The present invention relates to an ultra–light cement–based mineral foam, to a
method for producing this foam and to construction elements comprising this foam.
5 In general, a mineral foam, in particular a cement foam, is highly advantageous for
numerous applications on account of its properties such as thermal and sound
insulation, durability, fire resistance and ease of use.
Mineral foam designates a material in the form of a foam. This material is lighter than
traditional concrete on account of the pores or voids contained therein. These pores or
10 voids are due to the presence of air in the mineral foam and may be in the form of
bubbles. By ultra–light foam is meant foam having a dry density generally of 30 to 300
kg/m3.
When an element in mineral foam is cast it may collapse, for example through lack of
stability of the mineral foam as soon as it is placed or before complete hardening.
15 These problems of foam collapse may be due to phenomena of coalescence, Ostwald
ripening, hydrostatic pressure or drainage, the latter particularly being more extensive in
elements of large height.
The difficulty in producing mineral foam is therefore the obtaining of a stable foam
overcoming problems of collapse. Yet known techniques to allow the obtaining of
20 sufficiently stable foam have recourse to mixtures of cementitious compounds
comprising numerous admixtures which are therefore difficult and costly to produce.
The simultaneous use has already been proposed in patent US 5,696,174 of cationic
(I) and anionic (II) compounds to produce foams. Such cement foams comprise
ammonium stearate as anionic compound and a cationic compound called Arquad T.
25 Application WO 2013/150148 describes cement–based foams comprising various
admixtures. These foams may comprise calcium aluminate to allow rapid setting, or fine
mineral particles.
To meet user requirements, it has become necessary to find means for producing an
ultra–light mineral foam, having high stability and which is relatively easy to produce at
30 low cost.
Therefore, the problem that the invention sets out to solve is to find a formulation for
a stable, ultra–light mineral foam which does not collapse when the foam is vertically
cast and is relatively easy and cheap to process.
The invention relates to a method for producing a mineral foam comprising the
35 following steps:
(i) independently preparing a cement slurry and an aqueous foam, the
cement slurry being prepared by mixing water W and cement C, the cement C
2
comprising an amount x of soluble Na2O equivalent, x being expressed in weight per
100 parts of cement, said slurry having a ratio x / (W/C) less than or equal to 1.75,
with W/C expressed by weight, and the particles of cement C have a particle size
distribution such that the ratio dmax(h/2)/dmin(h/2) of the particle size distribution is
5 between 5 and 25;
(ii) contacting the cement slurry with the aqueous foam to obtain a slurry of
foamed cement; and
(iii) forming the slurry of foamed cement obtained at step (ii) and leaving to
set.
10 The soluble Na2O equivalent amount, or alkali content, of the cement slurry is
therefore surprisingly an important characteristic in the production of a stable mineral
foam. Here the expression “alkali content” is used to designate the weight proportion of
soluble Na2O equivalent i.e. of soluble sodium or potassium ions ((MNa2O / MK2O)*
K2O+Na2O)= Na2Oeq in the cement used to implement the method of the invention, with
15 M being the molar mass of the compounds in subscript. The K2O and Na2O levels are
measured after dissolution by atomic emission spectrometry, a method known as ICPAES
described below.
This cement C is placed in the presence of a given amount of water W in the
slurry, characterized by the weight ratio W/C. The limit value in terms of alkali to allow
20 stability of the final mineral foam is characterized by the ratio x / (W/C) which must not
exceed 1.75, x being the amount of soluble Na2O equivalent (Na2Oeq) by weight per
100 parts of cement.
Advantageously, the weight ratio x / (W/C) is less than or equal to 1.60, preferably
less than or equal to 1.50.
25 Preferably, the weight ratio x / (W/C) is between 0.1 and 1.75.
To implement the invention and achieve the weight ratio x / (W/C), one of the
elements to be taken into consideration is therefore the alkali content of the cement.
The selecting of a cement already having a low alkali content when produced (e.g. a
low alkali cement of CEM I type or use of a compound cement) is one simple way to
30 reach this ratio and to obtain an ultra-light foam. However, there are other ways to
achieve the target ratio e.g. diluting the cement through the addition of water.
The cement used in the method of the invention comprises particles having a
distribution size such that the ratio dmax(h/2)/dmin(h/2) of particle size distribution (volume
distribution) is from 5 to 25, preferably this ratio dmax(h/2)/dmin(h/2) is from 6 to 14.
35 The particle size distribution in a sample is measured using the laser diffraction
method. Said particle size distribution may be that of a monodisperse population of
solid particles. By monodisperse is meant that the graphical representation of particle
3
size distribution (volume abundance as a function of size graduated on a Renard series
scale) only has one peak (a single population). This definition of "monodisperse load"
preferably excludes particle stacking of several populations of different particle sizes.
A group of particles of different sizes can be characterized in particular by the
5 ratio between (i) the size of the largest particles at mid-height (dmax(h/2)) and (ii) the size
of the finest particles at mid-height (dmin(h/2)). To implement the invention this ratio is in
the order of 5 to 25 in the cement used, preferably from 6 to 14.
The values dmax(h/2) and dmin(h/2) are obtained as follows: the height h is the height
of the highest peak measured by laser particle size measurement represented in
10 volume (see for example Figure 1). Taking height h/2 as reference, dmax(h/2) and dmin(h/2)
are respectively defined as the largest particle size and smallest particle size having a
proportion equal to h/2.
Preferably, the cement used in the method of the invention comprises particles
having a monodisperse particle size distribution.
15 Cement is a hydraulic binder comprising a proportion at least equal to 50 % by
weight of calcium oxide (CaO) and silicon dioxide (SiO2). A cement may therefore
comprise other compounds in addition to CaO and SiO2, and in particular Portland
clinker, slag, silica fume, pozzolan (natural and calcined natural), fly ash (siliceous and
calcic), shale and/or limestone. The cements able to be used in the method of the
20 invention for the production of mineral foam can be selected from among the cements
described in standard NF-EN197-1 of April 2012, in particular the cements CEM I,
CEM II, CEM III, CEM IV or CEM V.
The cement used to carry out the invention is preferably selected from among
commercially available cements having sufficiently low alkalinity or “low alkali cements”.
25 Low alkali cements of Portland type are the preferred cements. However, if Portland
cements and in particular their clinker content have an alkali proportion that is too high,
such cements can be diluted through the addition of compounds such as limestone
CaCO3, slag, fly ash, pozzolan or the mixtures thereof. In this case, cements composed
of CEM II to V types comprising a non-negligible proportion of components other than
30 clinker can be used to reduce alkalinity and to reach the desired concentration.
According to one particular embodiment, the cement suitable for use in the present
invention has a Blaine specific surface area of 3 500 to 10 000 cm2/g, preferably 6 000
to 9 000 cm2/g.
The Portland cement able to be used in the present invention can be milled
35 and/or separated (using a dynamic separator) to obtain cement having a Blaine specific
surface area of 5 500 cm²/g or higher. This cement can be qualified as being ultra-fine.
The cement can be milled using 2 methods.
4
According to a first method, the cement or clinker can be milled to a Blaine
specific surface area of 5 500 to 10 000 cm²/g. A second or third generation high
efficiency separator or very high efficiency separator can be used at this first step to
separate the cement having the desired fineness. The material not having the desired
5 fineness is returned to the mill.
The mills that can be used for this method are ball mills for example or a vertical
mill, roller press, horizontal mill (e.g. of Horomill© type), an agitated vertical mill (e.g.
Tower Mill type), an agitated bead mill or any other type of mill adapted for the fine
milling of mineral particles.
10 According to a second method, a Portland cement can be passed through a
dynamic separator to extract the finest particles, so as to reach the target fineness
(higher than 5 500 cm²/g). The fine material can be used as such. The coarse material
is removed for other applications or returned towards a different milling circuit.
The cement slurry used in the method of the invention may advantageously
15 comprise a water reducing agent of plasticizer or superplasticizer type. A water reducing
agent allows a reduction in mixing water of about 10 to 15 weight % over a given
workability time. As examples of water reducing agents mention can be made of
lignosulphonates, hydroxycarboxylic acids, carbohydrates and other specific organic
compounds such as glycerol, polyvinyl alcohol, sodium aluminomethyl siliconate,
20 sulfanilic acid and casein (see Concrete Admixtures Handbook, Properties Science and
Technology, V.S. Ramachandran, Noyes Publications, 1984). Superplasticizers belong
to the new generation of water reducing agents and allow a reduction in mixing water of
about 30 weight % for a given workability time. As examples of superplasticizers
mention can be made of PCP superplasticizers free of anti-foaming agent, PEO
25 diphosphonates, PEO polyphosphates. By the term “PCP” or “polycarboxylate
polyoxide” according to the invention is meant a copolymer of acrylic or methacrylic
acids and their polyethylene oxide esters (PEO).
Preferably, the cement slurry used to produce the mineral foam of the invention
comprises 0.05 to 1 %, more preferably 0.05 to 0.5 % of water reducing agent, a
30 plasticizer or superplasticizer, percentage expressed in dry weight relative to the weight
of the cement slurry.
Preferably, the water reducing agent of plasticizer or superplasticizer type does not
contain any anti-foaming agent.
The cement slurry or aqueous foam may also comprise 0.05 to 2.5 % of an
35 accelerator, percentage expressed in dry weight relative to the cement. This accelerator
may derive from one or more salts selected from among:
5
- calcium salts, potassium salts and sodium salts, in which the anion may be a
nitrate, nitrite, chloride, formiate, the thiocyanate, sulfate, bromide, carbonate or
mixtures thereof; and
- alkaline silicates and aluminates, e.g. sodium silicate, potassium silicate, sodium
5 aluminate, potassium aluminate or mixtures thereof; aluminium salts e.g.
aluminium sulfate, aluminium nitrate, aluminium chloride, aluminium hydroxide or
mixtures thereof.
According to one particular embodiment, the aqueous foam does not comprise an
accelerator and in particular no calcium salts.
10 Other admixtures can be added either to the cement slurry or to the aqueous foam.
Said admixtures may be a thickening agent, viscosifying agent, air entraining agent, set
retarder, clay inerting agent, pigments, colouring agents, hollow glass beads, filmforming
agents, hydrophobic agents or depollutants (e.g. zeolites or titanium dioxide),
latex, organic or mineral fibres, mineral additions or mixtures thereof.
15 Preferably the admixtures used do not comprise any anti-foaming agent.
Preferably the mineral foam of the invention comprises a mineral addition. This
addition may be added to the cement slurry during the method of the invention.
For example, the mineral additions are slag (e.g. such as defined in standard
NF EN 197-1 of April 2012, paragraph 5.2.2), pozzolan (e.g. such as defined in
20 standard NF EN 197-1 of April 2012, paragraph 5.2.3), fly ash (e.g. such as defined in
standard NF EN 197-1 of April 2012, paragraph 5.2.4), calcined shale (e.g. such as
defined in standard NF EN 197-1 of April 2012, paragraph 5.2.5), materials containing
calcium carbonate such as limestone (e.g. such as defined in standard NF EN 197-1 of
April 2012, paragraph 5.2.6), silica fume (e.g. such as defined in standard NF EN 197-1
25 of April 2012, paragraph 5.2.7), metakaolins or mixtures thereof.
However, according to one particularly preferred aspect of the invention, only a
limited number of components is used. Therefore, the mineral foam may only be formed
either of cement, water and a foaming agent, or of cement, water, a foaming agent and
a water reducing agent of plasticizer or superplasticizer type such as a PCP
30 Such a formulation allows considerable savings in time and cost and goes against
preconceived technical opinion according to which the use of various admixtures is
necessary to ensure the stability of a cement foam.
Preferably, the mineral foam of the invention contains substantially no fine
particles. By the expression “fine particles” is meant a population of particles having a
35 median diameter D50 strictly lower than 2 jim. D50, also denoted DV50, corresponds to
the 50th percentile of particle size distribution in volume i.e. 50 % of the volume is
formed of particles having a size smaller than D50 and 50 % of size larger than D50.
6
By the term “substantially” is meant less than 1%, advantageously less than 5 %,
expressed in weight relative to the weight of the cement.
According to another aspect of the invention, the mineral foam of the invention does
not contain a mixture of two organic compounds respectively forming a long chain
5 anionic compound and cationic compound such as described in patent US 5,696,174.
The cements that are little or not suitable for implementation of the invention are
calcium aluminate cements and mixtures thereof. Calcium aluminate cements are
cements generally comprising a mineralogical phase, C4A3$, CA, C12A7, C3A or
C11A7CaF2 or mixtures thereof such as Ciments Fondu®, sulfoaluminate cements,
10 calcium aluminate cements conforming to European standard NF EN 14647 of
December 2006. Such cements are characterized by an aluminium oxide content
(Al2O3) greater than or equal to 35 weight. Therefore, to carry out the method of the
invention, the aluminium oxide content of the dry mineral compound used to produce
the foam is less than 35 weight % of the dry mineral compound. Preferably this content
15 is less than or equal to 30 %, advantageously less than or equal to 20 %, more
advantageously less than or equal to 15 %, and further advantageously less than or
equal to 10%, in dry compound weight.
According to a first embodiment, the cement slurry can be prepared by loading the
cement mixer with the cement and optionally all the other materials in powder form. The
20 cement is mixed to obtain a homogeneous mixture. Water is then added to the mixer.
The admixture(s) such as a water reducing agent are added with the water if they are
contained in the formulation of the mineral foam. The paste obtained is mixed to obtain
a cement slurry.
Preferably, the cement slurry is held under agitation e.g. using a deflocculating
25 blade, the speed of the blade possibly varying from 1000 rpm to 400 rpm, as a function
of slurry volume, throughout the entire duration of the method to produce the mineral
foam of the invention.
According to a second embodiment, the cement slurry can be prepared by loading
part of the water in the mixer, followed by the cement and then the other compounds.
30 According to a third embodiment, the cement slurry can be continuously generated.
To prepare the cement slurry, the W/C ratio of this slurry may advantageously range
from 0.23 to 2.0, preferably from 0.25 to 0.60, for example equal to 0.29, the ratio being
expressed by weight.
The aqueous foam can be prepared by contacting the water with a foaming agent
35 and then adding a gas. Therefore, the aqueous foam comprises water and a foaming
agent. This gas is preferably air. The amount of foaming agent is generally between
0.25 and 5 % by dry matter weight of foaming agent relative to the weight of water,
7
preferably 0.75 % to 2.5 %. The adding of air can be obtained by agitation, bubbling or
injection under pressure. Preferably, the aqueous foam can be prepared using a
turbulence foamer (bed of glass beads for example). This type of foamer allows air to
be added under pressure to an aqueous solution comprising a foaming agent.
5 Preferably, the aqueous foam can be generated continuously.
The generated aqueous foam has an air bubble size having a D50 equal to or less
than 400 jim, preferably from 100 to 400 jim, more preferably from 150 to 300 jim. D50,
also denoted DV50, corresponds to the 50th percentile of particle size distribution in
volume i.e. 50 % of the volume is formed of particles having a size smaller than D50
10 and 50 % of size larger than D50.
Preferably, the generated aqueous foam has an air bubble size having a D50 of
250 jim.
The D50 of the bubbles is measured by back scattering. The apparatus used is
Turbiscan ® Online supplied by Formulaction. Back scattering measurements allow an
15 estimation of the D50 for bubbles of an aqueous foam with knowledge of the volume
fraction of the bubbles and the refractive index of the foaming agent solution.
Preferably, the foaming agent is an organic derivative of proteins of animal origin
(e.g. the foaming agent Propump26, a powder of hydrolysed keratin sold by Propump)
or plant origin. The foaming agents may also be cationic (e.g. cetyltrimethylammonium
20 CTAB), anionic, amphoteric (e.g. cocoamidopropyl betaine CAPB) or non-ionic
surfactants, or mixtures thereof.
The contacting of the cement slurry with the aqueous foam to obtain a slurry of
foamed cement can be performed using any means e.g. using a static mixer.
According to one more particular embodiment, the cement slurry is pumped at a
25 constant volume rate as a function of the composition of the target foamed cement
slurry.
The cement slurry is then contacted with the aqueous foam already in circulation in
the circuit of the process. The foamed cement slurry of the invention is thus generated.
This foamed cement slurry is formed and left to set.
30 Advantageously, the method of the invention does not require an autoclave step
or curing step or heat treatment step e.g. at 60-80°C to obtain a cement foam of the
invention.
The mineral foam of the invention can be pre-manufactured or directly prepared
at the worksite by installing an onsite foaming system.
35 A further subject of the invention is a foamed cement slurry which can be obtained
at step (ii) of the method of the invention.
8
A further subject of the invention is a mineral foam obtainable using the method of
the invention.
Preferably, the mineral foam of the invention has a dry density of 35 to 300 kg /
m3, more preferably of 50 to 150 kg / m3, further preferably of 50 to 80 kg / m3. It is to be
5 noted that the density of the foamed cement slurry (wet density) differs from the density
of the mineral foam (density of hardened material).
Preferably, the mineral foam of the invention has thermal conductivity of 0.030 to
0.150 W/(m.K), more preferably 0.030 to 0.060 W/(m.K) and further preferably 0.030 to
0.040 W/(m.K), the margin of error being ± 0.4 mW/(m.K).
10 The invention also relates to a construction element comprising a mineral foam of
the invention.
The use of the mineral foam of the invention in the construction sector is also a
subject of the invention. For example, the mineral foam of the invention can be used to
cast walls, floors, roofing on a worksite. It is also envisaged to produce prefabricated
15 elements from the foam of the invention at a prefabrication plant, such as blocks,
panels.
The invention also relates to the use of the mineral foam of the invention as
insulating material, in particular as thermal or sound insulation.
Advantageously, the mineral foam of the invention in some cases allows the
20 replacement of glass wool, mineral wool or polystyrene or polyurethane insulating
materials.
Preferably, the mineral foam of the invention therefore has very low thermal
conductivity. Reducing the thermal conductivity of building materials is highly desirable
since it brings savings in heating energy in homes and at workplaces. In addition, the
25 mineral foam of the invention allows good insulating performance to be obtained with
narrow thicknesses, thereby preserving habitable surfaces and volumes. Thermal
conductivity (also known as lambda (λ)) is a physical magnitude characterizing the
behaviour of materials at the time of heat transfer via conduction. Thermal conductivity
represents the amount of heat transferred per unit surface area and per unit of time
30 under a temperature gradient. In the international unit system, thermal conductivity is
expressed in watts per metre-kelvin (W·m-1·K- 1). Conventional or traditional
concretes have thermal conductivity between 1.3 and 2.1 measured at 23°C and 50 %
relative humidity. The mineral foam of the invention can be selected from among foams
having thermal conductivity ranging from 0.030 to 0.150 W/(m.K), preferably 0.030 to
35 0.060 W/(m.K) and more preferably 0.030 to 0.040 W/(m.K), the margin of error being ±
0.4 mW/(m.K).
9
Advantageously, the mineral foam of the invention can be used for filling an empty
space or hollow in a building, a wall, partition, masonry block e.g. a breeze block, a
brick, floor or ceiling. Said materials or composite building elements comprising the
mineral foam of the invention are also subjects of the invention per se.
5 Advantageously, the mineral foam of the invention can be used as facade rendering
e.g. for the external insulation of a building. In this case, the mineral foam of the
invention may be coated with a finish rendering.
A further subject of the invention is a device comprising the mineral foam of the
invention. The foam may be contained in the device as insulating material. The device
10 of the invention is advantageously capable of resisting or reducing air and thermo–
hydric transfer i.e. this element has controlled permeability against transfer of air and of
water in vapour or liquid form.
The device of the invention preferably comprises at least one frame or structural
element. This frame may be in concrete (posts/beams), metal (upright or rail), wood,
15 plastic, composite material or synthetic material. The mineral foam of the invention may
also surround a structure of lattice type for example (plastic, metallic).
The device of the invention can be used to form or manufacture a lining, insulating
system, or partition e.g. a dividing partition, load distributing partition or wall lining.
The mineral foam of the invention can be vertically cast between two walls selected
20 for example from among concrete shells, brick walls, plasterboards, wood board e.g.
oriented thin strip wood panels, or fibre–cement panels, the whole forming a device.
The invention will be better understood on reading the following examples and
Figures that are not in any manner restrictive and in which:
Figure 1 is a graphical illustration of the particle size distribution in a typical cement
25 used to implement the invention.
The following measuring methods were used:
Laser particle size measurement
The particle size curves of the different powders were obtained using a laser size
analyser of Mastersizer 2000 type (year 2008, series MAL1020429) sold by Malvern.
30 Measurement is carried out in a suitable medium (e.g. an aqueous medium) to
disperse the particles; the particle size must be between 1 μm and 2 mm. The light
source is a red He–Ne laser (632 nm) and blue diode (466 nm). The optical mode is a
Fraunhofer model with polydisperse particle sizing standard.
Measurement of background noise is first performed using a pump rate of
35 2000 rpm, an agitator speed of 800 rpm and noise measurement over 10 s, in the
absence of ultrasound. It is first verified that the light intensity of the laser is at least
10
80%, and that a decreasing exponential curve is obtained for background noise. If this
is not the case, the cell lenses must be cleaned.
A first measurement is taken on the sample with the following parameters: pump
speed 2000 rpm, agitator speed 800 rpm, no ultrasound, obscuration limit between 10
5 and 20 %. The sample is inserted to obtain obscuration slightly higher than 10 %. After
stabilisation of obscuration, measurement is conducted with a time between immersion
and measurement set at 10 s. Measurement time is 30 s (30000 diffraction images
analysed). In the size distribution graph obtained, consideration must be given to the
fact that part of the powder population may be agglomerated.
10 A second measurement is then carried out (without emptying the vessel) with
ultrasound. The pump rate is increased to 2500 rpm agitation to 1000 rpm, and with 100
% ultrasound emission (30 watts). This regimen is maintained for 3 minutes, before
returning to the initial parameters: pump rate 2000 rpm, agitator speed 800 rpm, no
ultrasound. After 10 s (to evacuate any air bubbles), a 30 s measurement is performed
15 (30000 images analysed). This second measurement corresponds to a powder de–
agglomerated by ultrasonic dispersion.
Each measurement is repeated at least twice to verify the stability of the result.
The apparatus is calibrated before each work session using a standard sample (C10
silica Sifraco) having a known particle size curve. All the measurements given in the
20 description and the given ranges correspond to the values obtained with ultrasound.
Method for measuring BLAINE specific surface area
The specific surface area of the different materials was measured as follows:
The Blaine method at 20°C with relative humidity not exceeding 65 %, using
Blaine Euromatest Sintco apparatus conforming to European standard EN 196–6.
25 Before measuring the specific surface area, the wet samples were dried to
constant weight in an oven at a temperature of 50 to 150°C (the dried product was then
ground to obtain a powder having a maximum particle size of 80 μm or less).
Method for measuring alkali content:
The alkali contents (%K2O and %Na2O) of these cements were measured by atomic
30 emission spectrometry, method known as ICP–AES (Inductively–Coupled Plasma –
Atomic Emission Spectrometry). The model of the measuring apparatus was a Varian
720–ES, series EL06093608, 2006. To perform this measurement a sample of 2 g of
cement was solubilised in 100 mL demineralised water for 15 minutes then filtered
through two superimposed filter papers e.g. a first of MN640W type and a second of
35 MN640DD type, in a 200 mL flask, then rinsed with demineralised water. 20 mL of
hydrochloric acid were added at a concentration of 1/20 (volume / volume). The flask
11
was completed up to the graduation line of 200 mL by adding demineralised water. This
solution was analysed on the ICP-AES apparatus.
The content of soluble Na2O equivalent was calculated on the basis of the following
formula:
5 ((MNa2O / MK2O)* K2O+Na2O) = Na2Oeq, M being the molar mass of the compounds in
subscript.
EXAMPLES OF EMBODIMENT
The method of the invention was practically applied to prepare cement foams of
formulas I, II, V, VII, VIII, IX, X and XI. Comparative examples III, IV and VI were also
10 carried out to evidence the advantageous aspects of the method of the invention.
Materials:
The cements used were Portland cements originating from different Lafarge cement
plants identified by the name of the place of their location as specified in Table (I).
These cements are standard type cements. The letters “R” and “N” correspond to the
15 definition of standard NF EN 197-1, version April 2012.
Micro A anhydrite is anhydrous calcium sulfate supplied by Anhydrite Minérale
France.
The superplasticizers used were mixtures comprising a polycarboxylate polyoxide
(PCP) produced by Chryso under the name Chrysolab EPB530-017 (Formulas III to X)
20 and Chrysolab EPB530-026 (Formulas I and II). They are based on Premia180
products (for Chrysolab EPB530-017) and Optima203 (for Chrysolab EPB530-026)
and do not contain any anti-foaming agent. The dry extract of Chrysolab EPB530-017
is 48 weight %. The dry extract of Chrysolab EPB530-026 is 58 weight %.
The foaming agents used were derived from animal proteins and were the following:
25 - Propump26 and Propump 40 produced by Propump, the dry extracts thereof being
26 and 34 weight % respectively;
- MAPEAIR L/LA produced by MAPEÏ having a dry extract of 26 weight %;
- Foamcem produced by LASTON having a dry extract of 28 weight %;
- EFA 1500 produced by Edama, having a dry extract of 36 weight %.
30 The water used was tap water.
Equipment used:
Rayneri mixers:
- Mixer of R 602 EV (2003) model supplied by Rayneri. The mixer is composed of a
35 chassis on which drums of 10 to 60 litres are positioned. The 10L drum was
used with a paddle of blade type adapted to the volume of the drum. This paddle
rotates about itself accompanied by planetary movement around the drum shaft.
12
- Turbotest mixer (MEXP–101, model Turbotest 33/300, series N°: 123861)
supplied by Rayneri. It is a mixer with vertical shaft.
Pumps:
- SeepexTM eccentric screw pump of MD 006–24 type, commission N° 244920.
5 - SeepexTM eccentric screw pump of MD 006–24 type commission N° 278702.
Foamer:
- Foamer composed of a bed of glass beads of SB30 type having a diameter of
between 0.8 and 1.4 mm, packed in a tube of length 100 mm and diameter 12
mm.
10 Static mixer:
- A static mixer composed of 32 helical elements of Kenics type, diameter 19 mm,
reference 16La632 by ISOJET
In the following examples mineral foams were prepared. Each cement slurry is
15 referenced with a number from I to XI and each aqueous foam carries a number from 1
to 6. The cement foam obtained (or mineral foam of the invention) is a combination of
one of these cement slurries with one of these aqueous foams.
I. Preparation of mineral foams
20 I.1 Preparation of a cement slurry
The chemical compositions of the different cement slurries used to carry out the
invention are given in Table I. The slurries were prepared using the Rayneri R 602 EV
mixer by previously loading the solid components (cement) then gradually adding water
and the admixture. The slurry was then mixed for two additional minutes.
25
Table (I): Formulation of the cement slurries
type of cement
Lafarge plant
x (% soluble Na2O–eq)
cement (weight %)
Formulas
I
CEM I
52.5 N
Le Havre
0.22
78.80
II
CEM I
52.5 R
Le Teil
0.14
77.54
III
CEM I
52.5 R
La Malle
0.78
77.30
IV
CEM I
52,5 R
Port La
Nouvelle
0.54
77.44
V
CEM III /B
42.5 N
La Malle
0.43
77.99
VI
CEM I
52.5 R
Saint
Pierre
La Cour
0.66
76.87
VII
CEM I
52.5 R
Saint
Pierre
La Cour
0.66
68.87
VIII
CEM I
52.5 R
Saint
Pierre
La Cour
0.66
66.56
IX
CEM I
52.5 R
Val
d'Azergue
0.4
66.18
13
water (weight %)
Superplasticizer
(weight %)
W/C ratio (weight)
x / (W/C)
dmax(h/2) / dmin(h/2)
21.20
0.06
0.27
0.759
8.4
22.46
0.08
0.29
0.483
10.5
22.70
0.18
0.29
2.69
13.4
22.56
0.10
0.29
1.862
6.5
22.01
0.13
0.29
1.483
7.2
23.13
0.13
0.28
2.276
6.8
31.13
0.01
0.45
1.467
6.8
33.44
0.00
0.5
1.320
6.8
33.82
0.00
0.51
0.784
10.2
Table (I) cont.
type of cement
Lafarge plant
Cement (weight %)
Addition (weight % )
Micro A anhydrite
(weight %)
Water (weight %)
SP superplasticizer
(weight %)
W/C ratio (weight)
W/L ratio (weight)
x (% soluble Na2O–eq)
x/(W/C)
dmax(h/2) / dmin(h/2)
Formulas
X
CEM I 52.5 R (Blaine = 6340 cm2/g)
Saint Pierre La Cour
16.33
60.33
0.37
22.85
0.12
1.40
0.30
0.61
0.436
18.2
XI
CEM I 52.5 R (Blaine = 9000 cm2/g)
Saint Pierre La Cour
16.15
59.79
0.74
23.15
0.18
1.43
0.30
0.69
0.480
24.5
The values dmax(h/2) and dmin(h/2) were measued as described above, with reference to
Figure 1.
5
The results are generally visualised in graph form such as the graph given in
Figure 1 illustrating a typical particle distribution by volume. The height h is the height of
the highest peak measured by laser particle size measurement (Figure 1). Taking a
height h/2 as reference, dmax(h/2) and dmin(h/2) are respectively defined as the size of the
14
largest particles and the size of the smallest particles of distribution in a proportion
equal to h/2.
I.2 Preparation of the aqueous foam
5 An aqueous solution containing the foaming agent was placed in a buffer vessel. The
composition of his aqueous solution of foaming agent (in particular the concentration
and type of foaming agent) is given in Table II. The solution of foaming agent was
pumped through the volumetric eccentric screw pump SeepexTM MD 006–24
(commission N° 278702).
10 This solution of foaming agent was passed through the bed of beads of the foamer
together with pressurised air (range 1 to 6 bars) using a T junction. The aqueous foam
was continuously generated at the flow rate indicated in Table II.
Table II: formulation of aqueous foams and flow rate
Aqueous foam
number
Foaming agent
Concentration
(%liq./water)
Concentration
(%dry/water)
Air flow rate
(L/min)
Solution flow rate
(L/min)
1
Propump 26
4.5
1.17
8
0.41
2
Propump 40
3
1.02
8
0.418
3
MapeAIR L/LA
2.5
0.65
8
0.41
4
Foamcem
3
0.84
8
0.41
15 I.3 Preparation of a slurry of foamed cement:
The previously obtained cement slurry was poured into a buffer vessel held under
agitation by means of a Turbotest Rayneri mixer (MEXP–101) comprising a
deflocculating blade (blade adjustable from 1000 rpm to 400 rpm as a function of slurry
volume). The slurry was pumped using a volumetric eccentric screw pump (SeepexTM
20 MD 006–24, commission N°: 244920).
The pumped slurry and the preceding, continuously generated aqueous foam were
placed in contact in the static mixer paying heed to the flow rates specified in Table II.
The volume of cement slurry used was about 33 L/m3 and the volume of aqueous foam
about 967 L/m3. The slurry of foamed cement was thus generated.
25
I.4 Obtaining a mineral foam
The slurry of foamed cement was cast into polystyrene cubes having sides of
10x10x10cm and into cylindrical columns of height 2.50 m and diameter of 20 cm.
Three cubes were prepared for each foamed slurry. The cubes were released from the
15
5
EFA1500
1.5
0.54
8
0.418
6
Propump26
3.5
0.91
8
0.418
could after 1 day and stored 7 days at 100 % relative humidity and 20°C. The cubes
were then dried to constant weight at 45°C. A column was formed with some of the
foamed slurries. The columns were released from the mould between 3 and 7 days
later and cut into sections of length 25 cm. The sections were dried at 45°C to constant
5 weight.
II. Analysis of the mineral foam
II. 1 Stability of the mineral foam
The stability of the foams was simply measured by visual inspection of the generated
10 cubes before mould release. A foam was described as being “stable” if the cube under
consideration had maintained a height of 10cm after setting. A foam was characterized
as being “unstable” if the cube under consideration had collapsed when setting. Each
test was performed on 3 cubes of 10*10*10 cm. The results show similar behaviour
between the 3 cubes. When applicable, the results expressed are the mean of these 3
15 cubes.
A column was considered stable if the difference in density between the bottom
section and the top section of the column did not exceed 5 kg/m3.
11.2 Thermal conductivity of the mineral foams
20 Thermal conductivity was measured using thermal conductivity measuring
apparatus: TC-meter supplied by Alphis-ERE (Resistance 5 , wire probe 50 mm).
Measurement was performed on samples dried at 45°C to constant weight. The sample
was then sawn into two pieces of equal size. The measuring probe was placed between
the two planar surfaces of these two sample halves (sawn sides). Heat was transmitted
25 from the source to the thermocouple through the material surrounding the probe. The
temperature rise of the thermocouple was measured as a function of time and allowed
calculation of the thermal conductivity of the sample.
11.3 Density of the mineral foams
30 The wet density of the slurries of foamed cement was measured by weighing the
cubes at the time of casting.
The dry density of the samples was measured on the dry samples dried at 45°C to
constant weight, again by weighing of the cubes.
35 II.4 Results
The results are given in Tables III and IV below,
16
Table (III): Analyses of mineral foams with the Propump26 foaming agent
Aqueous foam formula
Slurry formula
Wet density of foamed
slurry (g/l)
Dry density (g/l)
Stability (cube)
Stability
(column)
Lambda (w/k.m – TC
meter measurement)
1
I
108
72
Stable
Stable
0.043
1
II
113
71
Stable
Stable
0.044
1
III
112
–
Not
stable
Not
stable
–
1
IV
117
–
Not
stable
Not
stable
–
1
V
114
76
Stable
Not
Measured
Not
Measured
1
VI
112
–
Not
stable
Not
stable
–
1
VII
110
82
Stable
Stable
Not
Measured
1
VIII
113
71
Stable
Not
Measured
Not
Measured
1
IX
112
69
Stable
Stable
Not
Measured
1
X
100
57
Stable
Stable
0.041
1
XI
102
59
Stable
Stable
Not
Measured
Not stable means that the foam collapsed.
5 Table (IV): Analyses of mineral foams with different foaming agents
Aqueous foam formula
Slurry formula
Wet density of foamed slurry
(g/l)
Dry density (g/l)
Stability (cube)
Stability
(column)
Lambda (w/k.m – TC meter
measurement)
2
II
112
73
Stable
Stable
0.043
2
VI
118
–
Not
Stable
Not
Stable
–
3
II
105
69
Stable
Stable
0.042
3
VI
109
–
Not
stable
Not
stable
–
4
II
104
68
Stable
Stable
0.043
4
VI
112
–
Not
stable
Not
stable
–
5
II
117
76
Stable
Stable
Not
Measured
5
VI
111
–
Not
stable
Not
stable
–
6
II
106
69
Stable
Stable
0.043
6
VI
109
–
Not
stable
Not
stable
–
Not stable means that the foam collapsed.
II.5 Conclusions
These examples allow assessment of the role played by the soluble alkali equivalent
10 in the stability of a cement foam. If the alkalinity content is held at a low level through
the use of a low alkali cement, or if the ratio x / (W/C) is lower than 1.75, the foam is
stable. When the alkali content increases, the foam becomes destabilised and
17
collapses. It can be noted that the type of clinker used does not have any influence on
the stability of the foam. For example, the clinker contained in the cement of slurry
formula III (comparative) and V (of the invention) have the same origin. However, the
soluble alkali equivalent of the cement used in formula V is strongly reduced through
5 the addition of slag. This dilution allows obtaining of the desired stability.
The invention is not limited to the embodiments presented and other embodiments
will be clearly apparent to persons skilled in the art.
18
I/We Claim:
1. Method for producing a mineral foam comprising the following steps:
(i) independently preparing a cement slurry and an aqueous foam, the
cement slurry being prepared by mixing water W and cement C, the cement C
comprising an amount x of soluble Na20 equivalent, x being expressed in weight per
100 parts of cement, said slurry having a ratio x / (W/C) less than or equal to 1.75,
with W/C expressed by weight, and the particles of cement C have a particle size
distribution such that the ratio dmaX(h/2)/dmin(h/2) of the particle size distribution is
between 5 and 25;
(ii) contacting the cement slurry with the aqueous foam to obtain a slurry of
foamed cement; and
(iii) forming the slurry of foamed cement obtained at step (ii) and leaving to
set.
2. The method according to claim 1, wherein the ratio x / (W/C) is less than or equal
to 1.60, preferably less than or equal to 1.50.
3. The method according to claim 1 or 2, wherein the ratio dmax(h/2)/dmin(h/2) is from 6 to
14.
4. The method according to any one of the preceding claims, wherein the cement is
a cement of type CEM I, CEM II, CEM III, CEM IVorCEM V.
5. The method according to any one of the preceding claims, wherein the cement
has a Blaine specific surface area of 3 500 to 10 000 cm2/g.
6. The method according to any one of the preceding claims, wherein the cement
slurry comprises a water reducing agent of plasticizer or superplasticizer type.
7. The method according to any one of the preceding claims, wherein the mineral
foam comprises a mineral addition.
8. The method according to any one of the preceding claims, wherein the mineral
foam contains substantially no fine particles.
9. The method according to any one of the preceding claims, wherein the W/C
weight ratio of the cement slurry ranges from 0.23 to 2.0.
10. The method according to any one of the preceding claims, wherein the aqueous
foam comprises water and a foaming agent.
11. A mineral foam obtainable using the method according to any one of claims 1 to
10.
12. The foam according to claim 11, characterized in that it has a dry density of 30 to
300 kg/m3.
13. The foam according to claim 11 or 12, characterized in that it has thermal
conductivity of 0.030 to 0.150 VW(m.K).
14. A construction element comprising a mineral foam according to one of claims 11
to 13.
15. Use of the mineral foam according to one of claims 11 to 13 as insulating material,
in particular as thermal or sound insulation.