8 to 1.2 kg/100 kg of cement, on a DRY/DRY basis.


In laboratory conditions, the same proportion ranges from 0.05 to 0.1% by weight of the carbonate (DRY) that is 0.1 to 0.3 kg/100 kg of cement, on a DRY/DRY basis.


In laboratory conditions, for establishing the Table A, one used from 0.8 to 1.1 kg/100 kg cement, on a DRY/DRY basis.


At the end user location, the ratio superplastifier(s)/plasticizer(s) can be from 100/0 to 95/5-90/10, preferably no less than 85/15 on a weight dry basis.


The invention also resides in the said CEMENT (in the broad sense given above that is cement, cementitious compositions, mortars, concretes) COMPOSITIONS (OR SYSTEMS)

    • per se, since they are distinguishable from the prior art similar compositions by their physical structure and their properties,
    • or as prepared by the above process of the invention,


      and in the USE of those cement systems or compositions for making concrete elements,


      and ultimately in the CEMENT ELEMENTS such as blocks for building and construction etc.
    • per se, since they are distinguishable for the same reasons as the compositions,
    • and as prepared by using the said compositions.
    • as well as in the
    • calcium carbonate-based filler(s) blended with an aluminosiliceous material according to the invention, per se,
    • or as pre-treated by the superplastifier(s) pretreatment process of the invention.


Another objective is evidently to meet Clients requirements which are that the “galette” or “cone” or “cone spread” be above 350 mm in diameter, most preferably 400 mm, or still better, above 420 mm, at a cost-effective dosage.


The main purpose of this invention is to reach high values for the mechanical strength especially at 7 days, and still more at 28 and 90 days, so that in certain cases, a diameter of only 300 mm can be tolerated if the RC 28 d and 90 d are quite satisfactory.


This criteria can be easily and quickly appreciated by a skilled man by performing the cone and plate test, and by visual inspection showing a “fluid” cement composition (that is not dry, not plastic, and featuring a good flow rate). The skilled man how to appreciate those objective or subjective criterias on the basis of the general common knowledge.


This test allows therefore to discriminate the fillers and select the best-performing filler and even the best performing superplastifier(s), in view of the final properties required by the end user.


It is necessary to keep in mind that, for a concrete composition or system to be acceptable as HP composition, or upgraded from low or medium quality to HP quality, TWO features MUST be met simultaneously:

    • the diameter of the “galette” or cone must be above about 350, or better above 400, or still better above 420 mm, AND
    • the “galette” or cone must NOT be sticky or thick in consistency.


In addition, the present invention ensures very high values for Rc7 d, and especially Rc28 d and Rc90 d.


This is another measurement of the very tough challenge which this invention wishes to overcome, and of the very high technical and scientific input brought by the invention to the current state of the art.


As can be seen from the attached Table A, the “poor” fillers can NOT be upgraded since they never meet BOTH features.


This is also true for some “medium” fillers such as product D, B, G, I and K which may show a good fluidity for example at a dosage of 4 g BUT have a bad aspect or handling behaviour.


With the help of the Table A and of the above and below comments, the skilled man will be able to discriminate the fillers which CAN be upgraded by the invention, and those (regarded as “low” as per the test of the Table A) which can NOT.


To achieve these objectives, the skilled man bears in mind first that a certain water/cement ratio is directly linked to the workability of the composition and that it is also imperative to develop high performance qualities in the end product, such as high performance or “technical” level of setting properties, drying properties, mechanical strength, namely compressive strength etc.


Two superplastifiers products are providing the best results. They are the “best mode” as of the filing date (products A and B of the polycarboxylate ether family) as mentioned above.


It is very surprising to notice that when using the invention, proportions of superplastifier(s) treating agent(s) for the CaCO3 filler(s) as low as 0.03 or 0.05 to 0.1-0.2% are sufficient (/dry weight of the cement). It is entirely surprising to notice that such minuscule amounts of treating agents are capable of ensuring high Rc28 d and 90 d and an upgrade to HP quality for even medium to poor and “difficult” fillers, see in particular marbles and certain specific knowingly “difficult” carbonates such as from Ecouché (Betocarb EC™ d50=about 7 μm).


Some usual additives may be routinely added such as air entrainment agents, setting retarders or accelerators etc. at a place which is known from the skilled man, for example with the water or after the superplastifiers are added.


As to the “powders” that is the cement and the filler, the cement can be added first, then the filler, or the reverse, or they can be introduced together as a premix.


It is however preferred to introduce the cement and the treated filler together as a premix, so as to better ensure that both powders will be homogeneously mixed with and wet with the water.


The above are batch modes.


One can also think of continuous modes such as performing the addition in one of the above orders, for example in a kneading or mixing device equipped with an endless screw (with additions at various points along the length of the equipment), possibly with pre-mixes being added at some point(s), or as another example in a series of successive kneading or mixing devices, also with the possibility of adding premix(es) in one of the devices. It will be obvious to the skilled man that especially the latter option (several kneading or mixing devices) has numerous drawbacks, if only the necessary space and investment.


Batch modes are preferred and will be referred to here-below.


Routine tests can help the skilled man to select the most appropriate, in view of the available equipment, of the end user practice, and with the help of the following Tables and Figures which are attached to this application.


Dosage of the Alumino-Siliceous Material/Carbonate-Based Filler(s)

The dosage of the SiO2/Al2O3 aluminosiliceous material can represent 8.5 to 100%, preferably 8.5 to 40, or 10 to 70-85/dry weight of carbonate-based filler(s), preferably 30-35-40%/dry weight of carbonate-based filler(s).


As will be seen below, an optimum has been surprisingly discovered around 35% alumino-siliceous material/around 65% (total being 100%) carbonate-based filler(s)/dry weight of carbonate-based filler(s); this optimum allows to reduce the needed amount of superplastifier(s).


In the following examples, except if otherwise stated, the cement brand is the standardized cement 42,5 R Gaurain (CEM) having a water demand of 24.2%, and the sand is Standardized sand under Standard EN 196-1 (SAN).


EXAMPLES
Example 1
Refers to Table B and Corresponding FIGS. 1 to 8




















TABLE B














SiO2/
Flow






Cement
Sand
Water
Filler
A
Al2O3
table
Rc 28d
Rc 90d



















Test
Ref.
g
g
g
g
g
%
g
%
mm
MPa
Rc90/28
























Specimen
E1
ST
472
1676
260
0
0.0
0.0
0
 0%
200





EV
E2
MO
472
1645
223
142
2.2
0.5
0
 0%
206
45
32
0.7


EV + FS
E3
M1
472
1645
223
131
2.4
0.5
11
 8%
204
51
41
0.8


EV + FS
E4
M2
472
1645
223
119
2.9
0.6
23
16%
208
66
52
0.8


EV + FS
E5
M3
472
1645
223
107
3.3
0.7
35
25%
206
75
71
0.9


EV + FS
E6
M4
472
1645
223
92
3.8
0.8
50
35%
200
81
75
0.9


EV + FS
E7
M5
472
1645
223
0
0.0
0.0
142
100% 
0
0
0
0.0


Specimen
E8
ST
472
1676
260
0
0.0
0.0
0
 0%
205


0.0


EV + FS
E9
M6
472
1645
223
71
3.0
0.6
71
50%
191
46
50
1.1


EV + FS
E10
M7
472
1645
223
35
4.0
0.8
107
75%
180
57
54
0.9


Specimen
E11
ST
472
1676
260
0
0.0
0.0
0
 0%
203


EV
E12
MO
472
1645
223
142
2.2
0.5
0
 0%
209
42
35
0.8


EV + MK
E13
M1
472
1645
223
131
2.6
0.6
11
 8%
200
38
37
1.0


EV + MK
E14
M2
472
1645
223
119
3.2
0.7
23
16%
208
50
45
0.9


EV + MK
E15
M3
472
1645
223
107
3.6
0.8
35
25%
200
57
50
0.9


EV + MK
E16
M4
472
1645
223
92
4.1
0.9
50
35%
201
65
66
1.0


EV + MK
E17
M5
472
1645
223
0
8.3
1.8
142
100% 
203
111
104
0.9


Specimen
E18
ST
472
1676
260
0
0.0
0.0
0
 0%
205


0.0


EV + MK
E19
M6
472
1645
223
71
3.0
0.6
71
50%
182
40
33
0.8


EV + MK
E20
M7
472
1645
223
35
4.5
1.0
107
75%
189
55
45
0.8


Specimen
E21
ST
472
1676
260
0
0.0
0.0
0
 0%
205


Betocarb SL
E32
MO
472
1645
223
142
2.5
0.5
0
 0%
197
20
15
0.8


Betocarb SL + FS
E23
M4
472
1545
223
92
3.0
0.6
50
35%
199
40
38
0.9


Betocarb SL + FS
E24
M6
472
1645
223
71
4.0
0.8
71
50%
208
68
55
0.8


Betocarb SL + FS
E25
M7
472
1644
223
35
5.0
1.1
107
75%
200
63
49
0.8


Specimen
E26
ST
472
1676
260
0
0.0
0.0
0
 0%
205


Betocarb SL
E27
MO
472
1645
223
142
2.5
0.5
0
 0%
197
20
15
0.8


Betocarb SL + MK
E28
M4
472
1645
223
92
3.8
0.8
50
35%
197
46
42
0.9


Betocarb SL + MK
E29
M6
472
1645
223
71
5.0
1.1
71
50%
190
54
39
0.7


Betocarb SL + MK
E30
M7
472
1645
223
35
6.0
1.3
107
75%
192
62
52
0.8









In this test, a calcium carbonate filler respectively selected among


EV (violet label or etiquette Violette™) (ultrafine carbonate filler from Omey, France) d50=2.4-2.5 microns Blaine>1000 m2/kg and BET=2.3 m2/g or


Betocarb SL™ coarse carbonate filler from Salses, France d50=11-12 microns Blaine surface=320-365 m2/g


Is pre-mixed with an aluminosiliceous material, either:


SF (or FS) silica fume (ultrafine filler) d50=1.2 micron Blaine>1500 m2/kg and BET=16 m2/g or


MK (metakaolin) (ultrafine filler) d50=3 microns BET=3.8 m2/g.


“Specimen” is a test without treatment with an aluminosiliceous material and without a treatment with any superplastifier.


EV (test E2) or Betocarb SL (test E22) (etc. . . . ) are blank tests with no is aluminosiliceous material but with a treatment with Product B superplastifier.


EV+FS means that EV has been mixed in the indicated proportion (8%, 16% etc. . . . ) with FS (column SiO2/Al2O3) (the total remaining 142 g example E3 131 g+11 g) AND the mix (fillers blend) has been treated by the fluidifier in the % indicated.


Compressive strength (RC or Rc) at 28 days and 90 days are indicated, as well as the ratio of RC 90 d/RC 28 d.


Results are represented as schemes on FIGS. 1 to 8 which are self-explaining.


Example 2
Refers to Table C and FIGS. 9-16




















TABLE C














SiO2/
Flow






Cement
Sand
Water
Filler
A
Al2O3
table
Rc 28d
Rc 90d



















Bst
Ref.
g
g
g
g
g
%
g
%
mm
MPa
Rc90/28























Specimen
ST
472
1676
260
0
0.0
0.0
0
 0%
212





EV
MO
472
1534
250
142
0.0
0.0
0
 0%
208
19
11
0.6


EV + SF
M1
472
1534
258
131
0.0
0.0
11
 8%
206
24
16
0.7


EV + SF
M2
472
1534
260
119
0.0
0.0
23
16%
206
29
34
0.8


EV + SF
M3
472
1534
273
107
0.0
0.0
35
25%
200
34
30
0.9


EV + SF
M4
472
1534
273
92
0.0
0.0
50
35%
200
44
35
0.8


EV + SF
M5
472
1534
341
0
0.0
0.0
142
100% 
0
30
26
0.0


Specimen
ST
472
1676
260
0
0.0
0.0
0
 0%
205


0.0


EV + SF
M6
472
1534
283
71
0.0
0.0
71
50%
185
26
21
0.8


EV + SF
M7
472
1534
303
35
0.0
0.0
107
75%
181
11
7
0.6


Specimen
ST
472
1676
260
0
0.0
0.0
0
 0%
203


EV
MO
472
1534
250
142
0.0
0.0
0
 0%
203
19
18
0.9


EV + MK
M1
472
1534
255
131
0.0
0.0
11
 8%
205
23
19
0.8


EV + MK
M2
472
1534
258
119
0.0
0.0
23
16%
201
27
26
1.0


EV + MK
M3
472
1534
266
107
0.0
0.0
35
25%
200
30
29
1.0


EV + MK
M4
472
1534
275
92
0.0
0.0
50
35%
204
31
35
1.1


EV + MK
M5
472
1534
293
0
0.0
0.0
142
100% 
193
43
25
0.0


Specimen
ST
472
1676
260
0
0.0
0.0
0
 0%
205


0.0


EV + MK
M6
472
1534
283
71
0.0
0.0
71
50%
208
15
15
1.0


EV + MK
M7
472
1534
303
35
0.0
0.0
107
75%
206
20
15
0.8


Specimen
ST
472
1676
260
0
0.0
0.0
0
 0%
205


Betocarb SL
MO
472
1534
253
142
0.0
0.0
0
 0%
195
4
3
0.8


Betocarb SL + FS
M4
472
1534
265
92
0.0
0.0
50
35%
183
28
19
0.7


Betocarb SL + FS
M6
472
1534
230
71
0.0
0.0
71
50%
180
20
17
0.9


Betocarb SL + FS
M7
472
1534
303
35
0.0
0.0
107
75%
180
18
14
0.8


Specimen
ST
472
1676
260
0
0.0
0.0
0
 0%
205


Betocarb SL
MO
472
1534
253
142
0.0
0.0
0
 0%
195
4
3
0.8


Betocarb SL + MK
M4
472
1534
265
92
0.0
0.0
50
35%
189
22
18
0.8


Betocarb SL + MK
M6
472
1534
280
71
0.0
0.0
71
50%
198
16
17
1.1


Betocarb SL + MK
M7
472
1534
303
35
0.0
0.0
107
75%
213
21
13
0.6









This example is identical to Example 1 with the difference that the blend of fillers has NOT been treated with superplastifier A (column A=0%). It can be seen that the RC are lower in this example 2 as compared to example 1 what shows the synergy between the preblend (or “fillers blend”) and the treatment of that fillers blend with a superplastifier.


One can draw a surprising conclusion from table C which is that, without adding any superplastifier, and by varying from 0% to 100% the proportion of aluminosiliceous material/dry weight of filler CaCO3, there exists:

    • for the case where the filler is EV and the aluminosiliceous is Silica Fume Sifraco C800 (d50=2.4 μm, BET=2.7 m2/g)
    • an optimum of Rc at 28 d (Rc28 d=44) and Rc at 90 d (Rc90 d=35)
    • for an optimum of 35% UF (here silica fume)/65% CaCO3 filler (here EV), by dry weight.
    • This is also valid for 65% Betocarb SL/35% SF (Rc28 d=maximum 28 and Rc90 d=maximum 19).
    • To the contrary, with metakaolin, there does not seem to appear a clear optimum, see for example the Rc28 d of EV/MK rising from 19 to 43 while however Rc90 d shows a maximum value also at 35% MK (Rc90 d=35 then drops to 25 at 100% MK)


Therefore, the present tests have detected an optimum ratio of about 35% aluminosiliceous material/about 65% CaCO3 filler (by dry weight).


The invention therefore also covers the specific new industrial product comprising or consisting of:

    • about 35% aluminosiliceous material/about 65% CaCO3 filler (by dry weight)
    • namely 35% aluminosiliceous material/65% CaCO3 filler (by dry weight)
    • namely 35% Silica fume/65% UF CaCO3 filler
    • namely 35% Silica fume/65% EV CaCO3 filler


Example 3
Refers to Tables D to M

Two series of tests have been conducted.


Module 1:


one uses a fixed formulation for a mortar, which is given in Table D, with adjustment only on the dispersing agent proportion. The purpose of the “adjustment” is to reach a cone “mortar diameter” of between 300 and 400 mm with a somewhat plastic mortar















TABLE D








SiO2/Al2O3 = 0%
SiO2/Al2O3 = 35%
SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%



Standard
CaCO3 = 100%
CaCO3 = 65%
CaCO3 = 50%
CaCO3 = 25%





















Reference
ST
M0
M4
M6
M7


% Tested ultrafine SiO2 Al2O3
0
0
35
50
75


% Violet Label or Betocarb SL
0
100
65
50
25


Mass of tested SiO2/Al2O3
0
0.0
49.7
71.0
106.5


Mass of Violet Label or Betocarb SL
0
142.0
92.3
71.0
35.5


Dispersing agent quantity
0
adjusted
adjusted
adjusted
adjusted


Total quantity (SiO2/Al2O3 + CaCO3)
0
142.0
142.0
142.0
142.0


Cement: CEM I 42.5R de Gaurain
472
472
472
472
472


Sand
1676
1645
1645
1645
1645


Water
260
223
223
223
223


% of dispersing agent dry/dry
0
calculated
calculated
calculated
calculated



0
142
142
142
142


% (SiO2—Al2O3)/Cement
0
0.00
0.11
0.15
0.23


Water/Cement ratio
0.55
0.47
0.47
0.47
0.47








Mortar diameter (mm)
Must be between 300 and 400 mm



















TABLE E







SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


VIOLET LABEL + SILICA FUME
Standard
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M6
M7


% Tested ultrafine SiO2 Al2O3
0
50
75


% Violet Label
0
50
25


Mass of tested SiO2/Al2O3
0
71.0
106.5


Mass of Violet Label
0
71.0
35.5


Dispersing agent quantity (g)
0
3
4


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472


Sand (g)
1676
1645
1645


Water (g)
260
223
223


% of dispersing agent dry/dry
0
0.74
0.98


% (SiO2—Al2O3)/Cement
0
0.15
0.23


Water/Cement ratio
0.55
0.47
0.47


Mortar diameter (mm)
205
191
180


Weight (g)
1717
1697
1685


Weight H2O (g)
973
941
928


Formulation volume
1.04
1.11
1.07


28 d resistances
74.7
109.3
117.4


28 d gain

46
57


90 d resistances
85.8
128.3
132.1


90 d gain

50
54



















TABLE F







SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


VIOLET LABEL + METAKAOLIN
Standard
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M6
M7


% Tested ultrafine SiO2 Al2O3
0
50
75


% Violet Label
0
50
25


Mass of tested SiO2/Al2O3
0
71.0
106.5


Mass of Violet Label or Betocarb SL
0
71.0
35.5


Dispersing agent quantity (g)
0
3
4.5


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472


Sand (g)
1676
1645
1645


Water (g)
260
223
223


% of dispersing agent dry/dry
0
0.74
1.11


% (SiO2—Al2O3)/Cement
0
0.15
0.23


Water/Cement ratio
0.55
0.47
0.47


Mortar diameter (mm)
205
182
189


Weight (g)
1717
1708
1712


Weight H2O (g)
973
956
956


Formulation volume
1.04
1.09
1.05


28 d resistances
74.7
104.7
116.1


28 d gain

40
55


90 d resistances
85.8
114.2
124.3


90 d gain

33
45





















TABLE G







SiO2/Al2O3 = 0%
SiO2/Al2O3 = 35%
SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


BETOCARB SL + SILICA FUME
Standard
CaCO3 = 100%
CaCO3 = 65%
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M0
M4
M6
M7


% Tested ultrafine SiO2 Al2O3
0
0
35
50
75


% Betocarb SL
0
100
65
50
25


Mass of tested SiO2/Al2O3
0
0.0
49.7
71.0
106.5


Mass of Violet Label or Betocarb SL
0
142.0
92.3
71.0
35.5


Dispersing agent quantity (g)
0
2.5
3
4
5


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472
472
472


Sand (g)
1676
1645
1645
1645
1645


Water (g)
260
223
223
223
223


% of dispersing agent dry/dry
0
0.61
0.74
0.98
1.23


% (SiO2—Al2O3)/Cement
0
0.00
0.11
0.15
0.23


Water/Cement ratio
0.55
0.47
0.47
0.47
0.47


Mortar diameter (mm)
205
197
199
202
195


Weight (g)
1717
1775
1690
1715
1692


Weight H2O (g)
973
1023
936
961
938


Formulation volume
1.04
1.05
1.11
1.09
1.06


28 d resistances
74.7
89.9
104.3
125.3
122


28 d gain

20
40
68
63


90 d resistances
85.8
98.8
118.4
132.9
128.3


90 d gain

15
38
55
49





















TABLE H







SiO2/Al2O3 = 0%
SiO2/Al2O3 = 35%
SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


BETOCARB SL + METAKAOLIN
Standard
CaCO3 = 100%
CaCO3 = 65%
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M0
M4
M6
M7


% Tested ultrafine SiO2 Al2O3
0
0
35
50
75


% Betocarb SL
0
100
65
50
25


Mass of tested SiO2/Al2O3
0
0.0
49.7
71.0
106.5


Mass of Violet Label or Betocarb SL
0
142.0
92.3
71.0
35.5


Dispersing agent quantity (g)
0
2.5
3.8
5
6


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472
472
472


Sand (g)
1676
1645
1645
1645
1645


Water (g)
260
223
223
223
223


% of dispersing agent dry/dry
0
0.61
1.08
1.23
1.48


% (SiO2—Al2O3)/Cement
0
0.00
0.11
0.15
0.23


Water/Cement ratio
0.55
0.47
0.47
0.47
0.47


Mortar diameter (mm)
205
197
197
190
192


Weight (g)
1717
1775
1730
1769
1766


Weight H2O (g)
973
1023
979
1021
1013


Formulation volume
1.04
1.05
1.08
1.05
1.01


28 d resistances
74.7
89.9
109.3
114.7
121


28 d gain

20
46
54
62


90 d resistances
85.8
98.8
121.8
119.7
130.4


90 d gain

15
42
39
52









Precise formulations and RC results are given in Tables:


E tested ultrafine aluminosiliceous SiO2/Al2O3=silica fume (SF) Sifraco™ C800 98% SiO2


Filler is an UF: violet label or EV


F same as E except that SF is replaced with metakaolin


G same as E (tested SF) except that the filler EV is replaced with a coarse filler CaCO3 Betocarb SL


H same as G except that the tested SF is replaced with metakaolin. Dispersing agent=Chryso Premia 196


The filler blend is treated in each case with Product B.


In each test, the aluminosiliceous material is tested at 0, 50 or 75% dry weight/CaCO3.


One can note a remarkable gain in RC at 28 days and 90 days.


From attached FIG. 17 it can be seen that the ratio Rc90 d/Rc28 d as a function of the % alumino-siliceous material/alumino-siliceous material+carbonate based filler (in dry weight) is low when there is no AlSi material (namely no SF), is quite good (close to 1 what means that there is almost no loss in Rc between 25 and 75%, with even a value above 1 (what means, there is a gain in Rc between 28 and 90 days) at 50%. It can also be seen that there is a sudden drop between 75% and 100%.


Module 2:


one uses a fixed formulation for a mortar, which is given in Table I, with adjustment only on water proportion.















TABLE I








SiO2/Al2O3 = 0%
SiO2/Al2O3 = 35%
SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%



Standard
CaCO3 = 100%
CaCO3 = 65%
CaCO3 = 50%
CaCO3 = 25%





















Reference
ST
M0
M4
M6
M7


% Tested ultrafine SiO2 Al2O3
0
0
35
50
75


% Violet Label or Betocarb SL
0
100
65
50
25


Mass of tested SiO2/Al2O3
0
0.0
49.7
71.0
106.5


Mass of Violet Label or Betocarb SL
0
142.0
92.3
71.0
35.5


Total quantity (SiO2/Al2O3 + CaCO3)
0
142.0
142.0
142.0
142.0


Cement: CEM I 42.5R de Gaurain
472
472
472
472
472


Sand
1676
1534
1534
1534
1534


water
260
adjusted
adjusted
adjusted
adjusted


% (SiO2—Al2O3)/Cement
0
0.00
0.11
0.15
0.23


Water/Cement ratio
0.55
calculated
calculated
calculated
calculated








Mortar diameter (mm)
Must be between 300 and 400 mm



















TABLE J







SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


VIOLET LABEL + SILICA FUME
Standard
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M6
M7


% Tested ultrafine SiO2 Al2O3
0
50
75


% Violet Label
0
50
25


Mass of tested SiO2/Al2O3
0
71.0
106.5


Mass of Violet Label
0
71.0
35.5


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472


Sand (g)
1676
1534
1534


Water (g)
260
283
303


% (SiO2—Al2O3)/Cement
0
0.15
0.23


Water/Cement ratio
0.55
0.60
0.64


Mortar diameter (mm)
205
185
181


Weight (g)
1717
1699
1660


Weight H2O (g)
973
935
899


Formulation volume
1.04
1.09
1.08


28 d resistances
74.7
94.4
83


28 d gain

26
11


90 d resistances
85.8
103.5
91.7


90 d gain

21
7



















TABLE K







SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


VIOLET LABEL + METAKAOLIN
Standard
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M6
M7


% Tested ultrafine SiO2 Al2O3
0
50
75


% Violet Label
0
50
25


Mass of tested SiO2/Al2O3
0
71.0
106.5


Mass of Violet Label
0
71.0
35.5


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472


Sand (g)
1676
1534
1534


Water (g)
260
283
303


% (SiO2—Al2O3)/Cement
0
0.15
0.23


Water/Cement ratio
0.55
0.60
0.64


Mortar diameter (mm)
205
208
206


Weight (g)
1717
1714
1699


Weight H2O (g)
973
956
942


Formulation volume
1.04
1.08
1.04


28 d resistances
74.7
86.2
89.8


28 d gain

15
20


90 d resistances
85.8
98.4
99.1


90 d gain

15
15





















TABLE L







SiO2/Al2O3 = 0%
SiO2/Al2O3 = 35%
SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


BETOCARB SL + SILICA FUME
Standard
CaCO3 = 100%
CaCO3 = 65%
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M0
M4
M6
M7


% Tested ultrafine SiO2 Al2O3
0
0
35
50
75


% Betocarb SL
0
100
65
50
25


Mass of tested SiO2/Al2O3
0
0.0
49.7
71.0
106.5


Mass of Violet Label
0
142.0
92.3
71.0
35.5


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472
472
472


Sand (g)
1676
1534
1534
1534
1534


Water (g)
260
253
265
280
303


% (SiO2—Al2O3)/Cement
0
0.00
0.11
0.15
0.23


Water/Cement ratio
0.55
0.54
0.56
0.59
0.64


Mortar diameter (mm)
205
195
183
180
180


Weight (g)
1717
1714
1705
1672
1657


Weight H2O (g)
973
967
945
919
899


Formulation volume
1.04
1.05
1.08
1.09
1.07


28 d resistances
74.7
77.6
95.7
90
88.2


28 d gain

4
28
20
18


90 d resistances
85.8
88.2
102.3
100.6
97.4


90 d gain

3
19
17
14





















TABLE M







SiO2/Al2O3 = 0%
SiO2/Al2O3 = 35%
SiO2/Al2O3 = 50%
SiO2/Al2O3 = 75%


BETOCARB SL + METAKAOLIN
Standard
CaCO3 = 100%
CaCO3 = 65%
CaCO3 = 50%
CaCO3 = 25%







Reference
ST
M0
M4
M6
M7


% Tested ultrafine SiO2 Al2O3
0
0
35
50
75


% Betocarb SL
0
100
65
50
25


Mass of tested SiO2/Al2O3
0
0.0
49.7
71.0
106.5


Mass of Violet Label
0
142.0
92.3
71.0
35.5


Total quantity (SiO2/Al2O3 + CaCO3) (g)
0
142.0
142.0
142.0
142.0


Cement: CEM I 42.5R de Gaurain (g)
472
472
472
472
472


Sand (g)
1676
1534
1534
1534
1534


Water (g)
260
253
265
280
303


% (SiO2—Al2O3)/Cement
0
0.00
0.11
0.15
0.23


Water/Cement ratio
0.55
0.54
0.56
0.59
0.64


Mortar diameter (mm)
205
195
189
198
213


Weight (g)
1717
1714
1726
1685
1694


Weight H2O (g)
973
967
968
940
939


Formulation volume
1.04
1.05
1.06
1.07
1.05


28 d resistances
74.7
77.6
91.3
86.9
90.6


28 d gain

4
22
16
21


90 d resistances
85.8
88.2
101.2
100
96.6


90 d gain

3
18
17
13









Precise formulations and results are given as for. Module 1 in Tables:


J carbonate filler EV

    • Aluminosiliceous material SF Sifraco C800


K carbonate filler EV

    • Aluminosiliceous (AlSi) material MK Premix MK (d50=3, BET=3.8 m2/g)


L carbonate filler Betocarb SL coarse CaCO3

    • Aluminosiliceous material SF Sifraco C800


M carbonate filler Betocarb SL

    • Aluminosiliceous MK


We note as in Module 1 an important gain in RC 28 d and RC 90 d.


Example 4
Refers to Tables N, O, P

























TABLE N
















Consis-
Air
Water
den-







Sand
Cement
Filler
Ultrafine
Ultrafine
Water
Additive
tancy
mass
mass
sity
Rc28d
%
Rc90d































g

g

g

%
g

%
g
g
F
%
g
mm
g
g
kg/m3
Mpa
rc28d
Mpa
Observation


































Specimen
SAN099
1676
CEM099
472

0


0


0
260

0.00
0.0
200
1757
993
2.30
44.8

water releasing

























(*resuant*)


E1
SAN099
1645
CEM099
472
A
142

0
0


0
223
SP B
0.21
1.0
170
1752
982
2.27
57.4

slightly

























water releasing,

























compact


E2
SAN099
1545
CEM099
472

0
B
100
142


0
223
SP B
0.32
1.5
235
1753
993
2.31
61.3
4
water releasing


E3
SAN099
1645
CEM099
472
A
142
B
0
0


0
223
SP B
0.26
1.3
170
1739
977
2.28
59.0
0
slightly

























water releasing


E4
SAN099
1645
CEM099
472
A
135
B
5
7


0
223
SP B
0.32
1.5
177
1808
1034
2.34
63.8
8
slightly

























water releasing


E5
SAN099
1645
CEM099
472
A
127
B
11
15


0
223
SP B
0.32
1.5
185
1774
1009
2.32
62.5
6
water releasing


E6
SAN099
1645
CEM099
472
A
120
B
15
22


0
223
SP B
0.32
1.5
195
1782
1021
2.34
64.4
9
water releasing


E7
SAN099
1545
CEM099
472
A
113
B
20
29


0
223
SP B
0.32
1.5
193
1754
992
2.30
62.1
5
water releasing


E8
SAN099
1645
CEM099
472
A
142


0
C
0
0
223
SP B
0.32
1.5
177
1739
977
2.28
58.1
0
slightly

























water releasing


E8R
SAN099
1645
CEM099
472
A
142


0
C
0
0
223
SP B
0.42
2.0
195
1806
1040
2.36
65.5
0
slightly

























water releasing


E9
SAN099
1645
CEM099
472
A
114


0
C
20
28
223
SP B
0.32
1.5
155
1735
965
2.25
62.7
−4
slightly

























water releasing,

























no gaz bubble

























(vibrating table)


E9R
SAN099
1645
CEM099
472
A
114


0
C
20
28
223
SP B
0.53
2.5
210
1737
973
2.27
68.1
4
water releasing


E10
SAN099
1645
CEM099
472
A
92


0
C
35
50
223
SP B
0.32
1.5
137
1730
961
2.25
68.2
4
dry and homogeneous,

























no gaz bubble

























(vibrating table)


E10R
SAN099
1645
CEM099
472
A
92


0
C
35
50
223
SP B
0.64
3.0
187
1723
956
2.25
68.8
5
water releasing


E11
SAN099
1645
CEM099
472
A
57


0
C
60
85
223
SP B
0.32
1.5
125
1725
956
2.24
72.8
11
dry and homogeneous,

























no gaz bubble

























(vibrating table)


E11R
SAN099
1645
CEM099
472
A
57


0
C
60
85
223
SP B
0.85
4.0
195
1752
985
2.28
79.8
22
water releasing


E12
SAN099
1645
CEM099
472
A
0


0
C
100
142
223
SP B
0.32
1.5
107
1709
947
2.24
72.1
10
“crumble”,

























no gaz bubble

























(vibrating table)


E12R
SAN099
1645
CEM099
472
A
0


0
C
100
142
223
SP B
1.06
5.0
175
1690
926
2.21
77.1
18
water releasing


E13
SAN099
1645
CEM099
472
A
142


0
D
0
0
223
SP B
0.42
2.0
207
1812
1045
2.36
65.5
0
water releasing


E14
SAN099
1645
CEM099
472
A
114


0
D
20
28
223
SP B
0.64
3.0
210
1822
1053
2.37
72.9
11
water releasing


E15
SAN099
1645
CEM099
472
A
92


0
D
35
50
223
SP B
0.85
4.0
217
1842
1066
2.37
73.8
13
water releasing


E16
SAN099
1645
CEM099
472
A
57


0
D
60
85
223
SP B
1.06
5.0
193
1614
1045
2.36
84.5
29
water releasing


E17
SAN099
1645
CEM099
472
A
0


0
D
100
142
223
SP B
1.27
6.0
160
1743
972
2.26
80.7
23
slightly

























water releasing


E18
SAN099
1645
CEM098
472
A
142


0
E
0
0
223
SP B
0.42
2.0
188
1731
969
2.27
62.0
0
water releasing


E1BR
SAN099
1645
CEM099
472
A
142


0
E
0
0
223
SP B
0.42
2.0
197
1824
1051
2.36


water releasing


E19
SAN099
1645
CEM098
472
A
114


0
E
20
28
223
SP B
0.42
2.0
193
1747
979
2.27
65.2
5
water releasing


E19R
SAN099
1645
CEM099
472
A
114


0
E
20
28
223
SP B
0.42
2.0
190
1785
1018
2.33


water releasing


E20
SAN099
1645
CEM098
472
A
92


0
E
35
50
223
SP B
0.42
2.0
185
1727
963
2.26
61.8
0
water releasing


E20R
SAN099
1645
CEM099
472
A
92


0
E
35
50
223
SP B
0.42
2.0
195
1808
1031
2.33


water releasing


E21
SAN099
1645
CEM098
472
A
57


0
E
60
85
223
SP B
0.42
2.0
180
1724
960
2.26
63.2
2
water releasing


E21R
SAN099
1645
CEM099
472
A
57


0
E
60
85
223
SP B
0.42
2.0
215
1791
1024
2.34


water releasing

























(*très resuant)


E22
SAN099
1645
CEM098
472
A
0


0
E
100
142
223
SP B
0.42
2.0
165
1725
963
2.26
65.6
6
sightly

























water releasing,

























sticky.


E22R
SAN099
1645
CEM099
472
A
0


0
E
100
142
223
SP B
0.53
2.5
240
1830
1055
2.36


water releasing

























(*très resuant)
































TABLE O
















Consis-
air
water
den-







Sand
Cement
Filler
Utrafine
Ultrafine
Water
Additive
tancy
mass
mass
sity
Rc28d
%
Rc90d































g

g

g

%
g

%
g
g
F
%
g
mm
g
g
kg/m3
Mpa
rc28d
Mpa
Observation


































Specimen
SAN099
1676
CEM099
472

0


0


0
260

0.00
0.0
200
1757
993
2.30
44.8

water releasing

























(*resuant*)


E23
SAN099
1645
CEM098
472

0
B

142
C
0
0
223
SP B

2.0
205
1758
987
2.28
62.6
0
water releasing


E23R
SAN099
1645
CEM099
472

0
B

142
C
0
0
223
SP B

2.0
245
1833
1055
2.36


water releasing

























(*très resuant*)


E24
SAN099
1645
CEM099
472

0
B

114
C
19.72
28
223
SP B

2.0
217
1739
972
2.27
66.5
6
water releasing


E25
SAN099
1645
CEM099
472

0
B

92
C
35.21
50
223
SP B

3.0
230
1801
1031
2.34
80.0
28
water releasing;

























Rc 80.3/81.1/74.6


E26
SAN099
1645
CEM099
472

0
B

57
C
59.86
85
223
SP B

4.0
195
1700
934
2.22
72.5
16
water releasing


E27
SAN099
1645
CEM099
472

0
B

0
C
100
142
223
SP B

5.0
195
1686
922
2.21
77.6
24
water releasing


E28
SAN099
1645
CEM099
472

0
B

142
D
0
0
223
SP B

1.0
175
1744
977
2.27
54.7
0
water releasing


E29
SAN099
1645
CEM099
472

0
B

114
D
19.72
28
223
SP B

2.0
213
1764
997
2.30
65.7
20
water releasing


E30
SAN099
1645
CEM099
472

0
B

92
D
35.21
50
223
SP B

3.0
205
1740
974
2.27
66.6
22
water releasing


E31
SAN099
1645
CEM099
472

0
B

57
D
59.86
85
223
SP B

4.0
197
1732
968
2.27
73.7
35
water releasing


E32
SAN099
1645
CEM099
472

0
B

0
D
100
142
223
SP B

6.0
180
1757
993
2.30
85.0
55
slightly

























water releasing

























(*légèrement

























resuant*)


E33
SAN099
1645
CEM099
472

0
B

142
E
0
0
223
SP B

1.5
203
1740
974
2.27
58.7
0
water releasing


E34
SAN099
1645
CEM099
472

0
B

114
E
19.72
28
223
SP B

1.5
187
1744
979
2.28
59.9
2
water releasing


E35
SAN099
1645
CEM099
472

0
B

92
E
35.21
50
223
SP B

1.5
180
1737
974
2.28
60.2
3
water releasing


E36
SAN099
1645
CEM099
472

0
B

57
E
59.86
85
223
SP B

2.0
215
1758
990
2.29
62.3
6
water releasing,

























slightly outgassing


E37
SAN099
1645
CEM099
472

0
B

0
E
100
142
223
SP B

2.0
235
1796
1027
2.34
71.3
21
water releasing

























(*très resuant*),

























outgassing


E38
SAN099
1645
CEM099
472
A
142
B
0
0


0
223
SP B

1.8
185
1797
1031
2.35
63.9

sligthly

























water releasing

























(*légèrement

























resuant*)


E39
SAN099
1645
CEM099
472
A
127
B
10.56
15
C

0
223
SP B

2.0
217
1842
1064
2.37
63.9

water releasing

























(*très resuant*)


E40
SAN099
1645
CEM099
472
A
101
B
28.87
13
C

28
223
SP B

2.0
187
1731
966
2.26
66.9

water releasing


E41
SAN099
1645
CEM099
472
A
81
B
42.96
11
C

50
223
SP B

3.0
220
1785
1014
2.32
79.5

water releasing


E42
SAN099
1645
CEM099
472
A
50
B
64.79
7
C

85
223
SP B

4.0
183
1710
944
2.23
76.0

water releasing


E43
SAN099
1645
CEM099
472

0
B
100
0
C

142
223
SP B

5.0
167
1720
945
2.22
80.7

water releasing

























and sticky


E44
SAN099
1645
CEM099
472
A
142
B
0
0


0
223
SP B

2.0
197
1842
1064
2.37
64.0

water releasing


E45
SAN099
1645
CEM099
472
A
127
B
10.56
15
D

0
223
SP B

2.0
223
1830
1058
2.37
63.4

water releasing

























(*très resuant*)


E46
SAN099
1645
CEM099
472
A
101
B
28.87
13
D

28
223
SP B

2.0
170
1741
974
2.27
64.6

sligthly

























water releasing


E47
SAN099
1645
CEM099
472
A
81
B
42.96
11
D

50
223
SP B

3.0
185
1784
1014
2.32
74.5

water releasing


E48
SAN099
1645
CEM099
472
A
50
B
64.79
7
D

85
223
SP B

4.0
180
1763
1001
2.31
81.6

water releasing


E49
SAN099
1645
CEM099
472

0
B
100
0
D

142
223
SP B

6.0
175
1743
983
2.29
83.6

sligthly

























water releasing

























(*légèrement

























resuant*)


E50
SAN099
1645
CEM099
472
A
142
B
0
0


0
223
SP B

2.0
220
1832
1062
2.38
60.1

water releasing

























(*très resuant*)


E51
SAN099
1645
CEM099
472
A
127
B
10.56
15
E

0
223
SP B

2.0
213
1828
1073
2.42
64.0

water releasing


E52
SAN099
1645
CEM099
472
A
101
B
28.87
13
E

28
223
SP B

2.0
217
1749
1038
2.46
65.6

water releasing


E53
SAN099
1645
CEM099
472
A
81
B
42.96
11
E

50
223
SP B

2.0
233
1815
1046
2.36
68.1

water releasing

























(*très resuant*)


E54
SAN099
1645
CEM099
472
A
50
B
64.79
7
E

85
223
SP B

2.0
235
1820
1043
2.34
69.2

water releasing

























(*très resuant*)


E55
SAN099
1645
CEM099
472

0
B
100
0
E

142
223
SP B

2.0
235
1783
1017
2.33
71.9

water releasing

























(*très resuant*)
























TABLE P















Consis-



Sand
Cement
Filler
Ultrafine
Ultrafine
Water
Additive
tancy


























g

g

g

%
g

%
g
g
F
%
g
mm





Specimen
SAN099
1676
CEM099
472

0


0


0
260

0.00
0.0
200


E56
SAN099
1645
CEM099
472
A
142






223
SP B

2.0
217


E57
SAN099
1695
CEM099
472
A
92






223
SP B

2.0
193


E58
SAN099
1745
CEM099
472
A
42






223
SP B

3.0
205


E59
SAN099
1787
CEM099
472
A
0






223
SP B

3.0
187


E60
SAN099
1595
CEM099
472
A
192






223
SP B

1.5
175


E61
SAN099
1545
CEM099
472
A
242






223
SP B

1.8
200


E62
SAN099
1645
CEM099
472
F
142






223
SP B

2.0
187


E63
SAN099
1695
CEM099
472
F
92






223
SP B

2.0
207


E64
SAN099
1745
CEM099
472
F
42






223
SP B

2.0
193


E65
SAN099
1787
CEM099
472
F
0






223
SP B

2.0
180


E66
SAN099
1595
CEM099
472
F
192






223
SP B

2.0
175


E67
SAN099
1545
CEM099
472
F
242






223
SP B

2.0
207


E68
SAN099
1645
CEM099
472
A
142






223
SP B

3.0
225


E69
SAN099
1645
CEM099
472
A
142






223
SP B

4.0
245


E70
SAN099
1400
CEM099
472
F
387






223
SP B

2.0
387


E71
SAN099
1500
CEM099
472
F
287






223
SP B

2.0
307


E72
SAN099
1600
CEM099
472
F
187






223
SP B

2.0
273


E73
SAN099
1700
CEM099
472
F
87






223
SP B

2.0
187


E74
SAN099
1300
CEM099
472
F
487






223
SP B

2.0
135


E75
SAN099
1500
CEM099
472
F
287






223
SP B

2.0


E76
SAN099
1400
CEM099
472
A
387






223
SP B

4.0
370


E77
SAN099
1500
CEM099
472
A
287






223
SP B

4.0
368


E78
SAN099
1600
CEM099
472
A
187






223
SP B

4.0
265


E79
SAN099
1700
CEM099
472
A
87






223
SP B

4.0
215


E80
SAN099
1300
CEM099
472
A
487






223
SP B

4.0
100




















air
water
den-








mass
mass
sity
Rc28d
%
Rc90d




g
g
kg/m3
Mpa
rc28d
Mpa
Observation







Specimen
1757
993
2.30
44.8


water releasing










(*resuant*)











Rc24h
Rc28j







E56
1825
1053
2.36
22.3
55.2

water releasing



E57
1843
1065
2.37
20.1
50.8

water releasing



E58
1837
1063
2.37
21.3
46.2

water releasing










and hollow



E59
1826
1051
2.36
19.0
43.5

water releasing










and hollow



E60
1724
968
2.28
20.2
48.8

water releasing










and segregating



E61
1743
984
2.30
22.4
51.8

water releasing










and segregating



E62
1750
986
2.29
20.3
rc7



E63
1822
1049
2.36
21.4
rc7



E64
1845
1065
2.37
19.4
rc7



E65
1823
1050
2.36
19.0
rc7



E66
1779
1005
2.30
22.9
rc7



E67
1744
988
2.31
20.4
rc7










Vfunnel






(s)







E68






heavy, sticky



E69






heavy, compact,










almost segregation



E70


11



full, flexible,










outgassing



E71






heavy and sticky



E72


36



heavy and compact



E73






heavy,










almost homogeneous,










water releasing



E74


100



E75



E76






heavy, outgassing










and segregation



E77






heavy, outgassing










and segregation



E78


36



slow,










water releasing










and segregation



E79






heavy, slow










and water releasing



E80






dry and homogenous










In the tables D, E, F:


A is a coarse CaCO3 filler Betocarb SL as described above


B is a treating ultrafine carbonate filler EV described above


C is a treating ultrafine filler Silica Fume


D is a treating ultrafine filler metakaolin


E is a treating siliceous filler


F is a coarse CaCO3 filler Betocarb HP-OG (d50 about 6 μm, Blaine 380 m2/kg)


SP B is the treating superplastifier as described above.


The cement brand is the standardized cement 42,5 R Gaurain (GEM)


The sand is Standardized sand Under EN 196-1 (SAN)


The column <<consistency>> provides the cone diameter.


This examples provides numerous possible combinations and data and will therefore allow the skilled man to reach the best compromises between Rc and cone diameter.

Claims
  • 1. A product comprising a blend of a calcium carbonate—comprising filler and at least one aluminosiliceous material, wherein the blend is optionally treated with at least one treating agent comprising at least one superplastifier.
  • 2. The product according to claim 1, wherein the calcium carbonate—comprising filler is ground natural calcium carbonate, precipitated calcium carbonate, modified calcium carbonate, or any mixture thereof.
  • 3. The product according to claim 1, wherein the aluminosiliceous material is present in an amount of from 8.5 to 85% per dry weight based on the dry weight of the calcium carbonate-comprising filler.
  • 4. The product according to claim 1, wherein the aluminosiliceous material is present in an amount of from 8.5 to 40% per dry weight based on the dry weight of the calcium carbonate-comprising filler.
  • 5. The product according to claim 1, wherein the aluminosiliceous material is present in an amount of from 30 to 40% per dry weight based on the dry weight of the calcium carbonate-comprising filler.
  • 6. The product according to claim 1, wherein the aluminosiliceous material is present in an amount of from 25 to 75% per dry weight based on the weight of the blend of the calcium carbonate—comprising filler and the aluminosiliceous material.
  • 7. The product according to claim 1, wherein the aluminosiliceous material comprises an aluminum oxide, a silica fume, calcined kaolin, metakaolin, a pozzolanic product, a blast furnace slag, an ultrafine siliceous product, and a blend of Al2O3 and SiO2.
  • 8. The product according to claim 1, wherein the aluminosiliceous material comprises a blend of Al2O3 and SiO2.
  • 9. The product according to claim 1, wherein the blend is treated with at least one treating agent comprising at least one superplastifier. 70
  • 10. The product according to according to 9, wherein superplastifier is a polycarboxylate, a polycarboxylate ether, or a product manufactured from sulfonated naphthalene condensate or sulfonated melamine formaldehyde.
  • 11. The product according to claim 9, wherein the superplastifier is a polycarboxylate ether.
  • 12. A cement composition comprising the product according to claim 9.
  • 13. The cement composition according to claim 12, wherein the superplastifier is present in an amount of from 0.03 to 3% per dry weight based on the dry weight of the cement composition.
  • 14. The cement composition according to claim 12, wherein the superplastifier is present in an amount of from 0.3 to 3 kg for 100 kg of the cement composition, on a dry to dry basis.
  • 15. The cement composition according to claim 12, wherein the at least one treating agent comprises a superplastifier only, or a superplastifier and a plasticizer.
  • 16. The cement composition according to claim 12, wherein the at least one treating agent comprises a superplastifier and a plasticizer in a ratio of from 95/5 to 85/15 on a dry weight basis.
  • 17. The cement composition according to claim 12, further comprising one or more of a fluidifier, a setting accelerator, a setting retarder and an air entrainment agent.
  • 18. The cement composition according to claim 12, wherein the calcium carbonate-comprising filler is dry calcium carbonate, the at least one treating agent is a superplastifier, and the cement composition further comprises one or more additives, and optionally water and aggregates selected from the group consisting of sand and gravel.
  • 19. A cement product made from the cement composition of claim 12.
Priority Claims (1)
Number Date Country Kind
12 001 307.3 Feb 2012 EP regional
Provisional Applications (1)
Number Date Country
61620485 Apr 2012 US
Divisions (1)
Number Date Country
Parent 14373401 Jul 2014 US
Child 14941944 US