The present invention relates to a cement admixture used in the civil engineering field, the construction field, etc., a method for producing the cement admixture, and a cement composition.
Concrete used in architectural structures such as high-rise buildings and civil engineering structures such as tunnels is required to have fire resistance performance. Adding organic fibers is said to be an effective for improving the fire resistance performance of concrete. This is a technology that prevents the concrete from exploding by vaporizing organic fibers through combustion, creating numerous cavities, and creating cracks between the cavities, creating a path for water vapor generated from the concrete structure to escape to the outside (Patent Literatures 1, 2, 3).
On the other hand, since concrete uses a large amount of cement as a raw material, it is said to be a material that emits a large amount of CO2. This is mainly due to the fact that in the cement production process, a large amount of fossil fuel is used to obtain combustion energy for the furnace, and in addition, a decarboxylation reaction of limestone (CaCO3→CaO+CO2) occurs. Reducing CO2 emissions from concrete has become an important theme as part of global warming countermeasures.
In order to reduce the total amount of CO2 emitted when producing concrete products, it is effective that the used amount of cement can be reduced by incorporating large amounts of industrial by-products (pulverized blast furnace slag, fly ash, etc.) as cement substitutes, and various studies are underway.
In addition, a technique is known for obtaining highly durable concrete products having densified surface layers from CO2 absorption, by forcibly performing a carbonation (salt) curing of concrete blended with non-hydraulic compounds such as γ-C2S (γ-2CaO·SiO2; also called belite γ phase) as an admixture (for example, Patent Literature 3). γ-C2S does not undergo hydration reaction, but reacts with CO2 to produce gels rich in CaCO3 and SiO2. These products fill the voids in the cement matrix and dramatically improve the durability of the surface layer of the concrete product. In this case, the total CO2 emissions in obtaining the concrete product are reduced by the amount of CO2 absorbed by the concrete during carbonation (salt) curing (Patent Literatures 4 and 5).
In the techniques described in the above Patent Literatures 1 to 3, when the temperature rises rapidly, path formation due to fiber combustion may not be completed in time, and explosion may occur. In addition, since conventional fireproof concrete contains organic fibers, there is a possibility that toxic gases such as carbon monoxide may be generated depending on the combustion conditions, and it can also be considered that if a fire breaks out in a closed space, the damage may spread.
In addition, in highly durable concrete blended with a non-hydraulic compound such as γ-C2S shown in Patent Literature 4, it is assumed that the structure to be cured is placed in a shielded space that can maintain a predetermined carbon dioxide concentration. Therefore, in order to make a huge concrete structure that cannot be accommodated in a curing facility to be cured, a cement admixture that can accelerate the carbonation (salt) of the blended non-hydraulic compound is required.
The present invention is to provide a cement admixture which has excellent fire resistance that does not generate toxic gas even when exposed to high temperatures due to fire, etc., and has an excellent retained ratio of compressive strength and a retained ratio of Young's modulus after the reception of heat, and excellent carbonation resistance after the reception of heat.
As a result of intensive research to solve the above problems, the present inventors discovered that a cement admixture containing a dicalcium silicate compound having a specific shape could solve the above problems, and completed the present invention. That is, the present invention is as follows.
[1]A cement admixture containing a dicalcium silicate compound having an average particle diameter of 5 to 100 μm as measured by microscopic observation and also having an average aspect ratio represented by (major axis diameter/minor axis diameter) of 1.3 or more.
[2] The cement admixture according to the above item [1], in which the dicalcium silicate compound has an average value of circularity expressed by (4×circumference ratio π×area/(square of circumferential length)) of 0.8 or less.
[3] The cement admixture according to the above item [1] or [2], in which the chemical composition is 44 to 75 parts by mass of CaO, 18 to 55 parts by mass of SiO2, 1 to 3 parts by mass of Al2O3, 0 to 5 parts by mass of MgO, and 0 to 2 parts by mass of SO3, with respect to 100 parts by mass of the total of CaO, SiO2, Al2O3, MgO, and SO3, and in which a Blaine specific surface area value is 2,000 to 6,000 cm2/g.
[4] The cement admixture according to any one of the above items [1] to [3], further containing 5 parts by mass or less of calcium carbonate with respect to 100 parts by mass of the cement admixture.
[5] The cement admixture according to any one of the above items [1] to [4], furthermore containing slag and/or pozzolanic substances.
[6] The cement admixture according to the above item [5], in which the slag and/or pozzolanic substances have one or more selected from the group consisting of blast furnace slag (air-cooled blast furnace slag, granulated blast furnace slag), steelmaking slag (converter slag, electric furnace slag), fly ash, silica fume, metakaolin, pulp sludge incineration ash, sewage sludge incineration ash, volcanic glass fine powder, and waste glass powder.
[7] The cement admixture according to the above item [5] or [6], in which a mixing ratio of the dicalcium silicate compound and the slag and/or pozzolanic substances is 10/1 to 1/10 in mass ratio.
[8]A method for producing a cement admixture, including adjusting a clinker to have a Blaine specific surface area value of 2,000 to 6,000 cm2/g, the clinker being obtained by blending a raw material containing CaO, a raw material containing SiO2 and a raw material containing SO3 so that the CaO/SiO2 molar ratio is 1.3 to 3.0 and the SO3 content is 0 to 3% by mass, and heat-treated at 1,000° C. or higher and 1,800° C. or lower.
[9]A cement composition containing:
cement; and
the cement admixture according to any one of the above items [1] to [7].
According to the present invention, a cement admixture which has excellent fire resistance, and has an excellent retained ratio of compressive strength and a retained ratio of Young's modulus after the reception of heat, and excellent carbonation resistance after the reception of heat.
Hereinafter, an embodiment of the present invention (the present embodiment) will be described in detail. Note that parts and percentages used in this description are based on mass unless otherwise specified.
The cement admixture according to the present embodiment contains a dicalcium silicate compound.
The dicalcium silicate compound according to the present invention is characterized by having an average particle diameter of 5 to 100 μm and also having an average aspect ratio represented by (major axis diameter/minor axis diameter) of 1.3 or more.
In addition, the dicalcium silicate compound preferably has an average value of circularity (hereinafter referred to as “average circularity”) expressed by (4×circumference ratio π×area/(square of circumferential length)) of 0.8 or less.
As mentioned above, the average particle diameter of the dicalcium silicate (hereinafter sometimes referred to as “DCS”) compound must be in the range of 5 to 100 μm. When the average particle diameter deviates from 5 to 100 μm, the retained ratio of compressive strength tends to decrease significantly with respect to the heating temperature. From the above viewpoint, the average particle diameter of the DCS compound is more preferably in the range of 10 to 90 μm, and still more preferably in the range of 15 to 80 μm.
As mentioned above, the average aspect ratio expressed by (major axis diameter/minor axis diameter) of the dicalcium silicate compound must be 1.3 or more. When the average aspect ratio is smaller than 1.3, the carbonation depth after heating tends to increase. From the above viewpoint, the average aspect ratio is more preferably 1.5 or more, and still more preferably 1.7 or more.
Furthermore, the average circularity of the dicalcium silicate compound is preferably 0.8 or less, as described above. When the average circularity is 0.8 or less, it is advantageous in improving fire resistance. From the above viewpoint, the average circularity is more preferably 0.75 or less, and still more preferably 0.7 or less. There is particularly no limit to the lower limit of the average circularity, but it is usually about 0.5.
Note that, as described above, the average circularity indicates the average value of circularity expressed as 4×circumference ratio π×area/(square of circumferential length).
The average particle diameter, average aspect ratio, and average circularity of the dicalcium silicate compound can be measured as follows.
(1) For a plurality of dicalcium silicate compounds, an image of the dicalcium silicate compounds projected on a plane, is obtained. Such an image can be obtained, for example, by photographing a plurality of dicalcium silicate compounds from one direction, or by photographing a cross section of a porous layer containing the dicalcium silicate compounds.
(2) From the obtained image, the particle diameter, the aspect ratio, and the circularity (area, circumferential length) of each grain of the dicalcium silicate compound are measured. The particle diameter, aspect ratio, and circularity (area, circumferential length) can be measured using appropriate image analysis software (IMAGEJ, etc.). The number of particle points to be measured is preferably in the range of 3,000 to 5,000 points. When it is 3,000 points or more, it is preferable because the measurement error is small, and when it is 5,000 points or less, it is preferable because it reduces the physical burden of the measurer.
(3) From the measured particle diameter, aspect ratio, and circularity, the respective average values can be calculated to obtain the average particle diameter, the average aspect ratio, and the average circularity.
Note that the aspect ratio is a value expressed as (major axis diameter)/(minor axis diameter). It shows that the closer this value is to 1, the closer to a perfect circle it is.
There is no particular problem even if the dicalcium silicate compound in the present invention contains MgO, R2O (R is an alkali metal), etc., as long as the total amount is 10% by mass or less. Further, as long as the total amount of the DCS compound in the present invention is 10% by mass or less, there is no particular problem even if the DCS compound contains a glass phase generated by rapid cooling.
The fineness of the dicalcium silicate compound is preferably 2,000 to 6,000 cm2/g, more preferably 2,500 to 5,000 cm2/g in Blaine specific surface area value (hereinafter referred to as “Blane value”). When it is 2,000 cm2/g or more, sufficient compressive strength development and fire resistance performance can be obtained. On the other hand, when it is 6,000 cm2/g or less, carbonation resistance after the reception of heat can be obtained.
The DCS compound is obtained by mixing a raw material containing CaO, a raw material containing SiO2, a raw material containing Al2O3, etc., and subjecting the mixture to heat treatment such as firing in a kiln or melting in an electric furnace. The heat treatment temperature depends on the composition of the raw materials, but is preferably 1,400° C. or higher and 1,800° C. or lower, more preferably 1,450° C. or higher and 1,600° C. or lower, and still more preferably 1,450° C. or higher and 1,550° C. or lower. When the temperature is lower than 1,400° C., the reaction will not proceed efficiently and unreacted Al2O3 may remain, making it impossible to obtain dicalcium silicate. On the other hand, when the temperature exceeds 1,800° C., coating will easily form during heat treatment. This may not only make operation difficult, but also reduce energy efficiency.
The content of the dicalcium silicate compound in the present admixture is preferably 35% or more, more preferably 45% or more. Further, the upper limit of the content of the dicalcium silicate compound is not particularly limited.
Examples of a method for quantifying the dicalcium silicate compound in the present admixture include the Rietveld method using powder X-ray diffraction.
The cement admixture according to the present embodiment preferably has a chemical composition in the range of 44 to 75 parts of CaO, 18 to 55 parts of SiO2, 1 to 3 parts of Al2O3, 0 to 5 parts of MgO, 0 to 2 parts of SO3; more preferably has a chemical composition in the range of 49 to 70 parts of CaO, 23 to 50 parts of SiO2, 1 to 2 parts of Al2O3, 0 to 3 parts of MgO, 0 to 1 parts of SO3; with respect to 100 parts of the total of CaO, SiO2, Al2O3, MgO, and SO3. When it is within this range, it is preferable because it has advantageous such that the time required to reach demoldable strength will not be extended, the compressive strength will be maintained, the time required to impart fire resistance will not be extended, and the carbonation depth after the reception of heat will be reduced.
Further, the cement admixture according to the present embodiment may further contain calcium carbonate in an amount of 5 parts or less with respect to 100 parts of the cement admixture. By containing calcium carbonate, it has advantages such as increasing the storage stability of cement admixtures and improving the strength development of produced concrete. From the above viewpoint, the content of calcium carbonate is more preferably in the range of 0.5 to 3 parts.
The raw materials used for producing the cement admixture used in the present invention will be explained.
Raw materials containing CaO are not particularly limited. Commercially available industrial raw materials, for example quicklime (CaO), slaked lime (Ca(OH)2), and limestone (CaCO3), can be given. In addition, by-product slaked lime such as acetylene by-product slaked lime, industrial waste such as steel slag (converter slag, electric furnace slag), coal ash, wood biomass combustion ash, fine powder generated from waste concrete lumps, concrete sludge, and municipal waste incineration ash, etc. can also be applied as long as they do not impair the effects of the present invention. From the viewpoint of reducing non-energy-derived CO2 emissions during heat treatment, it is preferable because one or two or more selected from industrial by-products containing CaO, such as by-product slaked lime, fine powder generated from waste concrete lumps, municipal waste incineration ash, and sewage sludge incineration ash, can be used. Among them, it is more preferable to use by-product slaked lime, which has a lower amount of impurities than other industrial by-products.
As the by-product slaked lime, by-product slaked lime produced in the acetylene gas production process using the calcium carbide method (there are wet and dry products depending on the acetylene gas production method), and acetylene by-product slaked lime, such as by-product slaked lime contained in the dust captured in the wet dust collection process of calcium carbide electric furnaces, can be given. The by-product slaked lime contains, for example, 65 to 95% (preferably 70 to 90%) calcium hydroxide, and in addition, contains 1 to 10% calcium carbonate and 0.1 to 6.0% (preferably 0.1 to 3.0%) of iron oxide. These ratios can be confirmed by X-ray fluorescence measurement and mass loss fractions determined by differential thermogravimetric analysis (TG-DTA) (Ca(OH)2: around 405° C. to 515° C., CaCO3: around 650° C. to 765° C.). The volume average particle size measured by the laser diffraction and scattering method is about 50 to 100 μm.
Further, the moisture content measured by the loss on drying method in JIS K 0068 “Method for measuring moisture in chemical products” is preferably 10% or less. Sulfur compounds such as CaS, Al2S3, and CaC2/CaS may also be included, but the content is preferably 2% or less.
The raw material containing SiO2 is not particularly limited. Commercially available industrial raw materials, for example silica stone, silica sand, quartz, and diatomaceous earth, can be given. Furthermore, various siliceous dusts generated as industrial by-products such as silica fume and fly ash can also be used as long as they do not impair the effects of the present invention.
<<Raw Materials Containing Al2O3>>
The raw material containing Al2O3 is not particularly limited. Commercially available industrial raw materials, for example Al2O3, aluminum hydroxide, and bauxite, can begiven. Note that bauxite is desirable because it contains Fe2O3, SiO2, and TiO2 together with Al2O3. On the other hand, when the raw material containing CaO or SiO2 contains the necessary amount of Al2O3, it may not be necessary to use the raw material containing Al2O3.
The MgO raw material used in the present invention is not particularly limited, but for example, magnesia such as fused magnesia, sintered magnesia, natural magnesia, and light burnt magnesia can be used. The MgO raw materials mentioned here refers to the one in which magnesium hydroxide (Mg(OH)2) extracted from seawater by the seawater method, magnesium carbonate (MgCO3), magnesite which is natural MgO, or sintered magnesia clinker obtained by sintering natural magnesium carbonate in a rotary kiln and the like, or electro-fused magnesia clinker obtained by melting such sintered magnesia clinker in an electric furnace and the like, are crushed and screened to a specified size.
The raw materials containing SO3 is not particularly limited, but for example, fresh gypsum, anhydrite (anhydrite), calcined gypsum (hemihydrate gypsum), and desulfurized gypsum (dihydrate gypsum), can be given.
The CaO raw material, SiO2 raw material, Al2O3 raw material, MgO raw material, and SO3 raw material may contain impurities, but this is not a particular problem to the extent that it does not impair the effects of the invention. As the specific examples of impurities, Fe2O3, TiO2, MnO, Na2O, K2O, P2O5, F, B2O3, chlorine, can be given. In addition, as the compounds that coexist, free calcium oxide, calcium hydroxide, calcium aluminate, calcium aluminosilicate, calcium ferrite and calcium aluminoferrite, calcium phosphate, calcium borate, magnesium silicate, leucite (K2O, Na2O)·Al2O3·SiO2, spinel MgO·Al2O3, magnetite Fe3O4, sulfur compounds such as the aforementioned CaS, Al2S3, and CaC2·CaS, can be given.
Among these impurities, the content of S (sulfur) in the dicalcium silicate compound is preferably 1.0% or less, more preferably 0.7% or less, still more preferably 0.5% or less in terms of oxide (SO3). When the content is 1.0% or less, a sufficient effect of promoting carbonation (salt) can be obtained, and the coagulation and curing properties can be controlled within appropriate ranges. The S content in terms of oxide (SO3) can be measured by fluorescent X-ray measurement. Note that S (sulfur) in the DCS compound may be present as long as it is about 2% in terms of oxide.
<Slag and/or Pozzolanic Substances>
The cement admixture of the present invention may contain slag and/or pozzolanic substances. The slag and/or pozzolanic substances are latent hydraulic substances and are not particularly limited, but for example, blast furnace slag (air-cooled blast furnace slag, granulated blast furnace slag), steelmaking slag (converter slag, electric arc furnace slag), fly ash, silica fume, metakaolin, pulp sludge incineration ash, sewage sludge incineration ash, volcanic glass fine powder, waste glass powder, and the like, can be given. These may be used alone or in combination of two or more.
Among these, granulated blast furnace slag fine powder, fly ash, silica fume, and metakaolin are preferable, from the viewpoint of maintaining the retained ratio of compressive strength and the retained ratio of Young's modulus after the sufficient reception of heat, as well as the effect of carbonation resistance after the reception of heat.
Further, the mixing ratio of the DCS compound and the slag and/or pozzolanic substance is not particularly limited, but the mass ratio is preferably 10/1 to 1/10, more preferably 5/1 to 1/5.
By setting the mixing ratio of the DCS compound and slag and/or pozzolanic substance (latent hydraulic substance) within the above range, sufficient rust prevention effect, chloride ion penetration resistance, the effect of inhibition of Ca ion elution and the improvement of self-healing ability can be obtained compared to the the case of DCS compound alone.
In addition, in the present invention, in order to maintain the retained ratio of compressive strength and the retained ratio of Young's modulus after the sufficient reception of heat, and the effect of carbonation resistance after the reception of heat, it is possible to use a cement admixture having the CaO/SiO2 molar ratio of 0.15 to 0.7 and the SO3 content of 0 to 3% in combination with slag and/or pozzolanic substances.
Note that this embodiment can also use industrial by-products containing non-hydraulic compounds such as γ-DCS. At this time, impurities coexist. As such industrial by-products, steelmaking slag and the like can be given.
The cement admixture can be produced by blending a raw material containing CaO, a raw material containing SiO2 and a raw material containing SO3 so that the CaO/SiO2 molar ratio is 1.3 to 3.0 and the SO3 content is 0 to 3%, and heat-treated at 1,000° C. or higher. The heat treatment method is not particularly limited, but can be performed using, for example, a rotary kiln or an electric furnace. Although the heat treatment temperature is not uniquely determined, it is usually conducted in the range of about 1,000 to 1,800° C., and often conducted in the range of about 1,200 to 1,600° C.
Further, it is preferable to adjust the clinker produced as described above by screening so as to have the Blaine specific surface area described in detail below.
Although the Blaine specific surface area of the present admixture is not particularly limited, it is preferably 1,500 cm2/g or more, and the upper limit is preferably 8,000 cm2/g or less. Among these, 2,000 to 6,000 cm2/g is more preferable, and 4,000 to 6,000 cm2/g is most preferable. When the Blaine specific surface area is 1,500 cm2/g or more, good material separation resistance is obtained and the effect of promoting carbonation (salt) is sufficient. In addition, by setting the Blaine specific surface to 8,000 cm2/g or less, the crushing power during crushing does not become large, which is economical, and weathering is suppressed, so that deterioration of quality over time can be suppressed.
The cement used in the present invention is not particularly limited, but preferably contains Portland cement, and various types of Portland cement such as normal, early strength, super early strength, low heat, and moderate heat, can be given as examples. In addition, various mixed cements made by mixing these Portland cements with blast furnace slag, fly ash, or silica, waste-based cements produced by using municipal garbage incineration ash, sewage sludge incineration ash, etc. as raw materials, so-called Ecocement (R), filler cements mixed with limestone powder, and the like, can be given. Furthermore, geopolymer cement which emit less CO2 than conventional cement, sulfoaluminate cement, and limestone calcined clay cement (LC3) can also be given. Among these, one or two or more of these can be used.
In the cement composition of the present embodiment, when the water binder ratio is low, it is beneficial for blast furnace cement and ecocement, which are strongly required to suppress carbonation, and it is most preferably used in combination with blast furnace cement.
The amount of cement admixture to be used is not particularly limited, but usually, when using only a dicalcium silicate compound as a cement admixture, 1 to 15 parts are preferred, 2 to 12 parts are more preferred, in 100 parts of a cement composition containing cement and cement admixture. When the used amount of cement admixture is small, a sufficient retained ratio of compressive strength and a retained ratio of Young's modulus after the sufficient reception of heat, and a sufficient carbonation resistance after the reception of heat may not be obtained, and when it is used in excess, a decrease in strength development may appear. In addition, when using a dicalcium silicate compound, a latent hydraulic substance, and/or a pozzolanic substance as a cement admixture, 1 to 50 parts are preferred, 5 to 30 parts are more preferred, in 100 parts of a cement composition containing cement and cement admixture. When the used amount of cement admixture is small, sufficient carbonation resistance after the reception of heat may not be obtained, and when it is used in excess, a sufficient retained ratio of Young's modulus may not be ensured.
In the present invention, a cement composition is prepared by blending cement and a cement admixture, or blending cement and a dicalcium silicate compound.
The used amount of the cement admixture is not particularly limited, but is usually preferably 5 to 80 parts, more preferably 5 to 50 parts, and still more preferably 10 to 40 parts in 100 parts of the total of the cement and the admixture. When it is 5 parts or more, the heat of hydration can be lowered, and when it is 80 parts or less (particularly 50 parts or less), strength development is improved.
The used amount of water in the cement composition of this embodiment is not particularly limited, and may be within a normal usage range. Specifically, the amount of water is preferably 25 to 70 parts, more preferably 30 to 65 parts, with respect to 100 parts of the total of the cement and present admixture. When it is 25 parts or more, sufficient workability can be obtained, and when it is 70 parts or less, sufficient strength development and carbonation (salt) promotion effects can be obtained.
In addition, in order to comply with the 32.5 N/mm2 standard using this cement admixture, approximately 10 to 20 parts of this cement admixture should be mixed in 100 parts of the present cement composition, regardless of the type of non-hydraulic compound. In addition, in order to comply with the 42.5 N/mm2 standard product class, it is sufficient to mix about 20 to 35 parts in 100 parts of the present cement composition.
The particle size of the cement composition of the present embodiment is not particularly limited since it depends on the purpose and use of the cement composition, but usually, the Blaine specific surface area is preferably 2,500 to 8,000 cm2/g, more preferably 3,000 to 6,000 cm2/g. When it is 2,500 cm2/g or more, sufficient strength development can be obtained, and when it is 8,000 cm2/g or less, good workability can be obtained.
For the cement admixture and cement composition of the present invention, the respective materials may be mixed at the time of construction, or some or all of the materials may be mixed in advance. Further, the method of mixing each material and water is not particularly limited, and each material may be mixed at the time of construction, or some or all of the materials may be mixed in advance. Alternatively, after mixing a part of the material with water, the remaining material may be mixed.
In the present invention, in addition to cement, cement admixtures, fine aggregates such as sand, and coarse aggregates such as gravel, it is possible to use one or two or more of the group consisting of known additives and admixtures used in ordinary cement materials, for examples, air-cooled blast furnace slag powder, admixtures such as fine limestone powder, expanding agents, rapid hardening materials, water reducing agents, AE water reducing agents, high performance water reducing agents, high performance AE water reducing agents, antifoaming agents, thickeners, rust preventive agents, antifreeze agents, shrinkage reducers, polymers, setting modifiers, clay minerals such as bentonite, and additives such as anion exchangers such as hydrotalcite, within a range that does not substantially impair the object of the present invention.
As the mixing device, any existing device can be used, such as a tilting mixer, omni mixer, Henschel mixer, V-type mixer, and Nauta mixer.
Hereinafter, the present invention will be explained in more detail using Examples and Comparative Examples, but the present invention is not limited to the following Examples unless it departs from the gist of the invention.
After embedding the cement admixture prepared in each example etc. in epoxy resin, it was cut with a diamond cutter. Thereafter, it was polished with #1200 silicon carbide abrasive paper, and mirror-finished using an abrasive (3 μm diamond paste). Next, using a 33% aqueous solution of ammonium chloride, etching was performed for 2 seconds, followed by microscopic observation.
The average particle diameter, average aspect ratio, and average circularity of the dicalcium silicate compound were measured by the method described in the description. The microscope used was “Eclipse E600POL” manufactured by Nikon Corporation, and the number of samples measured was 4,000. In addition, image analysis software (“IMAGEJ” manufactured by Wayne Rasband, National Institutes of Health, USA) was used.
After carbon was deposited on the sample surface of the prepared cement admixture, it was identified through point analysis (50 analysis points) using electron microscopy and EDX (energy dispersive X-ray fluorescence spectrometer).
It was measured by fluorescent X-ray measurement. As the fluorescent X-ray measurement device, “ZSX-100e” manufactured by Rigaku Co., Ltd. was used.
Compressive strength at 28 days of age was measured according to JIS R 5201 “Physical test method for cement”. However, the test specimens were demolded when the material was 1 day of age, and then sealed and cured until the material age was 7 days, and thereafter, carbonation curing was applied under the conditions of temperature: 20° C., humidity: 60% RH, and CO2 concentration: 5%, until the material became 28 days of age. After that, to prevent explosion due to moisture dissipation in the test specimen, the test specimen was dried in a drying oven at 105° C. for 1 week, and then heated in an electric furnace at 500° C. for 3 hours, and by using this, the compressive strength at room temperature was measured. Furthermore, the compressive strength of the test specimens before drying and heat treatment was also measured at room temperature. The ratio of the compressive strengths before and after drying and heat treatment was determined as the retained ratio of compressive strength (compressive strength after drying and heat treatment/compressive strength before drying and heat treatment).
Young's modulus was measured according to JIS A 1149 “Test method for static elastic modulus of concrete”. The pretreatment method for the test specimen was the same as the test method for the retained ratio of the compressive strength. The ratio of Young's modulus before and after drying and heat treatment was determined as the retained ratio of Young's modulus (Young's modulus after drying and heat treatment/Young's modulus before drying and heat treatment).
After 3 hours of heat treatment, the 4×4×16 cm specimen was subjected to accelerated carbonation in an environment of 30° C., relative humidity of 60%, and carbon dioxide concentration of 5%, and after 8 weeks, the specimen was sliced into rings. A 1% alcohol solution of phenolphthalein was applied to the cracked cross section of the test specimen to check the carbonation depth. The pretreatment method for the test specimen was the same as the test method for the retained ratio of compressive strength. The carbonation resistance was evaluated based on the following formula.
Carbonation resistance=(Carbonation depth after heat treatment+accelerated carbonation (mm)/Carbonation depth before heating at 500° C. (mm))×100
The final setting time was measured according to JIS R 5201 “Physical test method for cement”.
Cement admixtures A to J were prepared as follows. Each cement admixture was identified by the above method as a DCS compound, and the average particle size, average aspect ratio, average circularity, and chemical composition as measured by the above method are as listed in Table 1.
Calcium carbonate of 1st grade reagent and silicon dioxide of special grade reagent were mixed in a molar ratio of 2:1, and aluminum oxide of 1st grade regent was mixed to an internal ratio of 2 parts and mixed and milled in a planetary ball mill (manufactured by FRITSCH GmbH). The mixture was then heated at 1,400° C. for 2 hours, left to stand to room temperature, and a cement admixture A with a Blaine specific surface area of 4,000 cm2/g, which is the fraction that passes through a 150 μm sieve, was prepared.
It was produced in the same manner as the cement admixture A, except that silicon dioxide of special grade reagent was replaced by silica sand.
It was produced in the same manner as cement admixture A, except that calcium carbonate of 1st grade reagent was replaced by limestone.
It was produced in the same manner as cement admixture A, except that silicon dioxide of special grade reagent was replaced by fused silica.
It was produced in the same manner as cement admixture B, except that silica sand that had passed through a sieve mesh of 150 μm was used.
It was produced in the same manner as cement admixture A, except that the firing temperature was changed to 1,450° C.
It was produced in the same manner as cement admixture A, except that silicon dioxide of special grade reagent was replaced by silica sand, and the mixing and pulverization in a planetary ball mill was replaced by hand mixing.
It was produced in the same manner as cement admixture A, except that mixing and pulverizing in a planetary ball mill was replaced by hand mixing.
It was produced in the same manner as cement admixture G except that the residue on the sieve mesh of 150 μm of silica sand was used.
It was produced in the same manner as cement admixture A except that silicon dioxide of special grade reagent was replaced by fused silica.
The cement admixtures shown in Table 1 were mixed with cement to prepare a cement composition. The blending amount of the cement admixture was 20 parts in 100 parts of the cement composition. Note that Experimental Example 2-11 was a composition containing only cement, without blending cement admixture.
Next, a mortar specimen with a water/binder (cement composition) ratio of 0.5 was prepared according to JIS R 5201 “Physical test method for cement”. Using this mortar specimen, the retained ratio of compressive strength, the retained ratio of Young's modulus, and carbonation resistance were measured according to the above evaluation method. The results are listed in Table 2. Note that the test was conducted at an environmental temperature of 30° C.
Cement admixtures B-2 to B-9 were prepared as follows. Each cement admixture, as identified by the above method, contained a DCS compound, and the average particle size, average aspect ratio, and average circularity of the DCS as measured by the above method are as listed in Table 3. The chemical composition of the cement admixture are as shown in Table 3. The final setting time (time required to demold) measured by the above method is shown in Table 3. Furthermore, the retained ratio of compressive strength, the retained ratio of Young's modulus, and carbonation resistance measured in the same manner as in Experimental Example 2 are also listed in Table 3.
It was produced in the same manner as the cement admixture A, by replacing silicon dioxide of special grade reagent by silica sand, replacing aluminum oxide by aluminum oxide of special grade reagent, and blending the raw materials so that the chemical composition is the numerical values listed in Table 3, in the above (1-1) production of cement admixture A.
It was produced in the same manner as the cement admixture B-2, except that in the above (3-1), each raw material was blended so that the chemical composition is the numerical value listed in Table 3.
It was produced in the same manner as the cement admixture B-2, except that in the above (3-1), each raw material was blended so that the chemical composition is the numerical value listed in Table 3.
It was produced in the same manner as the cement admixture B-2, except that in the above (3-1), magnesium carbonate (MgCO3) of 1st grade reagent was further blended as an MgO source, and each raw material was blended so that the chemical composition is the numerical value listed in Table 3.
It was produced in the same manner as the cement admixture B-5, except that in the above (3-4), the amount of magnesium carbonate (MgCO3) was changed, and each raw material was blended so that the chemical composition is the numerical value listed in Table 3.
It was produced in the same manner as the cement admixture B-2, except that in the above (3-1), gypsum dihydrate (CaSO4·2H2O) of the 1st grade reagent was further blended as the SO3 source, and each raw material was blended so that the chemical composition is the numerical value listed in Table 3.
It was produced in the same manner as the cement admixture B-7, except that in the above (3-6), the amount of gypsum dihydrate (CaSO4·2H2O) was changed.
It was produced in the same manner as the cement admixture B-2, except that in the above (3-1), magnesium carbonate (MgCO3) of 1st grade reagent was further blended as an MgO source, gypsum dihydrate (CaSO4·2H2O) of 1st grade reagent was further blended as the SO3 source, and each raw material was blended so that the chemical composition is the numerical value listed in Table 3.
The tests were conducted in the same manner as in Experimental Example 2, except that DCS compound B (Blaine specific surface area; 3000 cm2/g) prepared in Experimental Example 1-2 was used and passed through a sieve to make a cement admixture with the fineness (Blaine specific surface area) shown in Table 4. The results are shown in Table 4.
Using the cement admixture B (Blaine specific surface area: 3,000 cm2/g, calcium carbonate content: 0 parts) prepared in Experimental Example 1-2, after passed through a sieve, it was allowed to stand in a room at 50° C., 60% of relative humidity, and CO2 concentration of 20% to produce the cement admixtures containing calcium carbonate shown in Table 5. The test was conducted in the same manner as in Experimental Example 2, except that the evaluation was performed after the accelerated storage test shown below. The results are shown in Table 5.
100 g of cement admixture was placed on a 20×20 cm square stainless-steel tray, spread out, and left in a room at 20° C. and 60% of relative humidity for 3 days with the top surface open. Mortar was prepared using the samples collected after 3 days, and physical properties were evaluated.
In Experimental Example 2-2, a test was conducted in the same manner as in Experimental Example 2, except that cement admixture B and a latent hydraulic substance and/or a pozzolanic substance described below were used together. The results are shown in Table 6.
Pozzolanic substance a (also serves as a latent hydraulic substance): commercially available granulated blast furnace slag powder, Blaine value: 4,000 cm2/g
Pozzolanic substance b: commercially available silica fume, BET specific surface area 20 m2/g
Pozzolanic substance c: commercially available fly ash, Blaine value 4,000 cm2/g
Pozzolanic substance d: commercially available metakaolin, BET specific surface area 10 m2/g
Pozzolanic substance e: commercially available pulp sludge incineration ash, Blaine value 4,000 cm2/g
Pozzolanic substance f: Commercially available sewage sludge incineration ash, Blaine value 9,000 cm2/g
Pozzolanic substance g: Commercially available waste glass powder, Blaine value 4,000 cm2/g
Pozzolanic substance h: mixture of 50 parts of pozzolanic substance a and 50 parts of pozzolanic substance b, Blaine value 10,000 cm2/g
Penetration resistance of chloride ion was evaluated. A cylindrical mortar specimen of 10 cmϕ×20 cm was prepared, and the prepared mortar specimen was cured in water at 30° C. until the material became 28 days of age, and then immersed in simulated seawater, which is saline water with a salinity concentration of 3.5%, at 30° C. for 12 weeks, and then the chloride penetration depth was measured. The chloride penetration depth was determined by the fluorescein-silver nitrate method, and the portion of the cross section of the mortar specimen that did not turn brown was regarded as the chloride penetration depth, and was measured at 8 points with a caliper to determine the average value.
The determination was made by immersing a 4×4×16 cm mortar specimen in 10 liters of pure water for 28 days and measuring the concentration of Ca ions dissolved in the liquid phase.
A 10×10×40 cm mortar specimen was prepared by mixing 0.15% by mass of 6 mm nylon fibers, and cracks with a width of 0.3 mm were introduced by bending stress. After being immersed in simulated seawater for 180 days, the crack width was measured. The evaluation criteria were as follows.
From the results in Tables 1 and 2, it can be seen that the cement composition blended with cement admixtures containing DCS compounds is excellent is all of the retained ratio of compressive strength, the retained ratio of Young's modulus, and the carbonation resistance after heating at 500° C.
On the other hand, it can be seen that the cement compositions blended with the cement admixture H containing a DCS compound having an average particle size of less than 5 μm, and the cement admixture I containing a DCS compound having an average particle size of more than 100 μm both have a small retained ratio of compressive strength and a small retained ratio of Young's modulus. Furthermore, it can be seen that the cement composition blended with the cement admixture J containing a DCS compound having an average aspect ratio of less than 1.3 has poor carbonation resistance after heating at 500° C.
Moreover, from the results in Table 3, it can be seen that the cement composition blended with the DCS compound according to the present invention has a short time required to demold and has high productivity.
Further, from the results in Table 4, it can be seen that when the Blaine specific surface area is in the range of 3,000 to 6,000 cm2/g, an extremely good strength development can be obtained.
In addition, from the results in Table 5, it can be seen that by blending an appropriate amount of calcium carbonate into the cement admixture, better results are shown in all of the retained ratio of compressive strength, the retained ratio of Young's modulus, and the carbonation resistance after heating at 500° C., compared to the case of the DCS compound alone.
Furthermore, from the results in Table 6, it can be seen that by further blending a latent hydraulic substance and/or a pozzolanic substance into the DCS compound, excellent chloride ion penetration resistance and the effect of inhibition of Ca ion elution are obtained, and self-healing ability is improved, compared to the the case of DCS compound alone.
The present invention can be particularly suitably used in cement admixtures used in the civil engineering field, construction field, etc.
Number | Date | Country | Kind |
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2021-134147 | Aug 2021 | JP | national |
Filing Document | Filing Date | Country | Kind |
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PCT/JP2022/031074 | 8/17/2022 | WO |