WO2007080286A2 - Coated iron sulphate particles and their use in the preparation of cements - Google Patents

Coated iron sulphate particles and their use in the preparation of cements Download PDF

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Publication number
WO2007080286A2
WO2007080286A2 PCT/FR2006/002759 FR2006002759W WO2007080286A2 WO 2007080286 A2 WO2007080286 A2 WO 2007080286A2 FR 2006002759 W FR2006002759 W FR 2006002759W WO 2007080286 A2 WO2007080286 A2 WO 2007080286A2
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WIPO (PCT)
Prior art keywords
cement
coated particles
sulfate
iron
alginic acid
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PCT/FR2006/002759
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French (fr)
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WO2007080286A3 (en
Inventor
Vincent Morin
Hélène DEBEGNAC
Marc Biosa
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Lafarge
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Publication of WO2007080286A2 publication Critical patent/WO2007080286A2/en
Publication of WO2007080286A3 publication Critical patent/WO2007080286A3/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B28/00Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
    • C04B28/02Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B20/00Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
    • C04B20/10Coating or impregnating
    • C04B20/1018Coating or impregnating with organic materials
    • C04B20/1029Macromolecular compounds
    • C04B20/1048Polysaccharides, e.g. cellulose, or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/22Compounds of iron
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/10Compositions or ingredients thereof characterised by the absence or the very low content of a specific material
    • C04B2111/1075Chromium-free or very low chromium-content materials
    • C04B2111/1081Chromium VI, e.g. for avoiding chromium eczema

Definitions

  • the present invention relates to coated particles of iron sulfate and / or manganese sulfate and / or tin sulfate, in particular coated with sodium alginate, suitable for the preparation of cements, in particular reduced-content cements. in chromium (VI). STATE OF THE ART
  • a common method of obtaining a reduced chromium (VI) cement is to add ferrous sulphate (FeSO 4 ) to the cement, since Fe 2+ ions can reduce Cr 6+ ions.
  • FeSO 4 ferrous sulphate
  • Iron sulphate is usually added at the mill inlet in the case of open-circuit mills, or as a separator inlet in the case of closed-circuit mills, or directly to the finished product.
  • EP-A-1100758 discloses a process for the preparation of inorganic binders to which complexes are added organometallic compounds having reducing properties, making it possible to obtain inorganic binders with low or no content of chromium (VI). More specifically, the organometallic complexes of the document are formed with a polyhydroxycarboxylic or carboxylic acid having a backbone of 2 to 8 carbon atoms surrounding a central ion (Mn 2+ or Fe 2+ ). In particular, iron gluconate is provided. It is stated that these organometallic complexes make it possible to use an almost stoichiometric amount of iron relative to chromium, the stability of these complexes being indicated as excellent.
  • coated particles comprising (a) a core comprising iron sulfate and / or tin sulfate and / or manganese sulfate; and (b) an envelope comprising a natural or synthetic polysaccharide.
  • iron sulfate which is the preferred chemical compound of the core of the coated particles according to the invention.
  • the iron sulphate may be replaced in an equivalent manner by manganese sulphate or sulphate of tin or a mixture of iron sulphate, tin sulphate and manganese sulphate, since these three chemical compounds are likely to reduce chromium (VI) and have a relative natural instability.
  • said polysaccharide is alginic acid or one of its derivatives, in particular sodium alginate, potassium alginate, calcium alginate, magnesium alginate, ammonium alginate or propylene glycol alginate.
  • Sodium alginate is particularly preferred.
  • the iron sulfate is monohydrate, heptahydrate or as a mixture of iron sulfate monohydrate and heptahydrate.
  • the coated particles as defined above have a size d max of less than about 200 ⁇ m, preferably less than about 100 ⁇ m.
  • the amount of polysaccharide of the envelope represents, relative to the weight of the core, an amount of between 0.05 and 5%, preferably between 0.2 and 2%.
  • the coated particles according to the invention are stable to storage in a cement for a period of between 3 and 9 months.
  • the coated particles are in powder form, thus in dry form.
  • the invention also provides the use of polysaccharides for stabilizing iron sulfate.
  • the invention further provides a cement comprising coated particles as defined above.
  • the cement according to the invention is obtained from a cement free of coated particles, and contains a quantity of coated particles such that the amount by weight of iron sulphate is less than 0.02% , in particular less than 0.01%, and preferably less than 0.005% per ppm of soluble chromium (VI) present in said cement free of coated particles.
  • the cement according to the invention contains a quantity by weight of iron sulphate of less than 0.3%, in particular less than 0.2%, and of preferably less than 0.1%, and having a chromium (VI) content of less than 2 ppm.
  • chromium (VI) content is expressed in relation to the dry weight of the cement, and is measured on cement juice as described in the draft standard PR NF EN 196-10 May 2005 "Test methods for cements - Part 10: Determination of the water - soluble chromium (VI) content of the cement.
  • the invention also provides the use of coated particles according to the invention or a cement according to the invention in the preparation of a concrete or a mortar.
  • the invention furthermore provides a process for preparing coated particles according to the invention comprising the following steps: - mixing of an iron sulphate powder with a polysaccharide solution, in a mixture of iron sulphate and polysaccharide; drying the mixture obtained in the preceding step in said coated particles.
  • acid is added to the iron sulfate powder and the polysaccharide solution before the end of the mixing step.
  • said method comprises an additional step of final grinding and sieving, after the step of drying the mixture.
  • the mass concentration of polysaccharide in the polysaccharide solution is between about 0.01 and about 10%, in particular between about 0.1 and about 5%, and wherein The mass ratio between the polysaccharide solution and the iron sulfate at the kneading step is from about 5% to about 50%, particularly from about 10% to about 35%.
  • the temperature during the kneading step is the ambient temperature.
  • the drying step is carried out at a temperature of between room temperature and about 70 ° C, in particular at a temperature between room temperature and about 40 0 C, for a period of between about 2 hours and about 5 days, at atmospheric pressure or under reduced pressure.
  • the present invention makes it possible to overcome the drawbacks of the state of the art, and more particularly to reduce significantly, compared with prior art techniques, the amount of iron sulphate which must be incorporated into a cement in order to to reduce the soluble chromium (VI) contained in this cement, by incorporating only a moderate amount of an additive in the cement, while obtaining satisfactory results. Reducing the amount of iron used allows undeniable economic gains.
  • the object of the invention is achieved by producing coated iron sulfate particles for incorporation into the cement, having the following characteristics: the iron sulfate is protected from the external environment by the coating and therefore remains essentially stable in the conditions of storage of the cement; the Fe 2+ ions are capable of being rapidly released (in particular in less than 10 minutes and preferably in less than 5 minutes) during the mixing of the concrete or the mortar, which then allows the reduction of the Cr 6+ ions; the cost of the coated particles bound to the raw materials and to the manufacture is low, which makes the solution proposed by the invention economically advantageous vis-à-vis the prior art.
  • the invention thus provides a solution for stabilizing iron sulfate, without complex formation of iron sulfate, unlike the state of the art.
  • the invention would likewise apply to tin, manganese or other metal sulphate and generally to sulphates and similar salts.
  • the invention therefore relates to coated particles, comprising a core and an envelope, in which the core comprises iron sulfate and the shell comprises a natural or synthetic polysaccharide.
  • the core comprises iron sulfate
  • the shell comprises a natural or synthetic polysaccharide.
  • the core consists of iron sulfate.
  • the envelope consists of a polysaccharide. Other layers and / or components could possibly be present.
  • core of the coated particles is also meant the center or the inner layer of said particles.
  • envelope of the coated particles is also understood to mean the coating, the outer layer, the protective film or the shell of said coated particles.
  • natural or synthetic polysaccharide is meant a polymeric organic molecule consisting of a chain of monosaccharide units.
  • the viscosity of these polymers in solution at 1% by weight in water is variable, for example between 10 and 1000 cps.
  • Satialgine S60 34 cps; Algogel 3001: 59 cps; Satialgine S550: 300 cps; Algogel 3541: 440 cps;
  • said natural or synthetic polysaccharide is capable of establishing, at multiple locations along the polymer chain, particularly ionic-type bonds with divalent cations, such as, for example, Fe 2+ ions,
  • polysaccharides examples include pectins and alginates.
  • the polysaccharide is alginic acid, in particular in the form of sodium alginate.
  • Sodium alginate is the sodium salt of alginic acid, which is extracted from brown algae (Phaeophyceae). It is also the most common form of marketing of alginic acid.
  • Alginic acid is a natural polymer of formula
  • n consists of two mono-saccharide units: D-mannuronic acid (M) and L-guluronic acid (G).
  • M D-mannuronic acid
  • G L-guluronic acid
  • the typical number of base units is about 200.
  • the proportion of mannuronic acid and guluronic acid varies from one species of seaweed to another and influences, for example, the chemical properties, by varying the gelling power. or thickener of alginate.
  • the ratio of the number of units M to the number of units G is between 0.5 and 1.5, and more particularly between 1 and 1.5.
  • the sodium alginate in solution forms, in the presence of divalent ions, a complex in gel form, also known as an "egg-box" assembly, in which said ions are sequestered.
  • the alginic acid would establish bonds with the surface of the iron sulphate core, without establishing bonds with the Fe 2+ ions located inside the iron sulphate core.
  • the alginate shell effectively protects the iron sulphate core from the environment under storage conditions, and is quickly and easily broken to liberate and render accessible the iron sulphate core under conditions of use.
  • the alginate is degraded in a basic medium.
  • the cement produces a basic medium during its mixing, which causes the rupture of the envelope and / or the release of iron sulfate.
  • the use of sodium alginate also has the additional advantage that this product is common and inexpensive.
  • the iron sulphate forming the core may be in its conventional forms, especially in monohydrate form, that is to say of formula (FeSO 4 , 1H 2 O), or in heptahydrate form, that is to say of formula (FeSO 4 , 7H 2 O).
  • the heptahydrate form is the more commonly used in the field of cement, especially in the form of powder.
  • the coated particles generally have a particle size d ma le (sieve pass) less than about 200 microns, preferably less than about 100 microns.
  • the amount of alginate in the coated particles is such that a protective film is created on the surface of the iron sulfate particles.
  • the amount of polysaccharide of the shell is, based on the weight of the iron sulfate of the core, an amount between 0.05 and 5%, preferably between 0.2 and 2%.
  • Polysaccharides are therefore useful for stabilizing iron sulfate.
  • the coated iron sulphate is therefore substantially stable for a storage period of between 3 and 9 months, under the usual conditions for storing the cement, in particular in a silo or paper bag.
  • substantially stable it is meant that sufficient Fe 2+ ions remain to reduce the amount of chromium (VI) to less than 2 ppm.
  • a proportion greater than 50%, in particular greater than 70%, in particular greater than 90%, of iron sulphate is still available at the time of maturity, that is to say has not undergone any oxidation of the ferrous ions.
  • the particles of the invention are useful as additives for cements.
  • cement By way of cement, it is possible to use any type of cement, in particular Portland, or composite cements, or any cement defined in the EN 197 standard.
  • the particles according to the invention can be added at any time during the manufacture of the cement. Particles can be added at the mill inlet in the case of open-circuit mills, or at the separator inlet in the case of closed circuit mills, or directly to the finished product. This latter solution is preferred in that it limits attrition actions on the surface of the particles. Particles can also be added in silos or in transport tanks, or in concrete or the final mortar.
  • the amount of particles is relatively small, compared to the amount of iron sulfate that was previously required to compensate for the loss of efficiency of iron sulfate over time.
  • the particles according to the invention have no noticeable effect on the conditions of use of the cement, which is therefore used quite conventionally.
  • the invention also provides a method of manufacturing the particles according to the invention, which comprises the following steps: - mixing of an iron sulfate powder with a polysaccharide solution, in a mixture of iron sulfate and polysaccharide; drying the mixture obtained in the preceding step in the coated particles.
  • the method according to the invention may comprise an additional step of pre-grinding and sieving prior to the kneading step, so as to obtain iron sulphate powder from a stock of crude iron sulphate.
  • the starting iron sulfate powder may optionally be calibrated to obtain the desired final diameter. Since the amount of alginate is relatively small, the starting diameter is only slightly less than that of arrival.
  • tapping is understood to mean any technique leading to the formation of a protective film around the iron sulphate, especially the simple mixing, coating or encapsulation, whatever the material used, in particular a mixer or a bed of iron. fluidized air (with spraying of the polysaccharide solution on a suspension of iron sulfate particles).
  • acid in particular hydrochloric acid
  • acid is added. to the iron sulfate powder and the polysaccharide solution before the end of the mixing step.
  • the acid in particular hydrochloric acid
  • the acid makes it possible to deflate the chains of the polysaccharide by themselves, which has the effect of forming a denser protective film on the surface of the iron sulphate.
  • the acid is added until an acidic pH is obtained, preferably less than 4.0 and in particular less than 2.0.
  • the preparation process according to the invention may optionally comprise an additional step of final grinding and sieving, after the step of drying the mixture, making it possible to obtain, from the coated particles, grinded and sieved coated particles.
  • the mass concentration of polysaccharide in the polysaccharide solution is between about 0.01 and about 10%, in particular between about 0.1 and about 5%, and the mass ratio between the polysaccharide solution and the iron sulfate at the kneading step is between about
  • alginate When alginate is fixed on the iron sulphate core, water molecules previously fixed by these alginate molecules are re-dropped. In general, the amounts of water and alginate are adapted to the specific surface area of the ferrous sulphate powder and to the quality of this powder.
  • the kneading step is carried out for a sufficient duration, which can be between 2 and 30 minutes. Short periods are preferred.
  • the temperature is generally room temperature, but may be higher if needed, or may be increased at the end of mixing.
  • the drying step is carried out at a temperature of between room temperature and approximately 70 ° C., in particular between room temperature and 40 ° C. for a time sufficient to remove the free water from the alginate.
  • the drying can be carried out under reduced pressure (which significantly reduces the duration of drying).
  • the end of the drying can be determined by visual inspection (the particles go from green to creamy white) or by loss of mass tracking (until the mass of the particles does not vary much more).
  • Example 1 Synthesis of coated particles.
  • Coated particles according to the invention are prepared according to the following protocol: a) A solution of sodium alginate (supplier: VWR International / Prolabo, catalog number 27 660.183, viscosity equivalent to that of Satialgine S550 marketed by Degussa, cf. above) is prepared by slow dissolution hot (50 0 C) of sodium alginate powder (1.2 g) in demineralized water (60 g). b) 250 g of iron sulphate heptahydrate (supplier: VWR International / Prolabo, catalog number 24 237.363) is crushed and sieved so that its particle size is less than 100 ⁇ m (the largest particle having a size of 100 ⁇ m ).
  • Chromium (VI) soluble Chromium (VI) soluble.
  • powdered iron sulphate or coated particles according to the invention are added thereto.
  • the iron sulphate, coated or not, which is used in addition with the cement has a particle size smaller than
  • iron sulphate coated or uncoated
  • the iron sulphate is mixed and homogenized with cement for 45 minutes with Turbula ® before the aging of the product.
  • This test consists in putting in a tank a bed of cement powder containing iron sulphate: the mass of cement is approximately 600 grams and the height of the bed of material 1 cm. This tray is then placed in a chamber maintained at 20 0 C and
  • This test is intended to simulate the storage conditions of the silo cement.
  • the cement arrives relatively warm in the silo at the factory and remains confined.
  • 1.5 kg of cement is introduced into a can of dimensions 108 mm ⁇ 136 mm (volume 1 L) which is then closed and placed in an oven regulated at 80 ° C.
  • the chromium content is measured ( VI) soluble at 7 and 28 days.
  • control refers to a reference state of the cement (with or without iron sulfate or coated particles) which has not been aged. Measurements of chrome "light” (VI) soluble are therefore obtained on a cement unaged control or non-aged cement mixed with any iron sulfate immediately after mixing and homogenisation in the Turbula ®.
  • Ferrous sulphate or ferrous gluconate is incorporated in a cement initially containing 13 ppm soluble chromium VI, for the same amount of Fe 2+ introduced (0.77 mM) in both cases.
  • the final amount of chromium VI in the cement is measured according to the standard method described above. The results are shown in Table 3 below. It is found that, with equivalent amounts of ferrous iron introduced, ferrous gluconate is less effective than ferrous sulfate in reducing chromium VI. Table 3
  • Example 4 Minimum amount of coated particles according to the invention for a total reduction of chromium VI.
  • the remaining concentration of Chrome VI in a cement initially containing 15 ppm of Chrome VI, after addition of the coated particles according to the invention, at different concentrations, is measured according to the standard procedure described in Example 2.
  • the results are reported in Table 4 below, in which the concentration of coated particles is represented by the concentration of FeSO 4 introduced.
  • the first line of the table represents the control (cement without coated particles).
  • Example 5 Impact on the properties of use of cement. Tests have been carried out to evaluate the impact of the addition of alginate (sodium alginate Prolabo) to a cement on the properties of use of said cement. 0.1% alginate is incorporated in a cement as defined in Example 1, that is, that is, about 100 times more than the amount of alginate recommended for incorporation of coated particles according to the invention.
  • alginate sodium alginate Prolabo
  • Curing time parameters determination of consistency and setting according to EN 19G-3 (Table 5) and mechanical strength parameters, namely flexural strength (Rf) and compression (Rc) (Table 6). The tests are carried out on standard mortar.
  • alginate even when present at such a high concentration, has no impact on the properties of the cement, which implies, a fortiori, that a much smaller quantity will not have impact.
  • the use of the coated particles according to the invention will therefore have no impact on the properties of use of the cement.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
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  • Curing Cements, Concrete, And Artificial Stone (AREA)
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Abstract

The invention relates to a cement comprising coated particles, the said coated particles comprising: (a) a core comprising iron sulphate and/or tin sulphate and/or manganese sulphate; and (b) a shell comprising alginic acid or a derivative thereof.

Description

PARTICULES DE SULFATE DE FER ENROBEES ET LEUR UTILISATION DANS LA PREPARATION DE CIMENTS FERTILIZED IRON SULFATE PARTICLES AND THEIR USE IN THE PREPARATION OF CEMENT
DOMAINE TECHNIQUE La présente invention concerne des particules de sulfate de fer et / ou de sulfate de manganèse et / ou de sulfate d'étain enrobées, notamment enrobées d'alginate de sodium, adaptées à la préparation de ciments, notamment de ciments à teneur réduite en chrome (VI) . ETAT DE LA TECHNIQUETECHNICAL FIELD The present invention relates to coated particles of iron sulfate and / or manganese sulfate and / or tin sulfate, in particular coated with sodium alginate, suitable for the preparation of cements, in particular reduced-content cements. in chromium (VI). STATE OF THE ART
II est bien connu dans le domaine de la cimenterie que la teneur en chrome (VI) soluble doit être aussi réduite que possible. Ainsi, les réglementations courantes (Directive européenne 2003/53/CE) exigent que la concentration du chrome (VI) soluble dans les ciments soit inférieure à 2 ppm.It is well known in the cement industry that the soluble chromium (VI) content should be as small as possible. Thus, current regulations (European Directive 2003/53 / EC) require that the concentration of chromium (VI) soluble in cement be less than 2 ppm.
Une méthode courante d'obtention d'un ciment à teneur réduite en chrome (VI) consiste à ajouter au ciment du sulfate ferreux (FeSO4) , dans la mesure où les ions Fe2+ permettent de réduire les ions Cr6+. Le sulfate de fer est habituellement ajouté en entrée de broyeur dans le cas des broyeurs à circuit ouvert, ou en entrée de séparateur dans le cas des broyeurs à circuit fermé, ou encore directement au produit fini.A common method of obtaining a reduced chromium (VI) cement is to add ferrous sulphate (FeSO 4 ) to the cement, since Fe 2+ ions can reduce Cr 6+ ions. Iron sulphate is usually added at the mill inlet in the case of open-circuit mills, or as a separator inlet in the case of closed-circuit mills, or directly to the finished product.
Toutefois, un problème rencontré avec cette méthode est l'instabilité du sulfate ferreux dans les conditions de stockage du ciment. Au cours du temps, les ions ferreux Fe2+ se transforment en effet en ions ferriques Fe3+ qui sont inefficaces pour la réduction du chrome (VI) . Par conséquent, la quantité de sulfate de fer qui doit être généralement incorporée dans le ciment est typiquement supérieure d'un facteur 30 à la quantité de sulfate de fer théoriquement nécessaire pour réduire le chrome (VI) soluble.However, a problem with this method is the instability of ferrous sulphate in the storage conditions of the cement. Over time, ferrous Fe 2+ ions are converted into Fe 3+ ferric ions which are ineffective for the reduction of chromium (VI). Therefore, the amount of iron sulfate that is generally to be incorporated into the cement is typically greater by a factor of 30 than the amount of iron sulfate theoretically required to reduce soluble chromium (VI).
Le document EP-A-1100758 décrit un procédé de préparation de liants inorganiques auxquels sont ajoutés des complexes organométalliques ayant des propriétés réductrices, permettant d'obtenir des liants inorganiques à teneur faible ou nulle en chrome (VI) . Plus précisément, les complexes organométalliques du document sont formés avec un acide polyhydroxycarboxylique ou carboxylique ayant un squelette de 2 à 8 atomes de carbone entourant un ion central (Mn2+ ou Fe2+) . Est notamment prévu le gluconate de fer. Il est indiqué que ces complexes organométalliques permettent d'utiliser une quantité presque stoechiométrique de fer par rapport au chrome, la stabilité de ces complexes étant indiquée comme excellente.EP-A-1100758 discloses a process for the preparation of inorganic binders to which complexes are added organometallic compounds having reducing properties, making it possible to obtain inorganic binders with low or no content of chromium (VI). More specifically, the organometallic complexes of the document are formed with a polyhydroxycarboxylic or carboxylic acid having a backbone of 2 to 8 carbon atoms surrounding a central ion (Mn 2+ or Fe 2+ ). In particular, iron gluconate is provided. It is stated that these organometallic complexes make it possible to use an almost stoichiometric amount of iron relative to chromium, the stability of these complexes being indicated as excellent.
Cependant, dans ce document, les ions ferreux étant séquestrés de manière individuelle, il est nécessaire d'utiliser une grande quantité de molécules organiques pour espérer les protéger d'une oxydation en ions ferriques . En outre, le document ne fournit pas de données quantitatives permettant d'évaluer la performance de cette méthode en terme de stabilité des ions ferreux complexés et de leur capacité à réduire le chrome (VI) . La question de l'accessibilité de ces ions au moment où ils sont censés réduire le chrome (VI) reste donc posée. D'ailleurs, dans les faits, le gluconate de fer n'est pas plus stable que le sulfate de fer.However, in this document, the ferrous ions being sequestered individually, it is necessary to use a large amount of organic molecules to hope to protect them from oxidation to ferric ions. In addition, the document does not provide quantitative data to evaluate the performance of this method in terms of stability of complexed ferrous ions and their ability to reduce chromium (VI). The question of the accessibility of these ions when they are supposed to reduce the chromium (VI) remains thus posed. Moreover, in fact, iron gluconate is not more stable than iron sulphate.
Il existe donc toujours un besoin d'un procédé permettant de stabiliser le sulfate de fer et de diminuer la quantité de sulfate de fer devant être incorporée dans un ciment (par exemple afin de réduire le chrome (VI) soluble contenu dans ce ciment) .There is therefore still a need for a method for stabilizing iron sulfate and decreasing the amount of iron sulfate to be incorporated into a cement (for example to reduce the soluble chromium (VI) contained in this cement).
RESUME DE L'INVENTIONSUMMARY OF THE INVENTION
L'invention fournit donc des particules enrobées, comprenant (a) un cœur comprenant du sulfate de fer et / ou du sulfate d'étain et / ou du sulfate de manganèse; et (b) une enveloppe comprenant un polysaccharide naturel ou synthétique .The invention thus provides coated particles, comprising (a) a core comprising iron sulfate and / or tin sulfate and / or manganese sulfate; and (b) an envelope comprising a natural or synthetic polysaccharide.
A des fins de simplification, toute la suite de la description est établie en relation avec le sulfate de fer, qui est le composé chimique préféré du cœur des particules enrobées selon l'invention. Toutefois, il reste entendu que, dans tout ce qui suit, le sulfate de fer peut être remplacé de manière équivalente par du sulfate de manganèse ou du sulfate d'étain ou par un mélange de sulfate de fer, de sulfate d'étain et de sulfate de manganèse, étant donné que ces trois composés chimiques sont susceptibles de réduire le chrome (VI) et présentent une relative instabilité naturelle. De préférence, ledit polysaccharide est l'acide alginique ou l'un de ses dérivés, en particulier l'alginate de sodium, l'alginate de potassium, l'alginate de calcium, l'alginate de magnésium, l'alginate d'ammonium ou le propylène glycol alginate. L'alginate de sodium est particulièrement préféré. De préférence, le sulfate de fer est monohydraté, heptahydraté ou sous forme d'un mélange de sulfate de fer monohydraté et heptahydraté .For the sake of simplification, all the rest of the description is established in relation to iron sulfate, which is the preferred chemical compound of the core of the coated particles according to the invention. However, it is understood that, in what follows, the iron sulphate may be replaced in an equivalent manner by manganese sulphate or sulphate of tin or a mixture of iron sulphate, tin sulphate and manganese sulphate, since these three chemical compounds are likely to reduce chromium (VI) and have a relative natural instability. Preferably, said polysaccharide is alginic acid or one of its derivatives, in particular sodium alginate, potassium alginate, calcium alginate, magnesium alginate, ammonium alginate or propylene glycol alginate. Sodium alginate is particularly preferred. Preferably, the iron sulfate is monohydrate, heptahydrate or as a mixture of iron sulfate monohydrate and heptahydrate.
Avantageusement, les particules enrobées telles que définies ci-dessus ont une taille dmax inférieure à environ 200 μm, de préférence inférieure à environ 100 μm.Advantageously, the coated particles as defined above have a size d max of less than about 200 μm, preferably less than about 100 μm.
Avantageusement, la quantité de polysaccharide de l'enveloppe représente, par rapport au poids du cœur, une quantité comprise entre 0,05 et 5 %, de préférence entre 0,2 et 2 %.Advantageously, the amount of polysaccharide of the envelope represents, relative to the weight of the core, an amount of between 0.05 and 5%, preferably between 0.2 and 2%.
De préférence, les particules enrobées selon l'invention sont stables au stockage dans un ciment pendant une durée comprise entre 3 et 9 mois.Preferably, the coated particles according to the invention are stable to storage in a cement for a period of between 3 and 9 months.
De manière avantageuse, les particules enrobées sont sous forme de poudre, donc sous forme sèche.Advantageously, the coated particles are in powder form, thus in dry form.
L'invention prévoit également l'utilisation de polysaccharides pour stabiliser du sulfate de fer.The invention also provides the use of polysaccharides for stabilizing iron sulfate.
L'invention fournit par ailleurs un ciment comprenant des particules enrobées telles que définies ci-dessus.The invention further provides a cement comprising coated particles as defined above.
Selon un mode de réalisation avantageux, le ciment selon l'invention est obtenu à partir d'un ciment dépourvu de particules enrobées, et contient une quantité de particules enrobées telle que la quantité en poids de sulfate de fer est inférieure à 0,02 %, en particulier inférieure à 0,01 %, et de préférence inférieure à 0,005 % par ppm de chrome (VI) soluble présent dans ledit ciment dépourvu de particules enrobées. Selon un mode de réalisation avantageux, le ciment selon l'invention contient une quantité en poids de sulfate de fer inférieure à 0,3 %, en particulier inférieure à 0,2 %, et de préférence inférieure à 0,1 %, et ayant une teneur en chrome (VI) inférieure à 2 ppm.According to an advantageous embodiment, the cement according to the invention is obtained from a cement free of coated particles, and contains a quantity of coated particles such that the amount by weight of iron sulphate is less than 0.02% , in particular less than 0.01%, and preferably less than 0.005% per ppm of soluble chromium (VI) present in said cement free of coated particles. According to an advantageous embodiment, the cement according to the invention contains a quantity by weight of iron sulphate of less than 0.3%, in particular less than 0.2%, and of preferably less than 0.1%, and having a chromium (VI) content of less than 2 ppm.
Ladite teneur en chrome (VI) est exprimée par rapport au poids sec du ciment, et est mesurée sur du jus de ciment comme cela est décrit dans le projet de norme PR NF EN 196- 10 Mai 2005 « Méthodes d'essais des ciments - Partie 10: détermination de la teneur du ciment en chrome (VI) soluble dans l ' eau » .Said chromium (VI) content is expressed in relation to the dry weight of the cement, and is measured on cement juice as described in the draft standard PR NF EN 196-10 May 2005 "Test methods for cements - Part 10: Determination of the water - soluble chromium (VI) content of the cement.
L'invention prévoit également l'utilisation de particules enrobées selon l'invention ou d'un ciment selon l'invention dans la préparation d'un béton ou d'un mortier.The invention also provides the use of coated particles according to the invention or a cement according to the invention in the preparation of a concrete or a mortar.
L'invention fournit par ailleurs un procédé de préparation de particules enrobées selon 1 ' invention comprenant les étapes suivantes : - malaxage d'une poudre de sulfate de fer avec une solution de polysaccharide, en un mélange de sulfate de fer et de polysaccharide; séchage du mélange obtenu à l ' étape précédente en lesdites particules enrobées. De manière avantageuse, on ajoute de l'acide à la poudre de sulfate de fer et à la solution de polysaccharide avant la fin de l'étape de malaxage.The invention furthermore provides a process for preparing coated particles according to the invention comprising the following steps: - mixing of an iron sulphate powder with a polysaccharide solution, in a mixture of iron sulphate and polysaccharide; drying the mixture obtained in the preceding step in said coated particles. Advantageously, acid is added to the iron sulfate powder and the polysaccharide solution before the end of the mixing step.
Selon un mode de réalisation particulier, ledit procédé comprend une étape supplémentaire de broyage final et de tamisage, après l'étape de séchage du mélange.According to a particular embodiment, said method comprises an additional step of final grinding and sieving, after the step of drying the mixture.
De préférence, dans le procédé selon l'invention, la concentration massique de polysaccharide dans la solution de polysaccharide est comprise entre environ 0,01 et environ 10 %, en particulier comprise entre environ 0,1 et environ 5 %, et dans lequel le rapport massique entre la solution de polysaccharide et le sulfate de fer à l'étape de malaxage est compris entre environ 5 % et environ 50 %, en particulier entre environ 10 % et environ 35 %.Preferably, in the process according to the invention, the mass concentration of polysaccharide in the polysaccharide solution is between about 0.01 and about 10%, in particular between about 0.1 and about 5%, and wherein The mass ratio between the polysaccharide solution and the iron sulfate at the kneading step is from about 5% to about 50%, particularly from about 10% to about 35%.
De préférence, dans le procédé selon l'invention, la température lors de l'étape de malaxage est la température ambiante .Preferably, in the process according to the invention, the temperature during the kneading step is the ambient temperature.
De préférence, l'étape de séchage s'effectue à une température comprise entre la température ambiante et environ 700C, en particulier à une température comprise entre la température ambiante et environ 400C, pendant une durée comprise entre environ 2 heures et environ 5 jours, à la pression atmosphérique ou sous pression réduite. La présente invention permet de surmonter les inconvénients de l'état de la technique, et plus particulièrement de diminuer de manière importante, par rapport aux techniques antérieures, la quantité de sulfate de fer qu'il est nécessaire d' incorporer dans un ciment afin de réduire le chrome (VI) soluble contenu dans ce ciment, et ce en incorporant dans le ciment une quantité seulement modérée d'un additif, tout en obtenant des résultats satisfaisants. La réduction de la quantité de fer utilisée permet des gains économiques indéniables . Le but de l'invention est atteint en fabriquant des particules de sulfate de fer enrobées destinées à être incorporées dans le ciment, présentant les caractéristiques suivantes : le sulfate de fer est protégé de l'environnement extérieur par l'enrobage et reste donc essentiellement stable dans les conditions de stockage du ciment; les ions Fe2+ sont susceptibles d'être libérés rapidement (notamment en moins de 10 minutes et préférentiellement en moins de 5 minutes) lors du gâchage du béton ou du mortier, ce qui permet alors la réduction des ions Cr6+; le coût de revient des particules enrobées lié aux matières premières et a la fabrication est faible, ce qui rend la solution proposée par l'invention économiquement avantageuse vis-à-vis de l'art antérieur. L'invention fournit donc une solution de stabilisation du sulfate de fer, sans formation de complexe du sulfate de fer, à la différence de l'état de la technique. L'invention s'appliquerait de même au sulfate d'étain, de manganèse ou d'autres métaux et de façon générale aux sulfates et sels similaires .Preferably, the drying step is carried out at a temperature of between room temperature and about 70 ° C, in particular at a temperature between room temperature and about 40 0 C, for a period of between about 2 hours and about 5 days, at atmospheric pressure or under reduced pressure. The present invention makes it possible to overcome the drawbacks of the state of the art, and more particularly to reduce significantly, compared with prior art techniques, the amount of iron sulphate which must be incorporated into a cement in order to to reduce the soluble chromium (VI) contained in this cement, by incorporating only a moderate amount of an additive in the cement, while obtaining satisfactory results. Reducing the amount of iron used allows undeniable economic gains. The object of the invention is achieved by producing coated iron sulfate particles for incorporation into the cement, having the following characteristics: the iron sulfate is protected from the external environment by the coating and therefore remains essentially stable in the conditions of storage of the cement; the Fe 2+ ions are capable of being rapidly released (in particular in less than 10 minutes and preferably in less than 5 minutes) during the mixing of the concrete or the mortar, which then allows the reduction of the Cr 6+ ions; the cost of the coated particles bound to the raw materials and to the manufacture is low, which makes the solution proposed by the invention economically advantageous vis-à-vis the prior art. The invention thus provides a solution for stabilizing iron sulfate, without complex formation of iron sulfate, unlike the state of the art. The invention would likewise apply to tin, manganese or other metal sulphate and generally to sulphates and similar salts.
EXPOSE DETAILLE DE MODES DE REALISATION DE L'INVENTION Particules enrobées .DETAILED DESCRIPTION OF EMBODIMENTS OF THE INVENTION Coated particles.
L'invention a donc pour objet des particules enrobées, comprenant un cœur et une enveloppe, dans lesquelles le cœur comprend du sulfate de fer et l'enveloppe comprend un polysaccharide naturel ou synthétique. De préférence, le cœur consiste en du sulfate de fer. De préférence, l'enveloppe consiste en un polysaccharide. D'autres couches et/ou composants pourraient éventuellement être présents .The invention therefore relates to coated particles, comprising a core and an envelope, in which the core comprises iron sulfate and the shell comprises a natural or synthetic polysaccharide. Preferably, the core consists of iron sulfate. Preferably, the envelope consists of a polysaccharide. Other layers and / or components could possibly be present.
Par "cœur" des particules enrobées on entend également le centre ou la couche interne desdites particules. ParBy "core" of the coated particles is also meant the center or the inner layer of said particles. By
"enveloppe" des particules enrobées on entend également l'enrobage, la couche externe, le film protecteur ou la coquille desdites particules enrobées ."envelope" of the coated particles is also understood to mean the coating, the outer layer, the protective film or the shell of said coated particles.
Par "polysaccharide naturel ou synthétique" , on entend une molécule organique polymérique constituée d'une chaîne d'unités de monosaccharides . La viscosité de ces polymères en solution à 1 % en poids dans l'eau est variable, par exemple entre 10 et 1000 cps .By "natural or synthetic polysaccharide" is meant a polymeric organic molecule consisting of a chain of monosaccharide units. The viscosity of these polymers in solution at 1% by weight in water is variable, for example between 10 and 1000 cps.
A titre d'exemple, la viscosité de divers alginates commercialisés par Degussa, à 1 % dans l'eau à 200C, est indiquée ci-après :By way of example, the viscosity of various alginates marketed by Degussa at 1% in water at 20 ° C. is indicated below:
Satialgine S60: 34 cps; Algogel 3001: 59 cps; Satialgine S550: 300 cps; - Algogel 3541: 440 cps;Satialgine S60: 34 cps; Algogel 3001: 59 cps; Satialgine S550: 300 cps; Algogel 3541: 440 cps;
Satialgine S1100: 610 cps.Satialgine S1100: 610 cps.
De préférence, ledit polysaccharide naturel ou synthétique est capable d'établir en de multiples emplacements le long de la chaîne polymérique des liaisons notamment de type ionique avec des cations divalents, tels que par exemple les ions Fe2+,Preferably, said natural or synthetic polysaccharide is capable of establishing, at multiple locations along the polymer chain, particularly ionic-type bonds with divalent cations, such as, for example, Fe 2+ ions,
Ca2+ , Mn2+ , Sn2+ .Ca 2+ , Mn 2+ , Sn 2+ .
A titre d'exemple de polysaccharides, on peut citer les pectines et les alginates.Examples of polysaccharides include pectins and alginates.
Dans ce qui suit, on donne une description en relation avec l'alginate, mais tout autre polysaccharide est approprié.In what follows, a description is given in relation to the alginate, but any other polysaccharide is appropriate.
Selon un mode de réalisation préféré des particules enrobées selon l'invention, le polysaccharide est l'acide alginique, en particulier sous forme d'alginate de sodium. L'alginate de sodium est le sel de sodium de l'acide alginique, qui est extrait d'algues brunes (Phaeophyceae) . C'est également la forme la plus usuelle de commercialisation de l'acide alginigue . L'acide alginique est un polymère naturel de formule bruteAccording to a preferred embodiment of the coated particles according to the invention, the polysaccharide is alginic acid, in particular in the form of sodium alginate. Sodium alginate is the sodium salt of alginic acid, which is extracted from brown algae (Phaeophyceae). It is also the most common form of marketing of alginic acid. Alginic acid is a natural polymer of formula
(C6H7NaO6) n constitué de deux unités mono-saccharidiques : l'acide D-mannuronique (M) et l'acide L-guluronique (G) . Le nombre typique d'unités de base est d'environ 200. La proportion en acide mannuronique et en acide guluronique varie d'une espèce d'algue à l'autre et influe par exemple sur les propriétés chimiques, en faisant varier le pouvoir gélifiant ou épaississant de l'alginate. De préférence, dans l'invention, le rapport du nombre d'unités M sur le nombre d'unités G est compris entre 0,5 et 1,5, et plus particulièrement entre 1 et 1,5.(C 6 H 7 NaO 6 ) n consists of two mono-saccharide units: D-mannuronic acid (M) and L-guluronic acid (G). The typical number of base units is about 200. The proportion of mannuronic acid and guluronic acid varies from one species of seaweed to another and influences, for example, the chemical properties, by varying the gelling power. or thickener of alginate. Preferably, in the invention, the ratio of the number of units M to the number of units G is between 0.5 and 1.5, and more particularly between 1 and 1.5.
L'alginate de sodium en solution forme, en présence d'ions divalents, un complexe sous forme de gel, aussi appelé assemblage "en boîte d'œufs", dans lequel lesdits ions sont séquestrés . Dans les particules enrobées selon l'invention, l'acide alginique établirait des liaisons avec la surface du cœur de sulfate de fer, sans établir de liaisons avec les ions Fe2+ situés à l'intérieur du cœur de sulfate de fer. Ainsi, l'enveloppe d'alginate protège efficacement le cœur de sulfate de fer de l'environnement dans des conditions de stockage, et est rapidement et aisément rompue pour libérer et rendre accessible le cœur de sulfate de fer dans des conditions d'utilisation. En effet, l'alginate se dégrade dans un milieu basique. Or, le ciment produit un milieu basique lors de son gâchage, ce qui provoque la rupture de l'enveloppe et/ou la libération du sulfate de fer.The sodium alginate in solution forms, in the presence of divalent ions, a complex in gel form, also known as an "egg-box" assembly, in which said ions are sequestered. In the coated particles according to the invention, the alginic acid would establish bonds with the surface of the iron sulphate core, without establishing bonds with the Fe 2+ ions located inside the iron sulphate core. Thus, the alginate shell effectively protects the iron sulphate core from the environment under storage conditions, and is quickly and easily broken to liberate and render accessible the iron sulphate core under conditions of use. Indeed, the alginate is degraded in a basic medium. However, the cement produces a basic medium during its mixing, which causes the rupture of the envelope and / or the release of iron sulfate.
L'utilisation d'alginate de sodium présente en outre l'avantage supplémentaire que ce produit est courant et peu onéreux. Le sulfate de fer formant le cœur peut être sous ses formes classiques, notamment sous forme monohydratée, c'est-à-dire de formule (FeSO4, 1 H2O), ou sous forme heptahydratée, c'est-à- dire de formule (FeSO4, 7 H2O) . La forme heptahydratée est la plus couramment utilisée dans le domaine de la cimenterie, notamment sous forme de poudre .The use of sodium alginate also has the additional advantage that this product is common and inexpensive. The iron sulphate forming the core may be in its conventional forms, especially in monohydrate form, that is to say of formula (FeSO 4 , 1H 2 O), or in heptahydrate form, that is to say of formula (FeSO 4 , 7H 2 O). The heptahydrate form is the more commonly used in the field of cement, especially in the form of powder.
Les particules enrobées présentent en général une taille de particule dmaχ (le passant au tamis) inférieure à environ 200 μm, de préférence inférieure à environ 100 μm.The coated particles generally have a particle size d ma le (sieve pass) less than about 200 microns, preferably less than about 100 microns.
La quantité d'alginate dans les particules enrobées est telle qu'un film protecteur est créé à la surface des particules de sulfate de fer. Par exemple, la quantité de polysaccharide de l'enveloppe représente, par rapport au poids du sulfate de fer du cœur, une quantité comprise entre 0,05 et 5 %, de préférence entre 0,2 et 2 %.The amount of alginate in the coated particles is such that a protective film is created on the surface of the iron sulfate particles. For example, the amount of polysaccharide of the shell is, based on the weight of the iron sulfate of the core, an amount between 0.05 and 5%, preferably between 0.2 and 2%.
Les polysaccharides sont donc utiles pour stabiliser le sulfate de fer. Le sulfate de fer revêtu est donc sensiblement stable pendant une durée de stockage comprise entre 3 et 9 mois, dans les conditions usuelles de stockage du ciment, notamment en silo ou sac papier.Polysaccharides are therefore useful for stabilizing iron sulfate. The coated iron sulphate is therefore substantially stable for a storage period of between 3 and 9 months, under the usual conditions for storing the cement, in particular in a silo or paper bag.
Par "sensiblement stable", on entend qu'il reste suffisamment d'ions Fe2+ pour réduire la quantité de chrome (VI) à moins de 2 ppm. De préférence, une proportion supérieure à 50 %, en particulier supérieure à 70 %, notamment supérieure à 90 % du sulfate de fer est encore disponible à l'échéance, c'est-à-dire n'a pas subi d'oxydation des ions ferreux.By "substantially stable" it is meant that sufficient Fe 2+ ions remain to reduce the amount of chromium (VI) to less than 2 ppm. Preferably, a proportion greater than 50%, in particular greater than 70%, in particular greater than 90%, of iron sulphate is still available at the time of maturity, that is to say has not undergone any oxidation of the ferrous ions.
Ciment contenant les particules enrobées .Cement containing the coated particles.
Les particules de l'invention sont utiles comme additifs pour les ciments .The particles of the invention are useful as additives for cements.
A titre de ciment, on peut utiliser tout type de ciment, notamment Portland, ou ciments composés, ou tout ciment défini à la norme EN 197.By way of cement, it is possible to use any type of cement, in particular Portland, or composite cements, or any cement defined in the EN 197 standard.
On peut ajouter les particules selon l'invention à tout moment de la fabrication du ciment. Les particules peuvent être ajoutées en entrée de broyeur dans le cas des broyeurs à circuit ouvert, ou en entrée de séparateur dans le cas des broyeurs à circuit fermé, ou encore directement au produit fini. Cette dernière solution est préférée, dans la mesure où elle limite les actions d'attrition sur la surface des particules. Les particules peuvent aussi être ajoutées dans les silos ou dans les citernes de transport, ou encore dans le béton ou le mortier final.The particles according to the invention can be added at any time during the manufacture of the cement. Particles can be added at the mill inlet in the case of open-circuit mills, or at the separator inlet in the case of closed circuit mills, or directly to the finished product. This latter solution is preferred in that it limits attrition actions on the surface of the particles. Particles can also be added in silos or in transport tanks, or in concrete or the final mortar.
La quantité de particules est relativement faible, en comparaison à la quantité de sulfate de fer qu'il était nécessaire d'utiliser auparavant pour compenser la perte d'efficacité dans le temps du sulfate de fer.The amount of particles is relatively small, compared to the amount of iron sulfate that was previously required to compensate for the loss of efficiency of iron sulfate over time.
Les particules selon l'invention n'ont pas d'effet notable sur les conditions d'emploi du ciment, qui est utilisé donc de façon tout à fait classique.The particles according to the invention have no noticeable effect on the conditions of use of the cement, which is therefore used quite conventionally.
Procédé de fabrication des particules enrobées.Process for manufacturing the coated particles
L'invention fournit aussi un procédé de fabrication des particules selon l'invention, qui comprend les étapes suivantes : - malaxage d'une poudre de sulfate de fer avec une solution de polysaccharide, en un mélange de sulfate de fer et de polysaccharide; séchage du mélange obtenu à l'étape précédente en les particules enrobées . Le procédé selon l'invention peut comprendre une étape supplémentaire de pré-broyage et tamisage préalablement à l'étape de malaxage, de manière à obtenir, à partir d'un stock de sulfate de fer brut, de la poudre de sulfate de fer.The invention also provides a method of manufacturing the particles according to the invention, which comprises the following steps: - mixing of an iron sulfate powder with a polysaccharide solution, in a mixture of iron sulfate and polysaccharide; drying the mixture obtained in the preceding step in the coated particles. The method according to the invention may comprise an additional step of pre-grinding and sieving prior to the kneading step, so as to obtain iron sulphate powder from a stock of crude iron sulphate.
La poudre de sulfate de fer de départ peut éventuellement être calibrée pour obtenir le diamètre final recherché. Dans la mesure où la quantité d'alginate est relativement faible, le diamètre de départ est seulement légèrement inférieur à celui d'arrivée.The starting iron sulfate powder may optionally be calibrated to obtain the desired final diameter. Since the amount of alginate is relatively small, the starting diameter is only slightly less than that of arrival.
On entend par « malaxage » toute technique conduisant à la formation d'un film protecteur autour du sulfate de fer, notamment le simple mélange, l'enrobage ou l ' encapsulation, quel que soit le matériel utilisé, notamment un mélangeur ou un lit d'air fluidisé (avec pulvérisation de la solution de polysaccharide sur une suspension de particules de sulfate de fer) .The term "kneading" is understood to mean any technique leading to the formation of a protective film around the iron sulphate, especially the simple mixing, coating or encapsulation, whatever the material used, in particular a mixer or a bed of iron. fluidized air (with spraying of the polysaccharide solution on a suspension of iron sulfate particles).
Selon un mode de réalisation du procédé selon la présente invention, on ajoute de l'acide (en particulier chlorhydrique) à la poudre de sulfate de fer et à la solution de polysaccharide avant la fin de l'étape de malaxage.According to one embodiment of the process according to the present invention, acid (in particular hydrochloric acid) is added. to the iron sulfate powder and the polysaccharide solution before the end of the mixing step.
L'acide (en particulier chlorhydrique) permet un dégonflement par repli sur elles-mêmes des chaînes du polysaccharide, ce qui a pour effet de former sur la surface du sulfate de fer un film protecteur plus dense. L'acide est ajouté jusqu'à obtention d'un pH acide, de préférence inférieur à 4,0 et notamment inférieur à 2,0.The acid (in particular hydrochloric acid) makes it possible to deflate the chains of the polysaccharide by themselves, which has the effect of forming a denser protective film on the surface of the iron sulphate. The acid is added until an acidic pH is obtained, preferably less than 4.0 and in particular less than 2.0.
Le procédé de préparation selon l'invention peut éventuellement comprendre une étape supplémentaire de broyage final et de tamisage, après l'étape de séchage du mélange, permettant d'obtenir, à partir des particules enrobées, des particules enrobées broyées et tamisées .The preparation process according to the invention may optionally comprise an additional step of final grinding and sieving, after the step of drying the mixture, making it possible to obtain, from the coated particles, grinded and sieved coated particles.
Selon un mode de réalisation particulier du procédé de préparation de la présente invention, la concentration massique de polysaccharide dans la solution de polysaccharide est comprise entre environ 0,01 et environ 10 %, en particulier comprise entre environ 0,1 et environ 5 %, et le rapport massique entre la solution de polysaccharide et le sulfate de fer à l'étape de malaxage est compris entre environAccording to a particular embodiment of the preparation method of the present invention, the mass concentration of polysaccharide in the polysaccharide solution is between about 0.01 and about 10%, in particular between about 0.1 and about 5%, and the mass ratio between the polysaccharide solution and the iron sulfate at the kneading step is between about
5 % et environ 50 %, en particulier entre environ 10 % et environ 35 %.5% and about 50%, especially between about 10% and about 35%.
Lors de la fixation de l'alginate sur le cœur de sulfate de fer, des molécules d'eau fixées auparavant par ces molécules d'alginate sont re-larguées. De manière générale, les quantités d'eau et d'alginate sont adaptées à la surface spécifique de la poudre de sulfate ferreux et à la qualité de cette poudre.When alginate is fixed on the iron sulphate core, water molecules previously fixed by these alginate molecules are re-dropped. In general, the amounts of water and alginate are adapted to the specific surface area of the ferrous sulphate powder and to the quality of this powder.
Les conditions du procédé sont en général les suivantes: - L'étape de malaxage est effectuée pendant une durée suffisante, qui peut être comprise entre 2 et 30 minutes . On préférera des durées courtes . La température est généralement la température ambiante, mais peut être plus élevée si besoin, ou peut éventuellement être augmentée en fin de malaxage.The conditions of the process are in general the following: the kneading step is carried out for a sufficient duration, which can be between 2 and 30 minutes. Short periods are preferred. The temperature is generally room temperature, but may be higher if needed, or may be increased at the end of mixing.
L'étape de séchage s'effectue à une température comprise entre la température ambiante et environ 700C, en particulier entre la température ambiante et 400C, pendant une durée suffisante pour éliminer l'eau libre de l'alginate. Le séchage peut s'effectuer sous pression réduite (ce qui diminue notablement la durée du séchage) . La fin du séchage peut être déterminée par contrôle visuel (les particules passent du vert au blanc crème) ou par suivi de perte de masse (jusqu'à ce que la masse des particules ne varie sensiblement plus) .The drying step is carried out at a temperature of between room temperature and approximately 70 ° C., in particular between room temperature and 40 ° C. for a time sufficient to remove the free water from the alginate. The drying can be carried out under reduced pressure (which significantly reduces the duration of drying). The end of the drying can be determined by visual inspection (the particles go from green to creamy white) or by loss of mass tracking (until the mass of the particles does not vary much more).
EXEMPLESEXAMPLES
Les exemples suivants illustrent 1 ' invention sans la limiter. Exemple 1. Synthèse de particules enrobées.The following examples illustrate the invention without limiting it. Example 1. Synthesis of coated particles.
Des particules enrobées selon l'invention sont préparées selon le protocole suivant: a) Une solution d'alginate de sodium (fournisseur: VWR International / Prolabo, numéro de catalogue 27 660.183; viscosité équivalente à celle du Satialgine S550 commercialisé par Degussa, cf. ci-dessus) est préparée par dissolution lente à chaud (500C) de poudre d'alginate de sodium (1,2 g) dans de l'eau déminéralisée (60 g) . b) 250 g de sulfate de fer heptahydraté (fournisseur: VWR International / Prolabo, numéro de catalogue 24 237.363) est broyé puis tamisé afin que la taille de ses particules soit inférieure à 100 μm (la plus grande particule ayant une taille de 100 μm) . c) Cette poudre de sulfate de fer tamisée est introduite dans un mélangeur Perrier ou Lodige . On rajoute ensuite à cette poudre la solution d'alginate de sodium dans une proportion d'environ 24 % par rapport à la masse de sulfate de fer. La quantité sèche d'alginate de sodium représente environ 0,5 % de la masse de sulfate de fer. L'ensemble est malaxé environ 30 minutes afin de permettre un enrobage homogène. d) L'enrobage est encore facilité par l'ajout d'acide chlorhydrique juste avant la fin du malaxage (1 mL à 3 M deCoated particles according to the invention are prepared according to the following protocol: a) A solution of sodium alginate (supplier: VWR International / Prolabo, catalog number 27 660.183, viscosity equivalent to that of Satialgine S550 marketed by Degussa, cf. above) is prepared by slow dissolution hot (50 0 C) of sodium alginate powder (1.2 g) in demineralized water (60 g). b) 250 g of iron sulphate heptahydrate (supplier: VWR International / Prolabo, catalog number 24 237.363) is crushed and sieved so that its particle size is less than 100 μm (the largest particle having a size of 100 μm ). c) This sieved iron sulfate powder is introduced into a Perrier or Lodige mixer. The sodium alginate solution is then added to this powder in a proportion of approximately 24% relative to the mass of iron sulphate. The dry amount of sodium alginate is about 0.5% of the iron sulfate mass. The whole is kneaded about 30 minutes to allow a homogeneous coating. d) The coating is further facilitated by the addition of hydrochloric acid just before the end of mixing (1 mL to 3 M of
HCl pour 50 g du mélange sulfate de fer / alginate de sodium. e) En fin de malaxage, on met le produit final dans une étuve à 1300C pendant environ 30 secondes. f) Le produit est ensuite séché à l ' étuve à 45°C pendant 2 jours afin d'évacuer l'eau contenue dans le film protecteur d' alginate . g) Le produit séché est enfin broyé afin d'obtenir une granulométrie inférieure à 100 μm. Cette étape de broyage est un broyage léger qui ne rompt pas le film protecteur d ' alginate .HCl for 50 g of the iron sulfate / sodium alginate mixture. e) At the end of mixing, the final product is placed in an oven at 130 ° C. for about 30 seconds. f) The product is then dried in an oven at 45 ° C for 2 days in order to evacuate the water contained in the protective film of alginate. g) The dried product is finally milled to obtain a particle size of less than 100 microns. This grinding step is a light grinding that does not break the protective alginate film.
Exemple 2. Réduction du chrome (VI) dans un ciment.Example 2. Reduction of chromium (VI) in a cement.
Dans cet exemple, on mesure la réduction du chrome (VI) dans différentes conditions de vieillissement du ciment.In this example, the reduction of chromium (VI) under different aging conditions of the cement is measured.
On utilise un ciment CEM 1 52.5N et contenant 15 ppm deA CEM 1 52.5N cement containing 15 ppm of
Chrome (VI) soluble.Chromium (VI) soluble.
On y ajoute, selon les tests, du sulfate de fer en poudre ou des particules enrobées selon l'invention. Dans tous les cas, le sulfate de fer, enrobé ou non, qui est utilisé en ajout avec le ciment, a une taille de particule inférieure àAccording to the tests, powdered iron sulphate or coated particles according to the invention are added thereto. In all cases, the iron sulphate, coated or not, which is used in addition with the cement, has a particle size smaller than
100 μm (taille maximale de la particule) .100 μm (maximum size of the particle).
Après avoir incorporé le sulfate de fer en poudre ou les particules enrobées selon l'invention au ciment, on soumet ce dernier à l'un ou l'autre de deux protocoles de vieillissement accéléré décrits ci-après. Ces deux protocoles de vieillissement accéléré constituent des conditions de conservation sévères (extrêmes) pour le ciment. Aussi, l'observation d'un "bon" comportement d'un ciment (en terme de faible teneur en chrome (VI) ) dans les conditions de vieillissement accéléré signifie a fortiori que ledit ciment aura nécessairement également un bon comportement dans des conditions de conservation/stockage usuelles.After incorporating the powdered iron sulfate or the coated particles according to the invention into the cement, the latter is subjected to one or the other of two accelerated aging protocols described below. These two accelerated aging protocols constitute severe (extreme) storage conditions for cement. Also, the observation of a "good" behavior of a cement (in terms of low chromium content (VI)) in the conditions of accelerated aging means a fortiori that said cement will necessarily also have a good behavior under conditions of usual storage / storage.
Lorsque du sulfate de fer (enrobé ou non) doit être ajouté au ciment, le sulfate de fer est mélangé et homogénéisé au ciment 45 minutes au Turbula® avant la mise en vieillissement du produit .When iron sulphate (coated or uncoated) must be added to the cement, the iron sulphate is mixed and homogenized with cement for 45 minutes with Turbula ® before the aging of the product.
Protocole de vieillissement n°l: forte humiditéAging protocol no. 1: high humidity
Ce test consiste à mettre, dans un bac, un lit de poudre de ciment contenant le sulfate de fer: la masse de ciment est d'environ 600 grammes et la hauteur du lit de matière 1 cm. Ce bac est ensuite placé dans une chambre maintenue à 200C et àThis test consists in putting in a tank a bed of cement powder containing iron sulphate: the mass of cement is approximately 600 grams and the height of the bed of material 1 cm. This tray is then placed in a chamber maintained at 20 0 C and
100 % d'humidité relative. Le bac reste 24 heures dans cette chambre, puis la mesure du chrome (VI) soluble est effectuée.100% relative humidity. The ferry stays 24 hours in this chamber, and then the measurement of soluble chromium (VI) is carried out.
On mesure à 1 jour.We measure to 1 day.
Protocole de vieillissement n°2: simulation siloAging protocol n ° 2: silo simulation
Ce test est destiné à simuler les conditions de stockage du ciment en silo. Le ciment arrive relativement chaud dans le silo en usine et reste confiné. Pour ce test, on introduit 1 , 5 kg de ciment dans une boîte métallique de dimensions 108 mm x 136 mm (volume 1 L) qui est ensuite fermée et placée dans une étuve régulée à 800C. On mesure la teneur en chrome (VI) soluble à 7 et 28 jours.This test is intended to simulate the storage conditions of the silo cement. The cement arrives relatively warm in the silo at the factory and remains confined. For this test, 1.5 kg of cement is introduced into a can of dimensions 108 mm × 136 mm (volume 1 L) which is then closed and placed in an oven regulated at 80 ° C. The chromium content is measured ( VI) soluble at 7 and 28 days.
Procédure de mesure du chrome (VI)Chromium (VI) measurement procedure
Le dosage du chrome (VI) est effectué selon le projet de norme PR NF EN 196-10 Mai 2005 "Méthodes d'essais des ciments - Partie 10: détermination de la teneur du ciment en chrome (VI) soluble dans l'eau". Résultats expérimentauxThe determination of chromium (VI) is carried out according to draft standard PR NF EN 196-10 May 2005 "Methods of testing cement - Part 10: Determination of the water-soluble content of chromium (VI) cement" . Experimental results
Les deux tableaux ci-dessous répertorient les résultats expérimentaux des mesures de chrome (VI) soluble dans des ciments soumis au protocole de vieillissement n°l (tableau 1) ou n°2 (tableau 2) .The two tables below list the experimental results of measurements of chromium (VI) soluble in cements subjected to the aging protocol No. 1 (Table 1) or No. 2 (Table 2).
A chaque fois, l'expression "témoin" désigne un état de référence du ciment (avec ou sans sulfate de fer ou particules enrobées) n'ayant pas subi de vieillissement. Les mesures "témoin" du chrome (VI) solubles sont donc obtenues sur un ciment témoin non vieilli ou un ciment non vieilli mélangé avec du sulfate de fer tout de suite après mélange et homogénéisation au Turbula® .In each case, the term "control" refers to a reference state of the cement (with or without iron sulfate or coated particles) which has not been aged. Measurements of chrome "light" (VI) soluble are therefore obtained on a cement unaged control or non-aged cement mixed with any iron sulfate immediately after mixing and homogenisation in the Turbula ®.
Tableau 1Table 1
Figure imgf000014_0001
Les résultats du tableau 1 démontrent clairement que, même dans des conditions très défavorables d'humidité, l'utilisation des particules enrobées selon l'invention permet une réduction beaucoup plus efficace de la teneur en chrome (VI) que l'utilisation de poudre de sulfate de fer, à teneur en sulfate de fer égale ou moindre.
Figure imgf000014_0001
The results in Table 1 clearly demonstrate that, even under very unfavorable humidity conditions, the use of the coated particles according to the invention allows a much more effective reduction of the chromium (VI) content than the use of iron sulphate with equal or less iron sulphate content.
Tableau 2Table 2
Figure imgf000015_0001
Figure imgf000015_0001
Les résultats du tableau 2 démontrent que l'utilisation de particules enrobées selon l'invention permet de réduire essentiellement tout le chrome (VI) soluble même après avoir soumis le ciment à 28 jours de vieillissement accéléré par la chaleur.The results in Table 2 demonstrate that the use of coated particles according to the invention makes it possible essentially to reduce all soluble chromium (VI) even after having subjected the cement to 28 days of accelerated aging by heat.
Exemple 3. Comparaison entre l'utilisation de sulfate de fer et de gluconate ferreux.Example 3. Comparison between the use of iron sulphate and ferrous gluconate.
Dans cet exemple, on compare l'efficacité relative du sulfate de fer par rapport au gluconate ferreux pour la réduction du chrome VI soluble.In this example, the relative efficiency of iron sulfate with respect to ferrous gluconate is compared for the reduction of soluble chromium VI.
Le sulfate de fer ou le gluconate ferreux est incorporé dans un ciment contenant initialement 13 ppm de chrome VI soluble, pour une même quantité de Fe2+ introduit (0,77 mM) dans les deux cas. La quantité finale de chrome VI dans le ciment est mesurée selon la méthode normalisée décrite ci- dessus . Les résultats sont présentés dans le Tableau 3 ci- dessous. On constate que, à quantités équivalentes de fer ferreux introduit, le gluconate ferreux est moins efficace que le sulfate ferreux pour réduire le chrome VI. Tableau 3Ferrous sulphate or ferrous gluconate is incorporated in a cement initially containing 13 ppm soluble chromium VI, for the same amount of Fe 2+ introduced (0.77 mM) in both cases. The final amount of chromium VI in the cement is measured according to the standard method described above. The results are shown in Table 3 below. It is found that, with equivalent amounts of ferrous iron introduced, ferrous gluconate is less effective than ferrous sulfate in reducing chromium VI. Table 3
Figure imgf000016_0001
Figure imgf000016_0001
Exemple 4. Quantité minimale de particules enrobées selon l'invention permettant une réduction totale du chrome VI.Example 4. Minimum amount of coated particles according to the invention for a total reduction of chromium VI.
Dans cet exemple, on mesure, selon la procédure normalisée décrite à l'exemple 2, la concentration restante de Chrome VI dans un ciment contenant initialement 15 ppm de Chrome VI, après ajout de particules enrobées selon l'invention, à différentes concentrations. Les résultats sont reportés dans le Tableau 4 ci -dessous, dans lequel la concentration de particules enrobées est représentée par la concentration de FeSO4 introduit. La première ligne du tableau représente le témoin (ciment sans particules enrobées) .In this example, the remaining concentration of Chrome VI in a cement initially containing 15 ppm of Chrome VI, after addition of the coated particles according to the invention, at different concentrations, is measured according to the standard procedure described in Example 2. The results are reported in Table 4 below, in which the concentration of coated particles is represented by the concentration of FeSO 4 introduced. The first line of the table represents the control (cement without coated particles).
Tableau 4Table 4
Figure imgf000016_0002
Figure imgf000016_0002
Exemple 5. Impact sur les propriétés d'usage du ciment. Des essais ont été effectués visant à évaluer l'impact de l'ajout d'alginate (alginate de sodium Prolabo) à un ciment sur les propriétés d'usage dudit ciment. On incorpore 0,1 % d'alginate à un ciment tel que défini dans l'exemple 1, c'est- à-dire environ 100 fois plus que la quantité d'alginate préconisée pour l'incorporation de particules enrobées selon 1' invention.Example 5. Impact on the properties of use of cement. Tests have been carried out to evaluate the impact of the addition of alginate (sodium alginate Prolabo) to a cement on the properties of use of said cement. 0.1% alginate is incorporated in a cement as defined in Example 1, that is, that is, about 100 times more than the amount of alginate recommended for incorporation of coated particles according to the invention.
On mesure les paramètres de temps de prise du ciment (détermination de la consistance et de la prise selon la norme EN 19G-3) (Tableau 5) ainsi que les paramètres de résistance mécanique, à savoir résistance en flexion (Rf) et résistance en compression (Rc) (tableau 6) . Les essais sont réalisés sur mortier normalisé.Curing time parameters (determination of consistency and setting according to EN 19G-3) (Table 5) and mechanical strength parameters, namely flexural strength (Rf) and compression (Rc) (Table 6). The tests are carried out on standard mortar.
Tableau 5Table 5
Figure imgf000017_0001
Figure imgf000017_0001
Tableau 6Table 6
Figure imgf000017_0002
Figure imgf000017_0002
On constate que l' alginate, même lorsqu'il est présent à une concentration aussi élevée, n'a pas d'impact sur les propriétés du ciment, ce qui implique, a fortiori, qu'une quantité beaucoup plus faible n'aura pas d'impact. L'utilisation des particules enrobées selon l'invention n'aura donc pas d'impact sur les propriétés d'usage du ciment. It is found that alginate, even when present at such a high concentration, has no impact on the properties of the cement, which implies, a fortiori, that a much smaller quantity will not have impact. The use of the coated particles according to the invention will therefore have no impact on the properties of use of the cement.

Claims

REVENDICATIONS
1. Ciment comprenant des particules enrobées, lesdites particules enrobées comprenant: (a) un cœur comprenant du sulfate de fer et / ou du sulfate d' étain et / ou du sulfate de manganèse; et (b) une enveloppe comprenant de l'acide alginique ou l'un de ses dérivés.A cement comprising coated particles, said coated particles comprising: (a) a core comprising iron sulfate and / or tin sulfate and / or manganese sulfate; and (b) an envelope comprising alginic acid or a derivative thereof.
2. Ciment selon la revendication 1, dans lequel le dérivé d'acide alginique est l'alginate de sodium, l'alginate de potassium, l'alginate de calcium, l'alginate de magnésium, l'alginate d'ammonium ou le propylène glycol alginate .The cement of claim 1, wherein the alginic acid derivative is sodium alginate, potassium alginate, calcium alginate, magnesium alginate, ammonium alginate or propylene. glycol alginate.
3. Ciment selon la revendication 1 ou 2 , dans lequel le cœur des particules enrobées comprend du sulfate de fer monohydraté ou heptahydraté ou un mélange de sulfate de fer monohydraté et heptahydraté.3. Cement according to claim 1 or 2, wherein the core of the coated particles comprises iron sulfate monohydrate or heptahydrate or a mixture of iron sulfate monohydrate and heptahydrate.
4. Ciment selon l'une des revendications 1 à 3, dans lequel les particules enrobées ont une taille dmax inférieure à environ 200 μm, de préférence inférieure à environ 100 μm.4. Cement according to one of claims 1 to 3, wherein the coated particles have a size d max less than about 200 microns, preferably less than about 100 microns.
5. Ciment selon l'une des revendications 1 à 4, dans lequel l'acide alginique ou dérivé de l'enveloppe représente, par rapport au poids du cœur, une quantité comprise entre 0,05 et 5 %, de préférence entre 0,2 et 2 %.5. Cement according to one of claims 1 to 4, wherein the alginic acid or derived from the envelope is, based on the weight of the core, an amount of between 0.05 and 5%, preferably between 0, 2 and 2%.
6. Ciment selon l'une des revendications 1 à 5, dans lequel les particules enrobées sont stables au stockage pendant une durée comprise entre 3 et 9 mois.6. Cement according to one of claims 1 to 5, wherein the coated particles are stable storage for a period of between 3 and 9 months.
7. Ciment selon l'une des revendications 1 à 6, obtenu à partir d'un ciment dépourvu de particules enrobées, et contenant une quantité de particules enrobées telle que la quantité en poids de sulfate de fer et / ou de sulfate d'étain et / ou de sulfate de manganèse est inférieure à 0,02 %, en particulier inférieure à 0,01 %, et de préférence inférieure à 0,005 % par ppm de chrome (VI) soluble présent dans ledit ciment dépourvu de particules enrobées.7. Cement according to one of claims 1 to 6, obtained from a cement free of coated particles, and containing a quantity of coated particles such that the amount by weight of iron sulfate and / or tin sulfate and / or manganese sulfate is less than 0.02%, in particular less than 0.01%, and preferably less than 0.005% by ppm of soluble chromium (VI) present in said cement free of coated particles.
8. Ciment selon l'une des revendications 1 à 7, contenant une quantité en poids de sulfate de fer et / ou de sulfate d'étain et / ou de sulfate de manganèse inférieure à 0,3 %, en particulier inférieure à 0,2 %, et de préférence inférieure à 0,1 %, et ayant une teneur en chrome (VI) inférieure à 2 ppm.8. Cement according to one of claims 1 to 7, containing an amount by weight of iron sulfate and / or tin sulfate and / or manganese sulfate less than 0.3%, in particular less than 0, 2%, and preferably less than 0.1%, and having a chromium (VI) content of less than 2 ppm.
9. Ciment selon l'une des revendications 1 a 8, dans lequel les particules enrobées sont présentes sous forme de poudre .9. Cement according to one of claims 1 to 8, wherein the coated particles are present in powder form.
10. Utilisation de ciment selon l'une des revendications 1 à 9 dans la préparation d'un béton ou d'un mortier.10. Use of cement according to one of claims 1 to 9 in the preparation of a concrete or a mortar.
11. Procédé de fabrication de ciment selon l'une des revendications 1 à 9, comprenant: la préparation des particules enrobées; et - le mélange des particules enrobées au ciment.11. Cement manufacturing method according to one of claims 1 to 9, comprising: the preparation of the coated particles; and - the mixture of the particles coated with cement.
12. Procédé selon la revendication 11, dans lequel la préparation des particules enrobées comprend les étapes suivantes : - malaxage d'une poudre de sulfate de fer et / ou de sulfate d'étain et / ou de sulfate de manganèse avec une solution d'acide alginique ou dérivé, en un mélange de sulfate de fer et / ou de sulfate d'étain et / ou de sulfate de manganèse et d'acide alginique ou dérivé; séchage du mélange obtenu à l'étape précédente en les particules enrobées. 12. The method of claim 11, wherein the preparation of the coated particles comprises the following steps: - mixing of an iron sulfate powder and / or tin sulfate and / or manganese sulfate with a solution of alginic acid or derivative, a mixture of iron sulfate and / or tin sulfate and / or manganese sulfate and alginic acid or derivative; drying the mixture obtained in the preceding step in the coated particles.
13. Procédé selon la revendication 12, dans lequel on ajoute de l'acide à la poudre de sulfate de fer et / ou de sulfate d'étain et / ou de sulfate de manganèse et à la solution d' acide alginique ou dérivé avant la fin de l'étape de malaxage.The process according to claim 12, wherein acid is added to the iron sulfate and / or tin sulfate and / or manganese sulphate powder and to the alginic acid or derivative solution prior to end of the mixing step.
14. Procédé selon la revendications 12 ou 13 , comprenant une étape supplémentaire de broyage final et de tamisage, après l'étape de séchage du mélange.14. The method of claim 12 or 13, comprising an additional step of final grinding and sieving, after the step of drying the mixture.
15. Procédé selon l'une des revendications 12 à 14, dans lequel la concentration massique de d'acide alginique ou dérivé dans la solution d'acide alginique ou dérivé est comprise entre environ 0,01 et environ 10 %, en particulier comprise entre environ 0,1 et environ 5 %, et dans lequel le rapport massique entre la solution d'acide alginique ou dérivé et le sulfate de fer et / ou le sulfate d'étain et / ou le sulfate de manganèse à l'étape de malaxage est compris entre environ 5 % et environ 50 %, en particulier entre environ 10 % et environ 35 %.15. The process as claimed in one of claims 12 to 14, in which the mass concentration of alginic acid or derivative in the solution of alginic acid or derivative is between approximately 0.01 and approximately 10%, in particular between about 0.1 and about 5%, and wherein the weight ratio between the alginic acid or derivative solution and the iron sulfate and / or the tin sulfate and / or the manganese sulfate at the mixing step is from about 5% to about 50%, especially from about 10% to about 35%.
16. Procédé selon l'une des revendications 12 à 15, dans lequel la température lors de l'étape de malaxage est la température ambiante.16. The method according to one of claims 12 to 15, wherein the temperature during the kneading step is the ambient temperature.
17. Procédé selon l'une des revendications 12 à 16, dans lequel l'étape de séchage s'effectue à une température comprise entre la température ambiante et environ 7O0C, en particulier à une température comprise entre la température ambiante et environ 400C, pendant une durée comprise entre environ 2 heures et environ 5 jours, à la pression atmosphérique ou sous pression réduite.17. A method according to one of claims 12 to 16, wherein the drying step is performed at a temperature between room temperature and about 7O 0 C, especially at a temperature between room temperature and about 40 0 C, for a period of between about 2 hours and about 5 days, at atmospheric pressure or under reduced pressure.
18. Ciment selon l'une des revendications 1 à 9, susceptible d'être obtenu par le procédé de l'une des revendications 11 à 17. 18. Cement according to one of claims 1 to 9, obtainable by the method of one of claims 11 to 17.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2917083A1 (en) * 2007-06-08 2008-12-12 Lafarge Sa "ADDITIVE FOR CEMENT-BASED COMPOSITION"
US8142564B2 (en) 2007-05-10 2012-03-27 Lafarge Process to reduce the amount of Cr (VI) in a cement-containing composition and a composition comprising cement and coated metallic sulphate particles
EP2662346A1 (en) 2012-05-07 2013-11-13 Mapei S.p.A. Portland cement additives consisting of a reducing agent embedded in a polymer matrix
GB2502345A (en) * 2012-05-25 2013-11-27 Nexeon Ltd Composite particle comprising a polymer coating insoluble in N-methyl pyrrolidone

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2969144B1 (en) * 2010-12-15 2013-01-18 Chryso IRON ADJUVANT FOR REDUCING CHROME VI

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4572739A (en) * 1980-12-17 1986-02-25 Rasmussen Poul L Method for reducing chromate dermatitis
DE29613095U1 (en) * 1996-07-29 1996-10-02 Heidelberger Zement Ag, 69120 Heidelberg Hydrophobicized ferrous sulfate and its use
EP1520843A1 (en) * 2003-09-18 2005-04-06 Alexander Kehrmann Hydraulic binder
US20050109243A1 (en) * 2003-11-21 2005-05-26 Jardine Leslie A. Sulfate dispersion chromate reducer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4572739A (en) * 1980-12-17 1986-02-25 Rasmussen Poul L Method for reducing chromate dermatitis
DE29613095U1 (en) * 1996-07-29 1996-10-02 Heidelberger Zement Ag, 69120 Heidelberg Hydrophobicized ferrous sulfate and its use
EP1520843A1 (en) * 2003-09-18 2005-04-06 Alexander Kehrmann Hydraulic binder
US20050109243A1 (en) * 2003-11-21 2005-05-26 Jardine Leslie A. Sulfate dispersion chromate reducer

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
"Die Bedeutung des Chromates in Zementen und zementhaltigen Zubereitungen" VEREIN DEUTSCHER ZEMENTWERKE E.V. FORSCHUNGSINSTITUT DER ZEMENTINDUSTRIE, [Online] 5 janvier 1999 (1999-01-05), XP002400742 Extrait de l'Internet: URL:http://www.wbcsd.org/web/projects/cement/tf3/VDZ-Sachstandsbericht-Chromat.pdf#search=%22bedeutung%20%20chromates%20zement%20vdz%22> [extrait le 2006-09-20] *
BAETZNER S: "WAYS OF ANALYZING IRON(II) SULPHATE HYDRATE IN RESPECT OF ITS CHROMATE-REDUCING ACTION IN CEMENT" ZKG INTERNATIONAL, BAUVERLAG BV., TERSLOH, DE, vol. 55, no. 7, 2002, pages 80-86,88, XP001116336 ISSN: 0949-0205 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8142564B2 (en) 2007-05-10 2012-03-27 Lafarge Process to reduce the amount of Cr (VI) in a cement-containing composition and a composition comprising cement and coated metallic sulphate particles
FR2917083A1 (en) * 2007-06-08 2008-12-12 Lafarge Sa "ADDITIVE FOR CEMENT-BASED COMPOSITION"
FR2917082A1 (en) * 2007-06-08 2008-12-12 Lafarge Sa Additive, useful to prepare cement based composition containing concrete, mortar or cement, comprises particles of iron (II) sulfate dry heptahydrate
EP2662346A1 (en) 2012-05-07 2013-11-13 Mapei S.p.A. Portland cement additives consisting of a reducing agent embedded in a polymer matrix
GB2502345A (en) * 2012-05-25 2013-11-27 Nexeon Ltd Composite particle comprising a polymer coating insoluble in N-methyl pyrrolidone
GB2502345B (en) * 2012-05-25 2017-03-15 Nexeon Ltd Composite material

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