PRODUCTION METHOD FOR CEMENT CLINKER AND CEMENT CLINKER POWDER

Abstract

Portland cement clinker that includes C.sub.3A and C.sub.4AF in total from 22 to 40 mass % calculated by Bogue's formulas and has an iron modulus (I.M.) of 0.8 to 1.3 is produced. The burned raw materials are annealed at a cooling rate of 20 degree Celsius or lower at least to 1200 degree Celsius so that the lightness of the cement clinker is made high. When annealing till lower temperatures, the lightness value becomes generally higher, but the effect becomes negligible lower at 1000 degree Celsius. Therefore, the raw materials are quenched at 1000 degree Celsius and lower for improving the productiveness.

Claims

1. A production method for Portland cement clinker including C.sub.3A and C.sub.4AF in total from 22 to 40 mass % calculated by Bogue's formulas and having an iron modulus (I.M.) of 0.8 to 1.3, carrying out a step for cooling raw materials of the Portland cement clinker after burning the raw materials at 1300 to 1400 degree Celsius, being characterized by, in said cooling step, cooling the raw materials after the burning at a cooling rate of 20 degree Celsius or lower at least to 1200 degree Celsius and then quenching the raw materials from at lowest 1000 degree Celsius.

2. A production method for Portland cement from the Portland cement clinker produced according to claim 1, being characterized in that pulverizing the Portland cement clinker with gypsum or that pulverizing the Portland cement clinker and then mixing with gypsum.

3. The production method for Portland cement according to claim 2, being characterized in that mixing the Portland cement clinker further with at least one of blast furnace slag, limestone, fly ash, and siliceous admixture.

4. A Portland cement clinker powder, including C.sub.3A and C.sub.4AF in total from 22 to 40 mass % calculated by Bogue's formulas, having an iron modulus (I.M.) of 0.8 to 1.3, having a Blaine specific surface area of 2800 to 4500 cm.sup.2/g, and having an L value of at least 50 in Lab color system.

5. The production method for Portland cement clinker according to claim 1, being characterized in that burning the raw materials in a rotary kiln and cooling in a clinker-cooler.

6. The Portland cement clinker powder according to claim 4, being characterized in that the Portland cement clinker powder is obtainable by burning raw materials of the Portland cement clinker at 1300 to 1400 degree Celsius, and cooling the burned raw materials at a cooling rate of 20 degree Celsius or lower at least to 1200 degree Celsius and then quenching from at lowest 1000 degree Celsius.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0013] FIG. 1 A polarized microscopic image indicating the C.sub.2S structure in the cement clinker, burned at 1350 degree Celsius, annealed to 1200 degree Celsius at a rate of 20 degree Celsius per minute, and then quenched to 200 degree Celsius. The field of view is about 300 micro-meter×225 micro-meter.

[0014] FIG. 2 A polarized microscopic image indicating the C.sub.2S structure in the cement clinker, burned at 1350 degree Celsius and immediately quenched to 200 degree Celsius. The field of view is about 300 micro-meter×225 micro-meter.

[0015] FIG. 3 A polarized microscopic image indicating the interstitial phase structure in the cement clinker, burned at 1350 degree Celsius, annealed to 1200 degree Celsius at a rate of 20 degree Celsius per minute, and then quenched to 200 degree Celsius. The field of view is about 125 micro-meter ×90 micro-meter.

[0016] FIG. 4 A polarized microscopic image indicating the interstitial phase structure in the cement clinker, burned at 1350 degree Celsius and immediately quenched to 200 degree Celsius. The field of view is about 125 micro-meter×90 micro-meter.

THE BEST EMBODIMENT FOR CARRYING OUT THE INVENTION

[0017] The quantities of C.sub.3A, C.sub.4AF, and C.sub.3S in the present invention are calculated by the Bogue's formulas.

[0018] The Bogue's formulas have been used along with various indexes and moduli and well-known calculation formulas for calculating approximate major compound compositions from major chemical analysis values. The method for determining the contents of minerals in clinker according to the Bogue's formulas will be described as follows, for reference purpose. The contents are described in mass % unit.

Content of C.sub.3S=(4.07×CaO)−(7.60×SiO.sub.2)−(6.72×Al.sub.2O.sub.3)−(1.43×Fe.sub.2O.sub.3).

Content of C.sub.2S=(2.87×SiO.sub.2)−(0.754×C.sub.3S).

Content of C.sub.3A=(2.65×Al.sub.2O.sub.3)−(1.69×Fe.sub.2O.sub.3).

Content of C.sub.4AF=3.04×Fe.sub.2O.sub.3.

[0019] Iron modulus (I.M.), together with hydraulic modulus (H.M.), silica modulus (S.M.), activity index (A.I.), and lime saturation degree (L.S.D.), is calculated from major chemical analysis values. The iron modulus (I.M.) is a characteristic value for the production control of clinker, and has been used as one of the relevant indexes and moduli and has been well-known. The calculation method of the iron modulus and other indexes will be described as follows.

Hydraulic modulus (H.M.)=CaO/(SiO.sub.2+Al.sub.2O.sub.3+Fe.sub.2O.sub.3).

Silica modulus (S.M.)=SiO.sub.2/(Al.sub.2O.sub.3+Fe.sub.2O.sub.3).

Iron modulus (I.M.)=Al.sub.2O.sub.3/Fe.sub.2O.sub.3.

Activity index (A.I.)=SiO.sub.2/Al.sub.2O.sub.3.

Lime Saturation Degree (L.S.D.)=CaO/(2.8×SiO.sub.2+1.2×Al.sub.2O.sub.3+0.65×Fe.sub.2O.sub.3).

[0020] The above CaO, SiO.sub.2, Al.sub.2O.sub.3, and Fe.sub.2O.sub.3 contents can be measured according to JIS R 5202 “Chemical Analysis Method of Portland Cement” and JIS R 5204 “Fluorescent X-ray Analysis Method of Portland Cement.”

[0021] The cement clinker produced by the present invention has a total content of C.sub.3A and C.sub.4AF from 22 to 40%. When the total content is under 22%, it becomes difficult to produce cement clinker having desirable properties such as strength developing property, by the burning at 1300 to 1400 degree Celsius. The total content is preferably 24% or more. On the other hand, the C.sub.3S content is preferably 60% or more for better strength developing property as described later. Therefore, the total content of C.sub.3A and C.sub.4AF is 40% or less, preferably 35% or less, more preferably 32% or less, and particularly preferably 28% or less. Between C.sub.4AF and C.sub.3A, C.sub.4AF contributes to proceed the sintering at the lower temperature and the reduction in free CaO content in the clinker, and therefore, the C.sub.4AF content is preferably 15% or more.

[0022] The C.sub.3S content has a high influence on the strength developing property of the cement composition (hereinafter, simply referred to as “cement”) using the cement clinker according to the present invention. When the content is 60% or more, a good strength developing property is easily achieved. The C.sub.3S content is more preferably 62% or more and particularly preferably 63% or more. As already described, the total content of C.sub.3A and C.sub.4AF is at least 22%, and therefore, the upper limit of C.sub.3S is 78%. For keeping a desirable time duration from the start of setting to the end of setting, the content is preferably 70% or less and more preferably 65% or less.

[0023] The cement clinker produced according to the present invention may further include C.sub.2S. The content is 18% or less and preferably 3% or more. For better long-term strength, it is particularly preferable to make the total content of C.sub.3S and C.sub.2S 69% or more.

[0024] The iron modulus (I.M.) in the cement clinker produced according to the present invention is 0.8 to 1.3. If the iron modulus exceeds 1.3, enough strength developing property (more specifically, for example, mortar strength development) can not be achieved, even when other conditions are satisfied in the cement clinker according to the present invention. In addition, when the iron modulus exceeds 1.3, the time duration from the start of setting to its end becomes easily too long, and therefore, the iron modulus is 1.3 or less. A more preferable range of iron modulus is 1.0 to 1.3 and it is 1.14 to 1.27, particularly preferably.

[0025] While the hydraulic modulus and the silica modulus are not particularly limited, however, for a good balance between various properties, the hydraulic modulus is preferably 1.8 to 2.2 and particularly preferably 1.9 to 2.1. The silica modulus is preferably 1.0 to 2.0 and particularly preferably 1.1 to 1.7.

[0026] In the production method for cement clinker according to the present invention, the raw materials for the clinker are prepared and mixed by known adequate methods. For example, raw materials such as waste materials, by-products, and other materials (CaO sources such as limestone, quick lime, and slaked lime, SiO.sub.2 sources such as silica stone, Al.sub.2O.sub.3 sources such as clay and coal ash, and Fe.sub.2O.sub.3 sources such as copper slag and blast furnace slag) are chemically analyzed in advance, the mixing ratios of the raw materials are calculated from the compositions of the raw materials such that those requirements according to the present invention are satisfied, and they are mixed at the ratios.

[0027] The same raw materials for the production of conventional cement clinkers can be used in the production method according to the present invention without specific restrictions. Of course, waste products and by-products can be used.

[0028] Usable waste products and by-products are, for example, as follows: blast furnace slag, steel slag, manganese slag, coal ash, sewage sludge, waterworks sludge, paper sludge, dirt produced by construction, casting sand, soot, incinerated fly ash, molten fly ash, chlorine by-path dust, wood, waste white clay, coal debris, waste tires, shells, dust, and its incinerated ash. Some of them are cement raw materials and others are heat energy sources.

[0029] In the conventional productions of cement clinkers, the mixtures of those raw materials are burned at burning temperatures about 1450 degree Celsius for predetermined periods in burning equipment (for example, in SP kilns or NSP kilns) and then normally immediately quenched to about 200 degree Celsius, at a cooling rate of more than 100 degree Celsius per minute, in cooling equipment called “clinker-coolers” comprising air blowers or sprinklers.

[0030] In contrast to this, in the production of cement clinkers having a total amount of C.sub.3A and C.sub.4AF from 22 to 40% and an iron modulus (I.M.) from 0.8 to 1.3, the burning temperature can be lowered from 1300 to 1400 degree Celsius, and the production becomes energy-saving.

[0031] However, the cement clinkers of the above compositions have generally lower lightness (L values in the Lab color system) than normal Portland cement clinkers; the L values are usually below 50 and in many cases, below 48.

[0032] For overcoming the above problem, according to the present invention, the cement clinkers burned at the lower temperature are annealed at a cooling ratio not higher than 20 degree Celsius per minute at least from 1300 degree Celsius to 1200 degree Celsius after the burning. Hereinafter, this process is sometimes called “annealing.” The cement clinkers produced through the annealing have significantly higher lightnesses (brightness) in comparison with conventional cement clinkers quenched in the same temperature range.

[0033] While the specific mechanism for this is further to be investigated, the speculated factors are phase transition including another phase from the phase resultant from the quenching and the changes of the clinker mineral crystals in their sizes and shapes, when annealed.

[0034] In addition, the present inventors have found further annealing in the temperature range below 1000 degree Celsius did not improve the lightness. Moreover, annealing at 1000 degree Celsius or lower needs significant time for the production of cement clinkers and lowers the productivity. Therefore, according to the present invention, quenching is performed at 1000 degree Celsius or lower, similarly to the conventional production.

[0035] When quenching is started at temperatures of 1000 degree Celsius or higher, the lightness increases at the lower quenching start temperatures. However, the productivity decreases as described above. Therefore, considering the two factors, the quenching is set to start between 1200 degree Celsius and 1000 degree Celsius.

[0036] The cement clinker produced according to the present invention can be converted to cement by pulverization with gypsum or mixing them after separate pulverization, similarly to conventional cement clinkers. Examples of types of the cement produced are ordinary Portland cement, early-strength Portland cement, and super early-strength Portland cement. They can be used, other than to Portland cement, in various mixed types of cement and as components of solidification agents, such as soil solidification agents.

[0037] When gypsum is added for converting the clinker into cement, gypsum known as cement raw material, such as gypsum dihydrate, gypsum hemihydrate, and anhydrous gypsum, can be used without limitations. Preferably, gypsum is added such that the SO.sub.3 concentration in the cement is from 1.5 to 5.0 mass % and more preferably, from 1.8 to 3.0 mass %. The cement clinker and gypsum can be pulverized by known methods without limitations.

[0038] The above cement can include and be pulverized with an admixture such as blast furnace slag, siliceous admixture, fly ash, calcium carbonate, and limestone, and/or a pulverizing agent. They can be pulverized separately and then mixed with them. These additives can be mixed with gypsum or separately mixed. In addition, chlorine by-path dust or the like can be mixed.

[0039] While the fineness of cement is not particularly limited, its Blaine specific surface area is preferably 2800 to 4500 cm.sup.2/g.

[0040] When the cement clinker without any additives is pulverized, and when its lightness (L value) is measured, the cement clinker according to the production method of the present invention has a lightness of 50 or more. As already described, if the quenching start temperature is further lowered, the lightness can be 52 or more. However, in most cases, the lightness is 55 or less.

[0041] While the greater Blaine specific surface areas generally afford the larger L values, the finer pulverization is not preferable due to the production cost and so on. The Portland cement clinker including 22 to 40% of C.sub.3A and C.sub.4AF in total, having a high iron content, in reduction to the iron modulus (I.M.), 0.8 to 1.3, having a Blaine specific surface area of 2800 to 4500 cm.sup.2/g, and having the L value of 50 or more is produced according to the production method of the present invention. It has not been produced by conventional methods,

[0042] If needed, the Portland cement clinker according to the present invention is mixed, after the pulverization, with blast furnace slag, fly ash, or the like, to produce blast furnace cement, fly ash cement, or the like.

Embodiment

[0043] The following embodiments describe the constitution and advantageous effects of the present invention. The present invention is not limited to these embodiments.

[0044] The raw materials comprising limestone, silica stone, coal ash, and iron slag, respectively of predetermined amounts, were mixed such that the mixtures after burning have the mineral compositions in Table 1. The mixtures were burned at 1450 degree Celsius or 1350 degree Celsius in an electric furnace and then cooled under predetermined conditions for respective examples, to cement clinkers. The mixtures were kept for 90 minutes at the highest temperature and the burning atmosphere was air, as in the usual method. The resultant cement clinkers were pulverized by a ball mill to the Blaine specific surface area became 3300 plus/minus 50 cm.sup.2/g. Then, the color tone of the clinker powders was measured by a spectro-photometer. The production conditions and measured values are listed in Table 1.

[0045] The spectro-photometer was Spectro-Photometer SE6000 by Nippon Denshoku Industries, Ltd.

TABLE-US-00001 TABLE 1 Quenching Start temperature, Clinker Composition, Three Moduli, and Color Value Quenching Start temperature Composition Three Moduli Color Value (Degree Celsius) C.sub.3S C.sub.2S C.sub.3A C.sub.4AF H.M. S.M. I.M. L a b Reference 1450 65 13.1 9.6 9.4 2.20 2.49 1.81 51.9 −1.2 6.3 Comp. 1 1350 64 6.2 8.7 17.3 2.07 1.51 1.21 45.8 −0.9 5.8 Emb. 1 1200 64.4 6.6 8.7 17.5 2.04 1.51 1.21 50.9 −0.9 4.9 Emb. 2 1100 64.7 6.3 8.7 17.4 2.05 1.51 1.21 52.5 −1.1 5.5 *The compositions are in mass %. *In the reference, quenching was started from the maximum temperature of 1450 degree Celsius, and in the comparative example 1, quenching was started from the maximum temperature of 1350 degree Celsius. *In the embodiments 1 and 2, the clinkers were annealed from the maximum temperature of 1350 degree Celsius to 1200 degree Celsius (Emb. 1) or 1100 degree Celsius (Emb. 2) at 20 degree Celsius per minute and then quenched.

[0046] The reference indicates the production of Portland cement clinker of conventional standard composition: burning at 1450 degree Celsius, and quenching from 1450 degree Celsius at a usual quenching rate larger than 100 degree Celsius per minute.

[0047] The cement clinker in the comparative example 1 included C.sub.3A and C.sub.4AF by 26% in total and had an iron modulus of 1.21 and was configured to be burned at the lower temperature. It was burned at 1350 degree Celsius and quenched from 1350 degree Celsius at a usual cooling rate greater than 100 degree Celsius.

[0048] In the embodiments 1 and 2 of the present invention, the raw materials were prepared to have the same composition to the comparative example 1, burned at 1350 degree Celsius, annealed to 1200 degree Celsius or 1100 degree Celsius at a cooling rate of 20 degree Celsius per minute, and then quenched by air-blow at a usual cooling rate larger than 100 degree Celsius.

[0049] The cement produced according to the production method of the present invention has a large iron content, is configured to be burned at the lower temperature, and has a lightness equivalent to that of the reference comprising a conventional Portland cement clinker.

[0050] FIGS. 1 and 3 indicate the mineral structure of a cement clinker powder corresponding to the embodiment 1; FIG. 1 indicates the C.sub.2S structure, and FIG. 3 indicates the interstitial phase structure comprising C.sub.3A and C.sub.4AF. FIGS. 2 and 4 indicate the mineral structure of a cement clinker powder corresponding to the comparative example 1; FIG. 2 indicates the C.sub.2S structure, and FIG. 4 indicates the interstitial phase structure comprising C.sub.3A and C.sub.4AF. By the way, the portion in FIG. 1 extending from the upper central position to the lower position is a void. In addition, the white structure occupying the gap between particles in FIGS. 1 and 2 comprises the interstitial phase. In FIGS. 3 and 4, the gray structure at gaps between particles comprises the interstitial phase; the dark area comprises C.sub.4AF structure, and the bright area comprises C.sub.3A structure.

[0051] When comparing FIGS. 1 and 2, the size of annealed C.sub.2S particles in FIG. 1 is smaller than that in FIG. 2, and the shape of the particles in FIG. 1 is different from that in FIG. 2. When comparing FIGS. 3 and 4, the C.sub.3A structure and C.sub.4AF structure in the annealed interstitial phase are mutually separated in FIG. 3, while the C.sub.3A structure and C.sub.4AF structure in the quenched interstitial phase are mutually mixed in FIG. 4. In addition, since C.sub.2S experiences several phase transitions at 1200 degree Celsius and lower, the crystalline phase of C.sub.2S can be different between the annealing and the quenching.

[0052] As already known, the size and shape of particles influence lightness. Generally, different crystalline phases afford different lightnesses. When annealed, impurities are excluded from crystal structures, and therefore, the lightness of powders increases generally. Lightness is estimated to increase when the dark C.sub.4AF structure and the bright C.sub.3A structure are separated in comparison with a uniform mixture. Improvement in the lightness of annealed cement clinker powder is estimated to be due to these factors.

[0053] When commercially carrying out the present invention, the burning is performed in a rotary kiln or the like, the annealing and quenching are performed in a clinker-cooler or the like. The adequate clinker-cooler has, for example, multi-stages; the annealing is performed at the first stage or the first and second stages, and the air-blow to the first stage or the first and second stages is reduced or set to 0 so that the cooling rate is made 20 degree Celsius per minute or lower.

[0054] Since the slow annealing rate makes the clinker-cooler larger in the size, the cooling rate at the annealing is preferably 20 degree Celsius per minute or lower and 5 degree Celsius per minute or larger. In the quenching, the cooling rate is 40 degree Celsius per minute or larger and 500 degree Celsius per minute or smaller, and preferably 100 degree Celsius per minute or larger and 500 degree Celsius per minute or smaller.

[0055] The cement clinker temperatures at the annealing and the quenching are measured, for example, by a radiation thermometer at plural positions in the clinker-cooler. The measured temperatures are converted into the cooling rate with use of the moving speed of the cement clinker in the clinker-cooler.