Patent Application
20250051240
The present invention concerns a method for reducing the thermal conductivity of mineral foam.
Mineral foams are used in many technological applications. Due to their low thermal conductivity, good heat and fire resistance, and acoustic properties, this type of material is suitable for insulation applications in building construction and renovation.
A mineral foam is a concrete material in the form of foam. This material is generally more lightweight than typical concrete due to its pores or empty spaces. These pores or empty spaces are due to the presence of air in the mineral foam and they may be in the form of bubbles. An ultra-light foam is understood to be a foam generally having a density in its dry state of between 20 and 300 kg/m3.
Mineral foam can be produced by mixing two liquid components, i.e. a cement slurry and a liquid containing a gas-forming agent, to obtain a foaming slurry which expands to form a foamed slurry and then sets and hardens to become said mineral foam. The expansion is the direct consequence of the formation of bubbles upon mixing of the two liquids.
Mineral foam may collapse due to a lack of stability in the mineral foam before setting. These collapse problems of the foam may be due to coalescence phenomena, to Ostwald ripening phenomena, to hydrostatic pressure or to draining phenomena, the latter being greater in particular in case of elements of important height. The difficulty in the production of mineral foams is therefore to produce stable mineral foam which reduces these collapse problems. Examples of stable mineral foams are disclosed in the following applications: WO2016/102838, WO2019/092090.
Generally, a mineral foam is very advantageous for many applications due to its properties, such as its thermal insulation properties, its acoustic insulation properties, its durability, its resistance to fire and its easy implementation, especially compared to expanded polystyrene foams and other organic foams.
Reducing the thermal conductivity of mineral foam is essential for insulating materials. Reducing by only one milliwatt the thermal conductivity represents better insulation or less material thickness for the same insulation.
There is still a need for stable mineral foams having lower thermal conductivity, especially to be a viable alternative to expanded polystyrene foams, or other organic foams currently used.
The invention is directed to the use of a component A selected from mineral component, sand, wood flour or combinations thereof, for reducing the thermal conductivity of a mineral foam. The mineral foam is produced by a process comprising a step of contacting a cement slurry and a gas-forming liquid. The cement slurry comprises a cement composition, ultrafine particles of which the D50 is comprised from 10 to 600 nm, a transition metal salt and water, the cement composition comprising Portland clinker and the component A. The gas-forming liquid comprises a gas-forming agent.
The mineral component is preferably selected from slag, pozzolanic materials, fly ash, calcined schists, material containing calcium carbonate for example limestone, silica fume, siliceous component, metakaolin and mixtures thereof.
Preferably, the sand is composed of particles that have a size greater than 0 mm to 2 mm, preferably greater than 0 mm to 0.5 mm.
Preferably, the wood flour is composed of wood particles that have a D50 comprised between 0.1 μm to 200 μm.
Preferably, the cement composition of the cement slurry comprises more than 25 wt.-%, preferably at least 30 wt.-%, more preferably at least 40 wt.-%, even more preferably at least 52 wt.-% of component A, compared to the total weight of the cement composition.
Component A preferably comprises material containing calcium carbonate, for example limestone, and at least one further component selected from sand, wood flour, a mineral addition different from material containing calcium carbonate, and combinations thereof.
Preferably, the cement composition of the cement slurry comprises 10 to 40 wt.-% of limestone, compared to the total weight of cement composition.
Preferably, the cement composition of the cement slurry comprises 10 to 30 wt.-% of limestone and from 20 to 60 wt.-% of slag, compared to the total weight of cement composition.
Preferably, the cement composition of the cement slurry comprises 21 to 30 wt.-% of limestone and from 5 to 10 wt.-% of silica fume, compared to the total weight of cement composition.
Preferably, the cement composition of the cement slurry comprises 10 to 30 wt.-% of limestone, from 20 to 60 wt.-% of slag, and from 5 to 10 wt.-% of silica fume, compared to the total weight of cement composition.
Preferably, the cement composition of the cement slurry comprises 10 to 30 wt.-% of limestone and from 20 to 40 wt.-% of sand, compared to the total weight of cement composition.
Preferably, the cement composition of the cement slurry comprises from 5 to 15 wt.-% of limestone and from 0.5 to 3 wt.-% of wood flour, compared to the total weight of cement composition.
In the cement slurry, water/cement mass ratio preferably ranges from 0.25 to 0.7, preferably from 0.28 to 0.6, more preferably from 0.29 to 0.45; mineral addition and/or sand and/or wood flour, ultrafine particles and cement are compatibilized as “cement” for the determination of water/cement mass ratio.
The mineral foam can be produced by a process comprising the following steps:
Preferably, the dry mineral foam has a dry density ranging from 50 to 180 kg/m3, more preferentially from 50 to 170 kg/m3, even more preferentially from 80 to 130 kg/m3.
The dry mineral foam has preferably a thermal conductivity ranging:
The invention is also directed to a method for manufacturing a mineral foam comprising the following steps:
The above and other objects, features and advantages of this invention will be apparent in the following detailed description of an illustrative embodiment thereof, with is to be read in connection with the accompanying drawing wherein:
Cement: cement is Portland cement. Portland cement comprises Portland clinker and usually calcium sulphate, and is preferably a Portland cement as defined in the standard NF-EN-197-1 of April 2012. The cements defined in standard NF-EN197-1 of April 2012 are grouped in 5 different families: CEM I, CEM II, CEM III, CEM IV and CEM V. In the present invention, the Portland cement is preferably chosen from the families CEM II, CEM III, CEM IV and CEM V. Alternatively, the Portland cement can be a CEM I, CEM II, CEM III, CEM IV or CEM V to which mineral components are added prior to preparing the cement slurry or during preparation of the cement slurry. The cement may optionally further contain less than 10 wt.-% of a calcium aluminate cement or a calcium sulfoaluminate cement, compared to the total weight of the cement, if shorter setting times and higher early age strength development are for example required.
Thus, when % are expressed in weight compared to the weight of cement, unless specified otherwise, the term cement includes the mineral component.
Calcium sulphate used according to the present invention includes gypsum (calcium sulphate dihydrate, CaSO4·2H2O), hemi-hydrate (CaSO4·½H2O), anhydrite (anhydrous calcium sulphate, CaSO4) or a mixture thereof. Calcium sulphate produced as a by-product of certain industrial processes may also be used. Preferably, the calcium sulphate content ranges from 0% to 5% by weight of the cement, more preferably from 0.2% to 5% by weight of the cement composition.
Mineral component: The mineral component comprises one or at least one of the following components: slag (as defined in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.2), pozzolanic materials (as defined in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.3), fly ash (as described in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.4), calcined schists (as described in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.5), material containing calcium carbonate, for example limestone (as defined in the European NF EN 197-1 Standard paragraph 5.2.6), limestone components (as defined in the “Concrete” NF P 18-508 Standard), silica fume (as defined in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.7), siliceous components (as defined in the “Concrete” NF P 18-509 Standard), ground steel slag, electric arc slag, metakaolin, or mixtures thereof.
Cement composition: composition comprising Portland clinker, calcium sulphate and a component A selected from mineral component, sand, wood flour or combinations thereof. When component A is mineral component, the cement composition is cement as defined above and the expression ‘cement’ and ‘cement composition’ can be used interchangeably.
Wood flour: powder made of ground wood particles
Cement slurry: The expression “cement slurry” designates a mixture comprising water and cement composition. That cement slurry may also comprise additional components, as disclosed below.
Gas-forming liquid: The expression “gas-forming liquid” designates a composition comprising a gas-forming agent. The gas-forming agent is preferably selected from hydrogen peroxide, peroxomonosulphuric acid, peroxodisulfphuric acid, alkaline peroxides, alkaline earth peroxides, organic peroxide, particles of aluminium, or mixtures thereof.
D50: The D50, also noted Dv50, corresponds to the 50th percentile of the volume distribution of the size of particles, that is to say that 50% of the volume is constituted of particles of which the size is less than the D50 and 50% of size greater than the D50. The D50 can be measured by a laser particle size method as further described below.
It was discovered that substituting part of the Portland clinker with a mineral component, sand and/or a wood flour in a mineral foam reduces the thermal conductivity of the mineral foam. It has been discovered that at equal dry density of the mineral foam, thermal conductivity of the mineral foam decreases with increasing the substitution of Portland clinker with a mineral component and/or with sand and/or with wood flour. Surprisingly, the crystalline or amorphous nature of the mineral component and/or sand and/or wood flour has no or little effect on the thermal conductivity of the foam. On the contrary, increasing the amount of mineral component and/or sand and/or wood flour in the cement composition significatively impacts the thermal conductivity of the mineral foam.
The invention thus relates to the use of a component A selected from mineral component, sand, wood flour and combinations thereof, in a mineral foam comprising Portland clinker for reducing thermal conductivity of the mineral foam.
Specifically, the invention thus relates to the use of a component A, selected from mineral component, sand, wood flour and combinations thereof, in the cement composition used to prepare the cement slurry for reducing thermal conductivity of a mineral foam.
Specifically, the invention thus relates to the use of a component A selected from mineral component, sand, wood flour or combinations thereof, for reducing the thermal conductivity of a mineral foam by substituting part of Portland clinker with component A.
Specifically, the invention thus relates to the use of a component A selected from mineral component, sand, wood flour or combinations thereof, for reducing, at equal dry density of a mineral foam, the thermal conductivity of the mineral foam by substituting part of Portland clinker with component A.
The mineral foam is produced by a process comprising a step of contacting the cement slurry and a gas-forming liquid. The cement slurry comprises a cement composition, ultrafine particles of which the D50 is comprised from 10 to 600 nm, a transition metal salt and water, the cement composition comprising Portland clinker and the component A. The gas-forming liquid comprises a gas-forming agent.
In the invention, the cement composition comprises Portland clinker, component A and optionally calcium sulphate. The cement composition is used to prepare a cement slurry comprising water and the cement composition. The cement composition is preferably the sole source of cement used to prepare the cement slurry.
In the description of the cement composition, the percentages of Portland clinker, component A and other component such as calcium sulphate will be expressed in weight compared to the total weight of the cement composition, i.e. compared to the total weight of Portland clinker, component A and component such as calcium sulphate.
The invention also relates to a method for manufacturing a mineral foam comprising the following steps:
In the present invention, the component A, meaning mineral component and/or sand and/or wood flour, can be added to the cement composition prior or during the preparation of the cement slurry. Commercial cements, especially CEM III cements, can also be used.
Advantageously, the cement has a Blaine specific surface ranging from 3000 to 10000 cm2/g, preferably from 5000 to 8000 cm2/g.
The mineral component used according to the invention may be slag (for example, as defined in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.2), pozzolanic materials (for example as defined in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.3), fly ash (for example, as described in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.4), calcined schists (for example, as described in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.5), material containing calcium carbonate, for example limestone (for example, as defined in the European NF EN 197-1 Standard paragraph 5.2.6), limestone components (for example, as defined in the “Concrete” NF P 18-508 Standard), silica fume (for example, as defined in the European NF EN 197-1 Standard of April 2012, paragraph 5.2.7), siliceous components (for example, as defined in the “Concrete” NF P 18-509 Standard), metakaolin or mixtures thereof.
Examples of siliceous components are ground glass, solid or hollow glass beads, glass granules, expanded glass powder.
Fly ash is generally pulverulent particles comprised in fume from thermal power plants which are fed with coal. Fly ash is generally recovered by electrostatic or mechanical precipitation. Slag is generally obtained by rapid cooling of molten slag resulting from melting of iron ore in a furnace. Ground granulated blast furnace slag is generally used. Slag can also be obtained by electric arc furnaces, and such slags are a non-metallic by-product that consists mainly of silicates and oxides formed during the process of refining the molten steel. The feed materials for electric arc furnace slags are mainly steel scrap and pig iron.
Silica fume may be a material obtained by the reduction of very pure quality quartz by the coal in electric arc furnaces used for the production of silicon and alloys of ferrosilicon. Silica fume is generally formed of spherical particles comprising at least 85% by weight of amorphous silica.
The pozzolanic materials may be natural siliceous and/or silico-aluminous materials or a combination thereof. Among the pozzolanic materials, natural pozzolans can be mentioned, which are generally materials of volcanic origin or sedimentary rocks, and natural calcined pozzolans, which are materials of volcanic origin, clays, shale or thermally-activated sedimentary rocks.
Sand is preferably a siliceous sand or a siliceous-calcareous sand.
Sand is preferably composed of particles that have a size greater than 0 mm to 2 mm (noted 0/2), preferably greater than 0 mm to 0.5 mm (noted 0/0.5) or greater than 0 mm to 1.6 mm (noted 0/1.6).
Wood flour is advantageously composed of powdered wood particles that have a D50 generally comprised between 0.1 to 200 μm, preferably from 0.1 to 150 μm, more preferably from 1 μm and 100 μm.
All mineral components except silica fume are advantageously composed of particles that have a D50 generally comprised between 0.1 to 200 μm, preferably from 0.1 to 150 μm, more preferably from 1 μm and 100 μm.
Slag is preferably ground granulated blast furnace slag. Preferably, ground granulated blast furnace slag has a Blaine specific surface ranging from 2000 to 6000 cm2/g, preferably from 3000 to 5000 cm2/g.
Silica fume comprises particles that have a D50 between 0.05 and 100 μm, preferably between 0.05 and 1 μm.
Preferably, the cement composition of the cement slurry comprises more than 25 wt.-%, preferably at least 30 wt.-%, more preferably at least 40 wt.-%, even more preferably at least 52 wt.-% of component A, the percentages are expressed in weight compared to the total weight of cement composition.
Preferably, the cement composition of the cement slurry comprises up to 85 wt.-% of component A, advantageously up to 80 wt.-% of component A or up to 70 wt.-% of component A, the percentages are expressed in weight compared to the total weight of cement composition.
As shown in examples, especially in
Preferably, the component A comprises material containing calcium carbonate, for example limestone, and at least one further component selected from sand, wood flour, a mineral addition different from material containing calcium carbonate, and combinations thereof.
The cement composition of the cement slurry advantageously comprises 10 to 40 wt.-%, preferably 20 to 40 wt.-%, of material containing calcium carbonate, in particular limestone, compared to the total weight of cement composition.
Preferably the material containing calcium carbonate, for example limestone, is composed of particles that have a D50 generally comprised between 0.05 μm to 200 μm, preferably from 0.05 μm to 100 μm, more preferably from 0.1 μm to 10 μm.
Preferably, the component A is selected from mixtures of slag and limestone. The cement composition of the cement slurry advantageously comprises 10 to 30 wt.-% of limestone and at least 20 wt.-% of slag, preferably from 20 to 60 wt.-% of slag, compared to the total weight of cement composition.
Preferably, the component A is selected from mixtures of silica fume and limestone. The cement composition of the cement slurry advantageously comprises 21 to 30 wt.-% of limestone and at least 5 wt.-% of silica fume, preferably from 5 to 10 wt.-% of silica fume, compared to the total weight of cement composition.
Preferably, the component A is selected from mixtures of slag, silica fume and limestone. The cement composition of the cement slurry advantageously comprises 10 to 30 wt.-% of limestone, at least 20 wt.-% of slag, preferably from 20 to 60 wt.-% of slag, and at least 5 wt.-% of silica fume, preferably from 5 to 10 wt.-% of silica fume, compared to the total weight of cement composition.
Preferably, the component A is selected from mixtures of sand and limestone. The cement composition of the cement slurry advantageously comprises 10 to 30 wt.-% of limestone and at least 20 wt.-% of sand, preferably from 20 to 40 wt.-% of sand, preferably from 20 to 34 wt.-% of sand compared to the total weight of cement composition.
Preferably, the component A is selected from mixtures of sand, limestone and slag. The cement composition of the cement slurry advantageously comprises 10 to 30 wt.-% of limestone, at least 20 wt.-% of sand, preferably from 20 to 40 wt.-% of sand, preferably from 20 to 34 wt.-% of sand and at least 20% wt.-% of slag, preferably from 20 to 60 wt.-% of slag compared to the total weight of cement composition.
Preferably, the component A is selected from mixtures of wood flour and limestone.
The cement composition of the cement slurry advantageously comprises 0 to 15 wt.-% of limestone, preferably from 5 to 15 wt.-% of limestone, and at least 0.5 wt.-% of wood flour, preferably from 0.5 wt.-% to 10 wt.-% of wood flour, preferably from 0.5 wt.-% to 5 wt.-% of wood flour, preferably from 0.5 wt.-% to 3 wt.-%, preferably from 1 to 3 wt.-% of wood flour, compared to the total weight of cement composition.
Preferably, the component A is selected from mixtures of wood flour, limestone and slag.
The cement composition of the cement slurry advantageously comprises 0 to 15 wt.-% of limestone, preferably from 5 to 15 wt.-% of limestone, at least 0.5 wt.-% of wood flour, preferably from 0.5 wt.-% to 10 wt.-% of wood flour, preferably from 0.5 wt.-% to 5 wt.-% of wood flour, preferably from 0.5 wt.-% to 3 wt.-%, preferably from 1 to 3 wt.-% of wood flour, and at least 20% wt.-% of slag preferably from 20 to 60 wt.-% of slag compared to the total weight of cement composition.
The cement slurry will typically further comprise:
The cement slurry does not comprise other cement or mineral addition than the components disclosed above in the description of the cement composition.
Advantageously, the cement slurry comprises from 0.5 to 10 wt. %, preferably from 1 to 7 wt. % of ultrafine particles compared to the total weight of cement slurry.
Advantageously, the ultrafine particles are as disclosed in WO2016/102838 or in WO2019/092090. In particular the ultrafine particles satisfy one or all of the following conditions:
It may be noted that the ultrafine particles generally comprise elementary particles having a diameter comprised from 10 to 50 nm. These elementary particles may agglomerate to form agglomerated particles having a diameter from 40 nm to 150 nm. These agglomerated particles may agglomerate to form aggregates having a diameter from 100 nm to 600 nm.
The water reducing agent is preferably a superplasticizer, such as PCP. The term “PCP” or “polyoxy polycarboxylate” is to be understood according to the present invention as a comb polymer comprising a backbone derived from acrylic acids and/or methacrylic acids bearing pending esters of polyoxyethylene (POE).
Preferably, the cement slurry of the present invention comprises from 0 to 2.0 wt. %, more preferentially from 0.05 to 1 wt. %, of a water reducing agent (dry content) compared to the total weight of the cement.
Preferably, the cement slurry does not comprise an anti-foaming agent, or any agent having the property of destabilizing an air/liquid emulsion. Certain commercial super-plasticisers may contain anti-foaming agents and consequently these super-plasticisers are not suitable for the cement slurry used to produce the mineral foam according to the invention.
Fibres can be polypropylene fibres.
Advantageously, the amount of fibres is between 0.2 wt. % and 2 wt. % by weight of cement, preferentially 0.2 wt. % and 1 wt. %.
The water/binder mass ratio of the cement slurry is preferably from 0.25 to 0.7, more preferably from 0.28 to 0.6, even more preferably from 0.29 to 0.45. The binder is composed of mineral addition and/or sand and/or wood flour, ultrafine particles and cement.
Advantageously, the mineral foam is produced by a process comprising the following steps:
Advantageously, the process is as disclosed in WO2016/102838 or in WO2019/092090 with further substitution of part of Portland clinker with component A.
In a preferred embodiment, the cement slurry is prepared by first blending a premix of cement, ultrafine particles and optionally component A. When component A comprises mineral addition, the mineral addition is preferably added to the premix. When component A comprises sand and/or wood flour, the sand and/or wood flour is added to the premix or later on when mixing premix and water. Preferably, the premix is constituted of all the solid constituents except the fibres of the cement slurry of the invention.
The cement slurry is then obtained by adding the premix to water comprising transition metal salt, and optionally water reducing agent. Component A, if not present in the premix, can be added during mixing. In particular, sand and/or wood flour can be added during mixing. Optionally fibres are subsequently added.
Advantageously, the gas-forming liquid is as disclosed in WO2016/102838 or in WO2019/092090. In particular the gas-forming liquid satisfy one or all of the following conditions:
To achieve this desired density, the weight ratio between the cement slurry and the gas-forming liquid is adjusted as done for mineral foam based on CEM I. Surprisingly, for a same density, the thermal conductivity decreases when the content of mineral component increases, the mineral component replacing part of the Portland clinker.
Thermal conductivity (also known as lambda (λ)) is a physical magnitude characterizing the behavior 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 under a temperature gradient. In the international unit system, thermal conductivity is expressed in watts per meter Kelvin (W·m−1·K−1).
The mineral foam obtained has preferably one or many of the following features:
The method has preferably one or more of the following characteristics:
The mineral foam provided by the instant invention has preferably one or more of the following characteristics:
Surprisingly, the quantity of Portland clinker is lowered but the mechanical resistance of the mineral foam does not sharply decrease.
The presence of mineral components makes it possible to obtain homogeneous, regular foam. The quantity of CSH (cement hydrates) decreases and the thermal conductivity is improved without degrading proportionally the other properties of the mineral foam: stability, mechanical strength, . . . .
The combined use of material containing calcium carbonate and at least another mineral component and/or sand and/or wood flour in a mineral foam is also new as such. Accordingly, the invention is also directed to mineral foam obtained by a process comprising a step of contacting a cement slurry and a gas-forming liquid, wherein:
The mineral component, the sand, the wood flour and the material containing calcium carbonate, for example limestone, are as defined above and their content in the cement slurry are as defined above. When silica fume is present, its content is preferably less than 20 wt.-% compare to the total weight of the cement. The component can in particular be selected from slag, silica fume, sand, wood flour and combinations thereof. The cement slurry and the foamed cement slurry can further comprise the components disclosed above. The mineral foam provided by the instant invention has one or more of the characteristics described above.
The following examples illustrate the invention.
The measuring methods used are now detailed below.
The method disclosed in WO2019/092090 is implemented.
In this specification, including the accompanying claims, particle size distributions and particle sizes are as measured using a laser granulometer of the type Mastersize 2000 (year 2008, series MAL1020429) sold by the company Malvern.
Measurement is carried out in an appropriate medium (for example an aqueous medium for non-reactive particles, or alcohol for reactive material) in order to disperse the particles. The particle size shall be in the range of 1 μm to 2 mm. The light source consists of a red He—Ne laser (632 nm) and a blue diode (466 nm). The optical model is that of Frauenhofer and the calculation matrix is of the polydisperse type. A background noise measurement is effected with a pump speed of 2000 rpm, a stirrer speed of 800 rpm and a noise measurement for 10 s, in absence of ultrasound. It is verified that the luminous intensity of the laser is at least equal to 80% and that a decreasing exponential curve is obtained for the background noise. If this is not the case, the cell's lenses have to be cleaned.
Subsequently, a first measurement is performed on the sample with the following parameters: pump speed 2000 rpm and stirrer speed 800 rpm. The sample is introduced in order to establish an obscuration between 10 and 20%. After stabilisation of the obscuration, the measurement is carried out with a duration between the immersion and the measurement being fixed to 10 s. The duration of the measurement is 30 s (30000 analysed diffraction images). In the obtained granulogram one has to take into account that a portion of the powder may be agglomerated.
Subsequently, a second measurement is carried out (without emptying the receptacle) with ultrasound. The pump speed is set to 2500 rpm, the stirrer speed is set to 1000 rpm, the ultrasound is emitted at 100% (30 watts). This setting is maintained for 3 minutes, afterwards the initial settings are resumed: pump speed at 2000 rpm, stirrer speed at 800 rpm, no ultrasound. At the end of 10 s (for possible air bubbles to clear), a measurement is carried out for 30 s (30000 analysed images). This second measurement corresponds to a powder desagglomerated by an ultrasonic dispersion.
Each measurement is repeated at least twice to verify the stability of the result.
The specific surface of the various materials is measured as follows. The Blaine method is used at a temperature of 20° C. with a relative humidity not exceeding 65%, wherein a Blaine apparatus Euromatest Sintco conforming to the European Standard EN 196-6 is used.
Prior to the measurement the humid samples are dried in a drying chamber to obtain a constant weight at a temperature of 50-150° C. The dried product is then ground in order to obtain a powder having a maximum particle size of less than or equal to 80 μm.
To measure thermal conductivity, two measuring devices are used: The CT-meter and the guarded hot plate.
Thermal conductivity was measured using a thermal conductivity measuring device: the CT-metre (Resistance 5Ω, probe wire 50 mm). The samples were dried in a drying oven at 45° C. until their weight remained constant. The sample was then cut into two equal pieces using a saw. The measurement probe was placed between the two flat sides of these two half samples (the sawed sides). Heat was transmitted from the source towards the thermocouple through the material surrounding the probe. The rise in temperature of the thermocouple was measured over time and the thermal conductivity of the sample was calculated.
Thermal conductivity was measured using a thermal conductivity measuring device: the guarded hot plate, TAURUS TLP 500 GX-1. The measurement has been validated for samples whose thermal conductivity is between 0.0295 and 0.6 W/(m·K) and whose compressive strength on the sample surface is greater than 200N. The samples were dried in a drying oven at 45° C. and 10% relative humidity, until their weight remained constant (difference less than 0.1 kg/m3/24 h)
The sample is placed between two contact plates containing the thermocouples and the cold faces and the hot faces are applied with a precharge of 125 N. For density less than 60 kg/m3 the preload is 62.5 N. The heat flux between hot plate and cold plate is measured at 10° C., 20° C. and 30° C. Thermal conductivity is calculated at 10° C. by linear regression from measurements at target average temperatures of 10° C., 20° C., 30° C.
The cement used is selected from:
The component A comprises:
Particles of precipitated calcium carbonate sold under the name Socal 312 and supplied by Imerys. These ultrafine particles have a contact angle varying from 90° to 130° as measured according to the method described above and a D50 of the particles of 40 nm as measured with the method described in the document EP1 740 649. These ultrafine particles are coated with stearine.
The gas forming liquid is prepared by mixing the components of the table 1 into the respective proportions given in the table.
The following mineral foams have been prepared:
The cement slurry is prepared by mixing the components of the table 2 into the respective proportions given in the table.
The cement slurry of table 2 is mixed with the gas forming liquid of table 1, with different mass ratio depending on the targeted density.
Resulting foams have the following features:
The cement slurry is prepared by mixing the components of the table 4 into the respective proportions given in the table.
The cement slurry of table 4 is mixed with the gas forming liquid of table 1, with different mass ratio depending on the targeted density.
Resulting foam has the following features:
The cement slurry is prepared by mixing the components of the table 6 into the respective proportions given in the table.
The cement slurry of table 6 is mixed with the gas forming liquid of table 1, with different mass ratio depending on the targeted density.
Resulting foam has the following features:
Inventive Mineral Foam No. 3; with Silica Fume in Addition to Limestone
The cement slurry is prepared by mixing the components of the table 8 into the respective proportions given in the table.
The cement slurry of table 8 is mixed with the gas forming liquid of table 1, with different mass ratio depending on the targeted density.
Resulting foams have the following features:
The cement slurry is prepared by mixing the components of the table 10 into the respective proportions given in the table.
The cement slurry of table 10 is mixed with the gas forming liquid of table 1, with different mass ratio depending on the targeted density.
Resulting foam has the following features:
The cement slurry is prepared by mixing the components of the table 12 into the respective proportions given in the table.
The cement slurry of table 12 is mixed with the gas forming liquid of table 1, with different mass ratio depending on the targeted density.
Resulting foam has the following features:
Thermal conductivity values of reference and inventive mineral foams in function of the dry density are reported on
In
| Number | Date | Country | Kind |
|---|---|---|---|
| 21306862.0 | Dec 2021 | EP | regional |
| 22305853.8 | Jun 2022 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2022/086470 | 12/16/2022 | WO |
