JPH06329453A - Production of cement - Google Patents

Production of cement

Info

Publication number
JPH06329453A
JPH06329453A JP11881393A JP11881393A JPH06329453A JP H06329453 A JPH06329453 A JP H06329453A JP 11881393 A JP11881393 A JP 11881393A JP 11881393 A JP11881393 A JP 11881393A JP H06329453 A JPH06329453 A JP H06329453A
Authority
JP
Japan
Prior art keywords
cement
coal ash
ash
clinker
raw material
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.)
Pending
Application number
JP11881393A
Other languages
Japanese (ja)
Inventor
Masaru Honda
優 本田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Cement Co Ltd
Original Assignee
Sumitomo Cement Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Cement Co Ltd filed Critical Sumitomo Cement Co Ltd
Priority to JP11881393A priority Critical patent/JPH06329453A/en
Publication of JPH06329453A publication Critical patent/JPH06329453A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/36Manufacture of hydraulic cements in general
    • C04B7/43Heat treatment, e.g. precalcining, burning, melting; Cooling
    • C04B7/44Burning; Melting
    • C04B7/4407Treatment or selection of the fuel therefor, e.g. use of hazardous waste as secondary fuel ; Use of particular energy sources, e.g. waste hot gases from other processes

Abstract

PURPOSE:To provide a method for producing a cement having the same quality as that of a conventional cement clinker, capable of easily burning non-burnt carbon contained in a carbon ash, by directly blowing the coal ash into a cement kiln from its front part and burning the non-burnt carbon in the coal ash in the cement kiln. CONSTITUTION:This method for producing a cement by mixing a cement raw material with a coal ash and calcining the mixture, when the cement raw material is calcined in a cement kiln, is to directly blow the coal ash into the cement kiln from its front part, burn non-burnt carbon contained in the coal ash, add the residual ash to a cement clinker, and to subsequently calcine the mixture. The method enables to easily burn the non-burnt carbon in the coal ash, utilize the generated heat as the combustion energy for the cement clinker, and produce a cement having the same quality as that of a conventional cement clinker, because the produced carbon-free coal ash is solid-dissolved in the cement clinker.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は石炭灰を混合するセメン
トの製造方法に係り、特に石炭灰中に未燃カーボンが混
入している場合にも適用が可能な技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing cement in which coal ash is mixed, and more particularly to a technique applicable even when unburned carbon is mixed in the coal ash.

【0002】[0002]

【従来の技術】石炭火力発電所から排出される石炭灰
は、その排出量が年々増加しており、その処分場が不足
することが懸念されている。一方、石炭灰を有効利用す
るためのの方法の1つとして、石炭灰をセメント中に混
合し、モルタルやコンクリート製造用のセメント材料と
して使用する方法が知られている。図2は、従来の石炭
灰混合セメントの製造方法の概要を説明するためのもの
であり、この図中符号1は原料混合サイロ、2はプレヒ
ーター、3はロータリーキルン、4はバーナー、5はク
ーラーである。従来法による石炭灰混合セメントの製造
では、石灰石や粘土などを微粉砕したセメント原料中に
石炭灰を添加し、原料混合サイロ1で均一に混合し、こ
の混合原料をプレヒーター2に導入し、多段に配置され
た炉内を順次移動させつつ、ロータリーキルン3からの
高温排ガスで混合原料を余熱し、余熱された混合原料を
ロータリーキルン3内で焼成し、更にクーラー5を通し
て冷却し、クリンカーを製造する。得られたクリンカー
はセッコウなどを加えてセメントミルで粉砕混合して製
品のセメントとする。
2. Description of the Related Art The amount of coal ash discharged from a coal-fired power plant is increasing year by year, and it is feared that the disposal site will be insufficient. On the other hand, as one of the methods for effectively utilizing coal ash, a method is known in which coal ash is mixed in cement and used as a cement material for producing mortar or concrete. FIG. 2 is for explaining an outline of a conventional method for producing a coal ash mixed cement, in which reference numeral 1 is a raw material mixing silo, 2 is a preheater, 3 is a rotary kiln, 4 is a burner, 5 is a cooler. Is. In the production of coal ash mixed cement by the conventional method, coal ash is added to a cement raw material in which limestone or clay is finely pulverized, and the raw material mixing silo 1 mixes the mixture uniformly, and the mixed raw material is introduced into the preheater 2. While moving sequentially in the furnace arranged in multiple stages, the mixed raw material is preheated by the high temperature exhaust gas from the rotary kiln 3, the preheated mixed raw material is calcined in the rotary kiln 3, and further cooled through the cooler 5 to produce a clinker. . Gypsum and the like are added to the obtained clinker, and the mixture is ground and mixed in a cement mill to obtain a product cement.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、石炭灰
をセメント混合材として使用する際には次のような問題
がある。石炭を燃料とする火力発電にあっては、大気汚
染物質の排出量削減のため、その燃焼条件に厳しい規制
がなされており、これに伴って石炭灰中の未燃カーボン
が増える傾向にあり、セメント混合材としての使用が不
適当な石炭灰が増加している。また、石炭灰はセメント
原料に比べ溶融温度が低いため、これをセメント原料中
に大量に添加すると、セメント原料を余熱するプレヒー
ター部分にコーチングが付着し、操業上問題を生じるお
それがある。
However, the use of coal ash as a cement admixture has the following problems. In the case of thermal power generation using coal as a fuel, strict regulations are applied to its combustion conditions in order to reduce emissions of air pollutants, and unburned carbon in coal ash tends to increase accordingly. Increasing coal ash is unsuitable for use as a cement admixture. Further, since coal ash has a lower melting temperature than that of the cement raw material, if a large amount of this is added to the cement raw material, the coating may adhere to the preheater portion that preheats the cement raw material, which may cause a problem in operation.

【0004】本発明は上記事情に鑑みてなされたもの
で、未燃カーボンが混入している石炭灰にも適用が可能
であり、石炭灰を大量に用いても操業に支障をきたすこ
となく、石炭灰を混入したセメントを製造することが可
能な製造方法の提供を目的としている。
The present invention has been made in view of the above circumstances, and can be applied to coal ash mixed with unburned carbon, and even if a large amount of coal ash is used, it does not hinder the operation. It is an object of the present invention to provide a manufacturing method capable of manufacturing cement mixed with coal ash.

【0005】[0005]

【課題を解決するための手段】かかる課題を解決するた
めに、本発明は、セメントキルンの窯前部から石炭灰を
セメントキルン中に直接吹き込み、該石炭灰中に含まれ
る未燃カーボンを燃焼させるとともに残部の灰分をセメ
ントクリンカー中に混合して焼成するようにした。
In order to solve such problems, the present invention is to blow coal ash directly into the cement kiln from the kiln front part of the cement kiln, and burn unburned carbon contained in the coal ash. At the same time, the remaining ash was mixed in cement clinker and fired.

【0006】[0006]

【作用】石炭灰をセメントキルン中に直接吹き込み、石
炭灰中に含まれる未燃カーボンを燃焼させるとともに残
部の灰分をセメントクリンカー中に混合して焼成するこ
とによって、石炭灰中の未燃カーボンを容易に燃焼させ
ることができ、しかもその熱をセメントクリンカーの焼
成エネルギーとして活用できるとともに、カーボンを含
まない石炭灰がセメントクリンカー中に固溶するので、
通常のセメントクリンカーと同等の品質のセメントが得
られる。
[Operation] By blowing coal ash directly into the cement kiln, burning the unburned carbon contained in the coal ash, and mixing the remaining ash with the cement clinker and firing it, the unburned carbon in the coal ash is removed. It can be easily burned, and its heat can be used as the burning energy of the cement clinker, and since coal ash that does not contain carbon dissolves in the cement clinker,
The quality of cement is the same as that of ordinary cement clinker.

【0007】[0007]

【実施例】以下、図面を参照して本発明を詳細に説明す
る。図1は本発明のセメントの製造方法の一例を説明す
るものであって、この方法では、石灰石や粘土などを微
粉砕したセメント原料を原料混合サイロ1で均一に混合
し、このセメント原料をプレヒーター2に導入し、多段
に配置された炉内を順次移動させつつ、ロータリーキル
ン3からの高温排ガスで混合原料を余熱し、ついで余熱
されたセメント原料をロータリーキルン3内に搬入して
高温焼成するとともに、ロータリーキルン3の窯前部に
石炭灰の吹き込み管6を設置し、石炭灰を直接ロータリ
ーキルン3内に吹き込み、セメント原料と混合して焼成
する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the drawings. FIG. 1 illustrates an example of a method for producing cement according to the present invention. In this method, a cement raw material obtained by finely crushing limestone or clay is uniformly mixed in a raw material mixing silo 1 and the cement raw material is preliminarily mixed. While introducing into the heater 2 and sequentially moving through the furnaces arranged in multiple stages, the high temperature exhaust gas from the rotary kiln 3 preheats the mixed raw material, and then the preheated cement raw material is carried into the rotary kiln 3 for high temperature firing. A blowing tube 6 for coal ash is installed in the kiln front part of the rotary kiln 3, and the coal ash is blown directly into the rotary kiln 3 and mixed with the cement raw material and fired.

【0008】ここで使用する石炭灰としては、石炭火力
発電所等からの石炭灰が使用され、この石炭灰中に未燃
カーボンを含有していても良い。使用する石炭灰は、乾
燥され、必要に応じて微粉砕され、吹き込み管6を通し
てロータリーキルン3内に吹き込み易い状態としてお
く。
As the coal ash used here, coal ash from a coal-fired power plant or the like is used, and the coal ash may contain unburned carbon. The coal ash to be used is dried, finely pulverized if necessary, and kept in a state in which it can be easily blown into the rotary kiln 3 through the blowing pipe 6.

【0009】この石炭灰を気流搬送するためのキャリア
ガスとしては、通常は空気が用いられる。一般にロータ
リーキルン3からの排ガスには酸素ガスが少ないため、
石炭灰を吹き込むためのキャリアガス中に酸素ガスがあ
れば、石炭灰中の未燃カーボンを容易に燃焼させること
ができる。
Air is usually used as a carrier gas for carrying the coal ash by air flow. In general, the exhaust gas from the rotary kiln 3 contains little oxygen gas,
If oxygen gas is present in the carrier gas for blowing in the coal ash, the unburned carbon in the coal ash can be easily burned.

【0010】石炭灰中の未燃カーボンは、ロータリーキ
ルン3内に吹き込まれ、瞬時に燃焼し、未燃カーボンを
含まない灰となってセメント原料に混合され、ロータリ
ーキルン3中で高温焼成されてセメント原料と灰とが固
溶し、セメントクリンカーとなり、クーラー5を通して
冷却し、ロータリーキルン3から取り出す。得られたク
リンカーは、通常のセメントクリンカーと同様に、セッ
コウ等を添加し、セメントミルで粉砕混合して製品のセ
メントとする。
The unburned carbon in the coal ash is blown into the rotary kiln 3 and is instantly burned to form ash containing no unburned carbon, which is mixed with the cement raw material, and fired at a high temperature in the rotary kiln 3 to produce the cement raw material. And ash form a solid solution to form a cement clinker, which is cooled through a cooler 5 and taken out from the rotary kiln 3. The obtained clinker is added with gypsum and the like and crushed and mixed with a cement mill to obtain a product cement, as in the case of a normal cement clinker.

【0011】このように、石炭灰をセメントキルン中に
直接吹き込み、石炭灰中に含まれる未燃カーボンを燃焼
させるとともに残部の灰分をセメントクリンカー中に混
合して焼成することによって、石炭灰中の未燃カーボン
を容易に燃焼させることができ、しかもその熱をセメン
トクリンカーの焼成エネルギーとして活用できるととも
に、カーボンを含まない石炭灰がセメントクリンカー中
に固溶するので、通常のセメントクリンカーと同等の品
質のセメントが得られる。以下、実験例により本発明の
効果を明確にする。
As described above, coal ash is directly blown into the cement kiln to burn unburned carbon contained in the coal ash, and the remaining ash is mixed in the cement clinker to be burned. Unburned carbon can be easily burned, and its heat can be used as the burning energy of cement clinker, and since coal ash containing no carbon forms a solid solution in cement clinker, it has the same quality as ordinary cement clinker. To obtain cement. Hereinafter, the effects of the present invention will be clarified by experimental examples.

【0012】(実験例)石炭灰をセメントキルンに直接
吹き込んだ場合のセメントの性状をあらかじめ把握して
おくために次の実験を行った。整粒したセメント原料を
1000℃の電気炉中で仮焼した後、この周りに石炭灰
を付着させ1450℃まで昇温し1時間加熱して得たク
リンカーに石膏を5%添加し、ボールミルでブレーン3
300cm2/gまで粉砕して試製セメントを調製し
た。このセメントのモルタル強さを、普通セメントのク
リンカーから調製したセメントの試験結果と比較し、J
IS R 5201に準じて測定した。その結果を次の表
1に示す。
(Experimental example) The following experiment was carried out in order to grasp beforehand the properties of cement when coal ash was directly blown into the cement kiln. After calcining the sized cement raw material in an electric furnace at 1000 ° C, adhering coal ash around this and heating to 1450 ° C and heating for 1 hour, 5% of gypsum was added to the clinker, and the mixture was crushed with a ball mill. Brain 3
Trial cement was prepared by grinding to 300 cm 2 / g. The mortar strength of this cement was compared with the test results of the cement prepared from the clinker of ordinary cement.
It measured according to ISR5201. The results are shown in Table 1 below.

【0013】[0013]

【表1】 [Table 1]

【0014】表1から明らかなように、石炭灰を添加し
て製造した試製セメントのモルタル強さは、普通セメン
トのクリンカーから調製したセメントと比較すると、3
日及び7日の強度はやや低めであるが、28日強度は同
等であり、品質上何ら問題はなく、実用化が可能であっ
た。
As is clear from Table 1, the mortar strength of the trial cement produced by adding coal ash is 3 when compared with the cement prepared from the clinker of ordinary cement.
Although the strengths on the 1st and 7th days were slightly lower, the strength on the 28th day was the same, and there was no problem in quality, and it was possible to put it into practical use.

【0015】[0015]

【発明の効果】以上説明したように、本発明によるセメ
ントの製造方法は、石炭灰をセメントキルン中に直接吹
き込み、石炭灰中に含まれる未燃カーボンを燃焼させる
とともに残部の灰分をセメントクリンカー中に混合して
焼成することによって、石炭灰中の未燃カーボンを容易
に燃焼させることができ、しかもその熱をセメントクリ
ンカーの焼成エネルギーとして活用できるとともに、カ
ーボンを含まない石炭灰がセメントクリンカー中に固溶
するので、通常のセメントクリンカーと同等の品質のセ
メントが得られる。
As described above, in the method for producing cement according to the present invention, the coal ash is directly blown into the cement kiln to burn the unburned carbon contained in the coal ash and the remaining ash in the cement clinker. The unburned carbon in the coal ash can be easily burned by mixing with and burned, and the heat can be utilized as the burning energy of the cement clinker, and the coal ash that does not contain carbon is mixed in the cement clinker. Since it forms a solid solution, it is possible to obtain cement of a quality equivalent to that of ordinary cement clinker.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明のセメントの製造方法の一例を説明する
ための概略構成図である。
FIG. 1 is a schematic configuration diagram for explaining an example of a method for producing cement according to the present invention.

【図2】従来の石炭灰混合セメントの製造方法を説明す
るための概略構成図である。
FIG. 2 is a schematic configuration diagram for explaining a conventional method for producing a coal ash mixed cement.

【符号の説明】[Explanation of symbols]

1……原料混合サイロ、2……プレヒーター、3……ロ
ータリーキルン、4……バーナー、5……クーラー。
1 ... Raw material mixing silo, 2 ... Preheater, 3 ... Rotary kiln, 4 ... Burner, 5 ... Cooler.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 セメント原料をセメントキルン中で焼成
するに際し、セメント原料に石炭灰を混合、焼成してセ
メントを製造する方法において、 セメントキルンの窯前部から石炭灰をセメントキルン中
に直接吹き込み、該石炭灰中に含まれる未燃カーボンを
燃焼させるとともに残部の灰分をセメントクリンカーに
混合して焼成することを特徴とするセメントの製造方
法。
1. A method for producing cement by firing coal ash in a cement raw material when firing the cement raw material in the cement kiln, in which coal ash is directly blown into the cement kiln from the kiln front part of the cement kiln. A method for producing cement, which comprises burning unburned carbon contained in the coal ash and mixing the remaining ash with a cement clinker and firing the mixture.
JP11881393A 1993-05-20 1993-05-20 Production of cement Pending JPH06329453A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11881393A JPH06329453A (en) 1993-05-20 1993-05-20 Production of cement

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11881393A JPH06329453A (en) 1993-05-20 1993-05-20 Production of cement

Publications (1)

Publication Number Publication Date
JPH06329453A true JPH06329453A (en) 1994-11-29

Family

ID=14745775

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11881393A Pending JPH06329453A (en) 1993-05-20 1993-05-20 Production of cement

Country Status (1)

Country Link
JP (1) JPH06329453A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012232866A (en) * 2011-04-28 2012-11-29 Tokuyama Corp Fired material production apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012232866A (en) * 2011-04-28 2012-11-29 Tokuyama Corp Fired material production apparatus

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