JPS641422B2 - - Google Patents
Info
- Publication number
- JPS641422B2 JPS641422B2 JP55053218A JP5321880A JPS641422B2 JP S641422 B2 JPS641422 B2 JP S641422B2 JP 55053218 A JP55053218 A JP 55053218A JP 5321880 A JP5321880 A JP 5321880A JP S641422 B2 JPS641422 B2 JP S641422B2
- Authority
- JP
- Japan
- Prior art keywords
- coal ash
- coal
- strength
- gypsum
- anhydrous gypsum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000010883 coal ash Substances 0.000 claims description 57
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims description 30
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 27
- 239000000920 calcium hydroxide Substances 0.000 claims description 27
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 27
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 27
- 239000002994 raw material Substances 0.000 claims description 25
- 239000003245 coal Substances 0.000 claims description 20
- 238000004519 manufacturing process Methods 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 12
- 238000002485 combustion reaction Methods 0.000 claims description 10
- 239000011812 mixed powder Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000000465 moulding Methods 0.000 claims description 4
- 238000004898 kneading Methods 0.000 claims description 3
- 239000000047 product Substances 0.000 description 21
- 238000000034 method Methods 0.000 description 19
- 229910001653 ettringite Inorganic materials 0.000 description 14
- 239000010440 gypsum Substances 0.000 description 14
- 229910052602 gypsum Inorganic materials 0.000 description 14
- 239000000843 powder Substances 0.000 description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 8
- 238000012545 processing Methods 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 239000002956 ash Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 5
- 239000000292 calcium oxide Substances 0.000 description 5
- 235000012255 calcium oxide Nutrition 0.000 description 5
- 150000004683 dihydrates Chemical class 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 239000004568 cement Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 240000006909 Tilia x europaea Species 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 150000004645 aluminates Chemical class 0.000 description 3
- 150000008064 anhydrides Chemical class 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000010881 fly ash Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- ZOMBKNNSYQHRCA-UHFFFAOYSA-J calcium sulfate hemihydrate Chemical compound O.[Ca+2].[Ca+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZOMBKNNSYQHRCA-UHFFFAOYSA-J 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000000306 component Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000012717 electrostatic precipitator Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 2
- 229910052815 sulfur oxide Inorganic materials 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 229910052925 anhydrite Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000009415 formwork Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052863 mullite Inorganic materials 0.000 description 1
- 238000013001 point bending Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
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[Industrial Field of Application] The present invention relates to a method for producing a hardened material using coal ash discharged during coal combustion as a main raw material, and more specifically, a method for producing a hardened material using coal ash as a main raw material, and more specifically, a mixed powder made by adding slaked lime and molded anhydrous gypsum to coal ash as a raw material. The present invention relates to a method for producing a hydrated and hardened body with high mechanical strength by preparing a molded body as a molded body and treating this molded body with steam. [Conventional technology] In recent years, it has become difficult for Japan to secure a large amount of oil imports due to the international oil supply instability since the oil crisis of 1978, and efforts have been made to develop alternative energies to oil in order to reduce the country's dependence on oil. has become a national issue, and coal, a fossil fuel like oil, has become a national issue.
It is being reconsidered as one pillar. There are various issues to overcome in the practical application of coal utilization technology, which is necessary for mass consumption of coal, and among them, the treatment of large amounts of coal ash generated during coal combustion has been highlighted as an important issue. When burning coal, usually almost 15-20 of the coal usage
% coal ash is generated. Previously in Japan, approximately 10 to 20% by weight of coal ash was reused as fly ash for cement admixtures, cement raw materials, etc., and the rest was disposed of in landfills. However, with regard to the current method of using fly ash as a raw material for cement, it is not expected that the demand will be sufficient to meet the large amount of coal ash generated in the future, and disposal in landfills is not possible either in sea-surface or land-based landfills. From the standpoint of environmental conservation, it is becoming difficult to secure land for ash dumping. Therefore, considering that an extremely large amount of coal ash is generated when full-scale coal is used in coal-fired power plants, etc., it is extremely difficult to process all of the coal ash using current coal ash processing methods. Coal ash processing and effective utilization technologies are thought to have a major impact on the scale of coal energy use. In addition, effective reuse as a resource is essential for establishing a mass processing method for coal ash. This is based, firstly, on the fact that in Japan, where domestic resources are scarce, reuse rather than mere disposal directly leads to resource and energy conservation, and secondly, there is very little environmental destruction. Previously, Japanese Patent Publication No. 43-21667 describes how limestone powder is used to reduce exhaust gas in heavy oil-fired power plants.
A method of producing concrete using dust after removing SO 2 and exhaust coal ash is disclosed. Furthermore, in JP-A-53-1222, the first raw material is a mixture of anhydrous gypsum and calcium hydroxide or calcium oxide, and the second raw material is a mixture of coal ash and dilute sulfuric acid. A method for producing cement by mixing a first raw material and a second raw material is disclosed. [Problems to be solved by the invention] In the method described in the above-mentioned Japanese Patent Publication No. 43-21667, the ratio range of the mixed powder is not indicated, but as shown in Table 1 on page 2 of the publication, In addition, the ratio of thickness is 58.1% for combination A {465 ÷ (335
+465)Ã100}, 33.3% for combination B {306÷
(306 + 306 + 306) x 100}, the ratio of ash is relatively small, and it is not suitable for processing coal ash, which is emitted in large quantities during coal combustion. In addition, when processing with steam, the temperature is relatively high at 180â and 10 atm.
High-pressure steam is used (No. 17, left column, page 2 of the bulletin)
line). In this way, the method described in this publication aims to effectively utilize desulfurized limestone powder in heavy oil-fired power plants, so even if relatively high temperature and high pressure steam is used, the compressive strength is 40%.
Kg/cm 2 , 70Kg/cm 2 (see Table 2 on page 2), which is an extremely low value. In the method described in this publication, as mentioned above, the curing is performed using relatively high-temperature, high-pressure steam at 180°C and 10 atm, so an autoclave is required as manufacturing equipment (page 2, left column 17 of the publication). (see row), the equipment is too large and continuous processing is not possible, so batch processing must be performed, making it unsuitable for processing large amounts of coal ash, and furthermore, the cost of heating energy to maintain the temperature at 180°C is significant. Further, in the method described in the above-mentioned Japanese Patent Application Laid-open No. 53-1222, the ratio range of the mixed powder is not indicated, but the example in the upper left column of page 3 of the publication shows coarse coal ash 14.9
%, calcium hydroxide 5.0%, anhydrous gypsum 79.5%
The case is shown in which the proportion of anhydrite is extremely large and the proportion of coal ash is small.
Therefore, it cannot be said to be a preferable method for treating coal ash that is emitted in large quantities during coal combustion. That is, the method described in this publication uses anhydrous gypsum, calcium hydroxide (or calcium oxide), coal ash,
It uses sulfuric acid as a raw material, and dihydrate gypsum after hydration hardening becomes the strength member, and Na 2 SO 4 and K 2 SO 4 , which are reaction products of coal ash and sulfuric acid, act as setting accelerators for anhydrous gypsum. Anhydrous gypsum is the main raw material. On the other hand, the present invention uses coal ash, slaked lime, and type anhydrous gypsum as raw materials, and the reaction product (ettringite) of these becomes a strength member, and coal ash is the main raw material. In this way, the method described in this publication,
The strength development mechanism is different from the present invention.
Further, this publication does not suggest any technical concept of treating the molded body with normal pressure steam at a relatively low temperature of 80 to 100°C. The present invention was made in view of the above points, and in order to utilize coal ash in large quantities as a resource in the civil engineering and construction fields, the present invention provides a method for producing a hydrated material with high mechanical strength using coal ash as the main raw material. The purpose is to provide [Means and effects for solving the problems] In order to achieve the above object, the method for producing a hardened material using coal ash as a main raw material of the present invention is to reduce the amount of coal ash emitted from coal ash by weight of 60 to 85% by weight. %, slaked lime 15-30
After adding water and kneading a mixed powder consisting of 10 to 20% by weight of anhydrous gypsum, this kneaded product is molded using a mold or a molding container, and then this molded body is It is designed to be treated with normal pressure steam at â. In the method of the present invention, the amount of mixed water (weight % of water added to 100 weight % of powder) is 10 to 60%,
Desirably it is 30-50%. Hereinafter, the configuration of the present invention will be explained in detail. In general, the typical properties of coal ash, such as its components, composition, and particle size distribution, greatly depend on the place of production and combustion history of the coal. First of all, the proportions of ingredients such as SiO 2 , Al 2 O 3 , CaO, Fe 2 O 3 , Na 2 O, K 2 O, etc. differ depending on the place where coal is produced. The coal ash generated is mainly pulverized coal combustion ash, and depending on the location and collection method, electrostatic precipitator (EP)
It is distinguished into ash (raw powder, fine powder, coarse powder), clinker ash, and cinder ash, each with a different particle size distribution. Therefore, when producing a high-strength hydration-hardened body by steam treatment using coal ash, slaked lime, and molded anhydrous gypsum as raw materials, hydration-hardening The proper manufacturing conditions for each body are slightly different. Factors that have a large contribution rate as manufacturing conditions include pretreatment of coal ash (mainly pulverization), blending ratio of coal ash, slaked lime, and molded anhydrous gypsum, and steam treatment conditions (temperature, time). Note that atmospheric pressure steam is used as the steam due to the strength of the processing equipment. The relationship between the manufacturing conditions for the raw material powder consisting of coal ash, slaked lime, and type anhydrous gypsum and the properties of the hydrated product is roughly as follows. The main components of the hydrated hardened product produced by steam treatment are ettringite (3CaOã»Al 2 O 3ã»3CaSO 4ã»32H 2 O) and various forms of calcium silicate hydrate (XCaOã»YSiO 2ã»
ZH 2 O), but the one that contributes the most as a strength member is ettringite. First, when the content of molded anhydrous gypsum in the raw material mixed powder is low,
Calcium monosulfo aluminate hydrate (3CaOã»Al 2 O 3ã»CaSO 4ã»12H 2 O) is the main component, and the strength of the hydrated hardened product is low, but as the anhydrous gypsum content increases The amount of ettringite, which is a strength member, increases and the strength increases. Furthermore, when the amount of mold anhydrous gypsum added increases,
During steam treatment, free gypsum that does not participate in the reaction is generated, reducing the strength of the hydrated and hardened product. Therefore, the amount of mold anhydrous gypsum is limited to 10-20% by weight. In addition, when the slaked lime content in the raw material mixed powder is low, calcium monosulfo aluminate hydrate becomes the main component, and the strength of the hydrated hardened product is small, and as the amount of slaked lime added increases, The amount of ettringite produced increases and the strength also increases.
When the amount of slaked lime added is further increased, more slaked lime does not participate in the ettringite production reaction, resulting in a decrease in strength. In other words, if the blending ratio of slaked lime exceeds 30% by weight, a large amount of slaked lime will remain after steam treatment, and in a dry atmosphere, the slaked lime will turn into calcium carbonate, and the reaction expansion will generate many hair cracks (microcracks), resulting in poor product quality. deteriorates. For these reasons, the amount of slaked lime is limited to 15 to 30% by weight. The particle size distribution of coal ash also has a large effect on the properties of the hydrated hardened material. Generally, as the particle size of coal ash becomes smaller, that is, as the specific surface area becomes larger, the hydrated and hardened material tends to exhibit a predetermined strength in a shorter treatment time. This is made from coal ash, slaked lime, and type anhydrous gypsum, and the reaction that produces ettringite by steam treatment is a through solution reaction, and the solubility of Al 2 O 3 is significantly lower than that of slaked lime and gypsum. The production rate of ettringite is
It can be assumed that this is because it depends on the dissolution rate of Al 2 O 3 . The steam treatment conditions are mainly determined by the treatment temperature and treatment time, and the appropriate range of the steam conditions also differs depending on the particle size distribution of the coal ash as described above. Generally, when the steam treatment time is short, the hydrated hardened product consists of a mixture of calcium monosulfo aluminate hydrate, dihydrate gypsum, and ettringite, and its strength is low; The amount of produced increases and the strength also increases. If steam treatment is carried out for a long time and steam treatment is continued even after the formation of ettringite has been completed, ettringite lacks heat resistance and decomposes into anhydrous gypsum and calcium aluminate hydrate, and the strength of the hydrated hardened product decreases. descend. Note that if the hydrated hardened product is cured for 1 to 30 days in an atmosphere with a relative humidity of 70 to 100%, the reaction of ettringite and the like will proceed and the strength can be improved. As mentioned above, the manufacturing conditions for the hydrated hardened material largely depend on the properties of the coal ash used as the raw material, and the most suitable coal ash pretreatment (pulverization) conditions and slaked lime that correspond to the components, composition, and particle size distribution of the coal. It is desirable to select the amount of anhydrous gypsum and steam treatment conditions (treatment temperature, treatment time). The type anhydrous gypsum used in the present invention may be either natural type anhydrous gypsum or type anhydrous gypsum produced by subjecting dihydrate gypsum to dry heat treatment or wet heat treatment. By constructing a plant that continuously converts flue gas desulfurization gypsum produced during the removal of sulfur oxides generated during coal combustion into anhydrous gypsum, coal ash and sulfur oxides, which are emissions from coal combustion, will be reduced. Another advantage of the present invention is that both can be treated at the same location and at the same time. After kneading the raw material powder and water in the present invention,
The strength of the molded product before steam treatment, which is molded in a formwork etc., is not very high after curing at room temperature for a short time, and if there is a risk of damage during handling or transportation, Accordingly, it is also useful to increase the mechanical strength by tamping press molding or the like when producing a molded body before steam treatment. In the method of the present invention, the temperature of atmospheric pressure steam is 80°C.
If the temperature is below 100°C, the rate of ettringite formation is slow, resulting in a small amount of produced crystals and thick crystals that do not exhibit high strength. Since this is more likely to occur, the generated ettringite will be decomposed and high strength will not be developed. Among the limes, slaked lime has the effect of making the hardened body porous and decreasing the bulk density, and quicklime has the effect of making the hardened body dense and increasing the bulk density. Furthermore, among gypsum, hemihydrate gypsum has a low solubility.
0.58 (β type), 0.45 (α type) (g anhydride/100g solution
at 50°C), the kneaded material rapidly hardens.
The solution is a saturated aqueous solution of gypsum dihydrate, which has a solubility of 0.26 (g anhydride/100g solution at 50°C).
Therefore, the kneaded material does not harden. Type anhydrous gypsum has a solubility of 0.21 (g anhydride/100g solution at 50°C), and as in the present invention, it will not harden if there is no hardening accelerator.
When a curing accelerator is present, it has the effect of increasing solubility and gradually curing.
Therefore, the strength of the molded product upon demolding varies depending on the type of gypsum. As mentioned above, the hardening speed of the coal ash-lime-gypsum mixture, bulk density, and strength of the hardened product differ due to the differences in the actions and effects of lime and gypsum. For this reason, lime and gypsum are used depending on the quality required depending on the purpose. For example, if we focus on the compressive strength of a hardened product, there is a close relationship with the solubility of gypsum; in a quicklime system, the compressive strength of a hardened product using the same coal ash is For slaked lime systems, the compressive strength of the hardened material when the same coal ash is used is as follows: hemihydrate gypsum system > dihydrate gypsum system > type anhydrous gypsum system. [Example] Next, Examples and Comparative Examples will be described.
The raw material coal ash in Examples and Comparative Examples was commercially available fly ash, and its properties are shown in Table 1.
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ã€ãã[Table] According to X-ray diffraction analysis, the chemical components of raw coal ash include a large amount of quartz (α-SiO 2 ), a medium amount of mullite (3Al 2 O 3ã»2SiO 2 ), and a small amount of magnetite (Fe 3 O4 ) was observed. The test methods for coal ash and hydrated hardened bodies are shown below. The Blaine specific surface area was measured using a powder specific surface area measuring device model SS-100 manufactured by Shimadzu Corporation, using the air permeation method. The bending strength test uses 20à as a test piece.
A 20 x 80 (mm) piece was used, and the MKS improved universal strength testing machine manufactured by Marubishi Kagaku Seisakusho was used as the testing device. The test method was a three-point bending method. In the compressive strength test, a 20 x 20 x 20 (mm) test piece was used, and an Instron universal testing machine (maximum load: 10 tons) was used as the test device. The test method was based on the constant deflection rate method. Note that in the Examples and Comparative Examples, atmospheric pressure steam was used as the steam. Example 1 70 parts of coal ash, 20 parts of slaked lime, 10 parts of molded anhydrous gypsum
1 part and 45 parts of water were mixed to form a slurry, and this slurry was poured into a mold to obtain a molded body. This molded body is demolded, stored in a sealed container, and exposed to steam at 96°C.
A hydrated and cured product was obtained by contacting for 15 hours. The properties of the hydrated and cured product were as shown in Table 2. Example 2 An experiment similar to Example 1 was conducted except that 65 parts of coal ash, 15 parts of slaked lime, and 20 parts of molded anhydrous gypsum were used. The properties of the hydrated and cured product were as shown in Table 2. Comparative example 1 80 parts of coal ash, 0 parts of molded anhydrous gypsum (no addition)
An experiment similar to that of Example 1 was conducted with the other exceptions. The properties of the hydrated and cured product were as shown in Table 2. Comparative Example 2 An experiment similar to Example 1 was conducted except that 90 parts of coal ash and 0 parts of slaked lime (no addition) were used. The properties of the hydrated and cured product were as shown in Table 2. Comparative Example 3 The molded article obtained in Example 1 was tested without steam treatment. The results were as shown in Table 2.
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As explained above, in the method of the present invention, since the coal ash blending ratio in the raw material is as high as 60 to 85% by weight, a large amount of coal ash can be processed.
In addition, because it uses normal pressure steam curing at a relatively low temperature of 80 to 100°C, an open structure is possible (no pressurized and sealed structure is required), simplifying manufacturing equipment, and continuous curing is possible, making it suitable for large-scale processing of coal ash. Furthermore, since the steam temperature is below 100°C, low-temperature steam such as waste steam can be used, reducing energy costs. According to the method of the present invention, by adding slaked lime and molded anhydrous gypsum, which are inexpensive raw materials, to coal ash, which is an exhaust product during coal combustion, and subjecting it to steam treatment, a high-strength hardened body can be easily and inexpensively produced. The method of the present invention is extremely useful as a technology that contributes to the production of various building materials and structural materials in the fields of civil engineering and architecture by effectively utilizing coal ash.
Claims (1)
ïŒ ãæ¶ç³ç°15ã30ééïŒ ãåç¡æ°Žç³ãã10ã20
ééïŒ ãããªãæ··åç²äœã«ãæ°Žãæ·»å ããŠæ··ç·Žã
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ãšãã硬åäœã®è£œé æ¹æ³ã1 Coal ash emitted during coal combustion 60-85% by weight, slaked lime 15-30% by weight, type anhydrous gypsum 10-20%
After adding water and kneading a mixed powder consisting of % by weight, molding the kneaded product using a mold or molding container, and then treating the molded product with atmospheric pressure steam at 80 to 100°C. A method for producing a hardened material using coal ash as a main raw material, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5321880A JPS56149371A (en) | 1980-04-21 | 1980-04-21 | Manufacture of hardened body chiefly based on coal ash |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5321880A JPS56149371A (en) | 1980-04-21 | 1980-04-21 | Manufacture of hardened body chiefly based on coal ash |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56149371A JPS56149371A (en) | 1981-11-19 |
JPS641422B2 true JPS641422B2 (en) | 1989-01-11 |
Family
ID=12936682
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5321880A Granted JPS56149371A (en) | 1980-04-21 | 1980-04-21 | Manufacture of hardened body chiefly based on coal ash |
Country Status (1)
Country | Link |
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JP (1) | JPS56149371A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5980956U (en) * | 1982-11-22 | 1984-05-31 | æ ªåŒäŒç€Ÿå³¶æŽ¥è£œäœæ | ion gun |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS531222A (en) * | 1976-06-25 | 1978-01-09 | Hokkaido Electric Power | Method of manufacturing cement by using as main raw materials calcium sulphonate and coal ash |
-
1980
- 1980-04-21 JP JP5321880A patent/JPS56149371A/en active Granted
Also Published As
Publication number | Publication date |
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JPS56149371A (en) | 1981-11-19 |
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