JPS58145648A - Coal-burning cement raw material calcining process - Google Patents
Coal-burning cement raw material calcining processInfo
- Publication number
- JPS58145648A JPS58145648A JP2678082A JP2678082A JPS58145648A JP S58145648 A JPS58145648 A JP S58145648A JP 2678082 A JP2678082 A JP 2678082A JP 2678082 A JP2678082 A JP 2678082A JP S58145648 A JPS58145648 A JP S58145648A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- raw material
- cement raw
- cement
- raw materials
- 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
Links
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明に石炭焚きセメント原料仮焼方法に関するもので
、とくに、仮焼炉の主燃料が石炭であるセメントクリン
カ焼成設備によって、セメント原料の一部に、ボタまた
は油頁岩などの可燃分を含む原料を利用してセメントク
リンカを製造する方法における原料の仮焼方法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coal-fired cement raw material calcination method, and in particular, by using cement clinker firing equipment in which the main fuel of the calciner is coal, a part of the cement raw material is mixed with botanicals or oil shale. The present invention relates to a method for calcining raw materials in a method for manufacturing cement clinker using raw materials containing combustible components such as.
従来のこの種のセメントクリンカ焼成設備は、第1図に
示すように、通常のセメント原料1と可燃分を含むセメ
ント原料2とを粉砕する粉砕iwsと、サスペンション
プレヒータ4と、仮焼バーナ5を有する仮焼炉6と、ロ
ータリキルン7と、クリンカクーラ8と、石炭9を粉砕
して仮焼バーナ5に供給するための粉砕装置10などと
からなっている。As shown in FIG. 1, this type of conventional cement clinker firing equipment includes a pulverizing IWS for pulverizing a normal cement raw material 1 and a cement raw material 2 containing combustibles, a suspension preheater 4, and a calcining burner 5. It consists of a calcining furnace 6, a rotary kiln 7, a clinker cooler 8, and a crushing device 10 for crushing coal 9 and supplying it to the calcining burner 5.
すなわち、従来の方法におけるBJ燃分を含むセメント
原料2については、通常の原料用粉砕装量6に可燃分を
含むセメント原料2を添加して粉砕し、その原料粉末を
サスペンションプレヒータ4の上段に供給していた。し
たがって、仮焼炉6Vc達するまでに、原料温度が70
0℃を越すので、可燃分の一部が燃焼する。この燃焼熱
は原料温度の昇温には寄与するが、CaCO3の脱炭酸
反応には役立たない。このため、結呆としてサスペンシ
ョンブレヒータ4の排ガス温度が」二昇する。そして、
丑だ該プレヒータ4のダスト内VCも未燃分が含まれて
いるため、結局は、供給した可燃分の約50%位しか寄
与しない。That is, regarding the cement raw material 2 containing BJ fuel in the conventional method, the cement raw material 2 containing combustible content is added to the usual crushing charge 6 for raw materials and pulverized, and the raw material powder is placed in the upper stage of the suspension preheater 4. was supplying. Therefore, by the time the calcining furnace reaches 6Vc, the raw material temperature is 70Vc.
Since the temperature exceeds 0°C, some of the combustibles will burn. Although this heat of combustion contributes to raising the temperature of the raw material, it is not useful for the decarboxylation reaction of CaCO3. As a result, the temperature of the exhaust gas from the suspension brake heater 4 rises by 2.5 cm. and,
Since the VC in the dust of the preheater 4 also contains unburned matter, it ultimately contributes only about 50% of the supplied combustible matter.
本発明は、ボタとか油頁岩とか、そのままで′は活用方
法の少々い固体可燃物質を十メント原料の一部として利
用するとともに、その保有する可燃分の熱量を有効利用
することができる石炭焚きセメンl−涼料仮焼方法を提
供することを目的とするものである。The present invention utilizes solid combustible materials such as botanicals and oil shale, which are difficult to utilize as they are, as part of the raw material for jukumento, and also provides a coal-fired material that can effectively utilize the calorific value of the combustible content. The object of the present invention is to provide a method for calcining cement l-coolant.
このため、本発明は、石炭を主燃料としてセメント原料
を仮焼するにあたり、その石炭の粉砕工程で可燃分を含
むセメント原料を混入し、これを仮焼用燃料とすること
を特徴としている。For this reason, the present invention is characterized in that when calcining cement raw materials using coal as the main fuel, cement raw materials containing combustibles are mixed in during the coal pulverization process, and this is used as a fuel for calcining.
以丁、本発明の一実施例について、第2図を参照しなか
ら’Jl明する。An embodiment of the present invention will now be explained with reference to FIG.
通常のセメント原料11、つまり、主として石灰質原料
と粘土質原料の混合粉末は、サスペンションブレヒータ
4の1一段供給口から供給され、畠温ガスと熱父換しな
がら下降して仮焼炉6に入る。A normal cement raw material 11, that is, a mixed powder of mainly calcareous raw materials and clay raw materials, is supplied from the 1st-stage supply port of the suspension breheater 4, descends while exchanging heat with the hot gas, and enters the calcining furnace 6. enter.
一方、仮焼炉6の主たる燃料である石炭9は足置供給機
12により粉砕装置10に供給されて粉末となる。その
際、ボタや油頁岩などの司燃分紫含むセメント原$12
も別のだ量供給機16により同し粉砕装置10に供給き
れて粉末となる。粉末の粒匿は88μのふるいて残渣4
〜15φ位でめる。On the other hand, coal 9, which is the main fuel for the calciner 6, is supplied to a crusher 10 by a foot feeder 12 and turned into powder. At that time, cement raw material containing solid minerals such as bota and oil shale was used for $12
The powder is completely supplied to the same crushing device 10 by another bulk feeder 16 and becomes powder. Powder particle size is 88μ sieve and residue 4
Finish at around 15φ.
そして、この両者の混合粉末は輸送装置14により仮焼
炉6に設り−られた仮焼バーナ5に供給され、仮焼fI
6内において、石炭および原料の可燃分は燃焼し、セメ
ント原料の仮焼反応に寄与する。それと同時に可燃分を
含むセメント原料はサスペンションブレヒータ4に供給
されたセメント原料と混合して、後続のロータリキルン
/内で焼成され、セメントクリンカとなるしたかつて、
原料の保有するb」燃分tよ専し仮焼炉6内で燃焼し、
かりに残ったとしても、仮焼炉6に続くサスペンション
プレヒータ下段す・1クロン内で燃焼するので、口丁燃
分の全熱量か有効利用される。またサスペンションプレ
ヒータ4からの排ガスダスト内には未燃分は含1れない
。しかも、1」−燃分を含むセメント原料は、通常、C
acosを含有しており、それを石炭粉砕装置10に混
入しているので、粉末化した石炭の輸送装置14などの
後続の装置での炭じん爆発の防止にも役立つ二次的効果
が期待−Cきる。Then, the mixed powder of both is supplied to the calcination burner 5 installed in the calcination furnace 6 by the transportation device 14, and the calcination fI
6, the combustible components of the coal and raw materials are combusted and contribute to the calcination reaction of the cement raw materials. At the same time, the cement raw material containing combustible content is mixed with the cement raw material supplied to the suspension breheater 4 and fired in the subsequent rotary kiln to become cement clinker.
The amount of fuel t possessed by the raw materials is burned exclusively in the calciner 6,
Even if it remains in the furnace, it will be burned in the lower stage of the suspension preheater following the calcination furnace 6, so the total amount of heat left by the combustion will be effectively utilized. Furthermore, the exhaust gas dust from the suspension preheater 4 does not contain any unburned matter. Moreover, cement raw materials containing 1"-fuel are usually C
Since it contains acos and is mixed into the coal crushing device 10, it is expected that it will have a secondary effect that will help prevent coal dust explosions in subsequent devices such as the powdered coal transportation device 14. C Kill.
すなわち、CaCO3が脱炭酸する時の反応は吸熱反応
なの一部、炭素の燃焼を防止するから、上記二次的効果
が期待できる。That is, the reaction when CaCO3 is decarboxylated is partly an endothermic reaction, and the combustion of carbon is prevented, so the above-mentioned secondary effects can be expected.
このように、本発明は、可燃分忙富むセメント原料ヲサ
スペンションプレヒータに通常の原料とともに供給する
のではなく、仮焼炉の主たる原料である石炭と同じ粉砕
装置でその石炭に剖記叶燃分を含むセメント原料を混入
して粉砕し、その輸送装置および仮焼バーナも石炭用の
それら?共用して仮焼炉にその粉末を供給して、前記可
燃分の熱量をセメント原料の焼成熱に利用する方法であ
るから、その原料の可燃分を100%イ1効利用てき、
セメント製造分野の省エネルギ一対策となり、かつ、従
来の設備を大幅に改造することなく、単に、可燃分を含
むセメント原料の定量供給機を石炭用粉砕装置の前に追
加するだけでよく、しかも、副次的効果として石炭の粉
じん爆発の防止にも役立つことにもなる。In this way, the present invention does not supply the cement raw material, which is rich in combustible content, to the suspension preheater together with ordinary raw materials, but instead uses the same crusher as the coal that is the main raw material of the calciner to process the coal with high combustible content. Are the cement raw materials containing them mixed and pulverized, and their transportation equipment and calcining burners also used for coal? Since this is a method in which the powder is shared and supplied to a calcining furnace and the heat of the combustible content is used as heat for firing the cement raw material, 100% of the combustible content of the raw material can be effectively used.
This is an energy-saving measure in the cement manufacturing field, and without major modification of existing equipment, it is sufficient to simply add a quantitative feeder for cement raw materials containing combustibles in front of the coal crushing equipment. As a side effect, it will also help prevent coal dust explosions.
第1図は従来の方法の説明図、第2図は本発明の一実施
例の説明図である。
2・・・可燃分を含むセメント原料、4・・・サスペン
ションプレヒータ、5・・・仮焼バーナ、6・・・仮焼
炉、9・・・石汝、10・・・粉砕装置、11・・・通
常のセメント原料、1213・・・定量供給機、140
0.@送装置。
特許出願人 石川島播暦重工業株式会社代 理 人
弁理士小 山 富 久FIG. 1 is an explanatory diagram of a conventional method, and FIG. 2 is an explanatory diagram of an embodiment of the present invention. 2... Cement raw material containing combustible matter, 4... Suspension preheater, 5... Calciner, 6... Calciner, 9... Stone, 10... Grinding device, 11... ...Ordinary cement raw materials, 1213...Quantitative feeder, 140
0. @Feeding device. Patent applicant: Ishikawajima Banreki Heavy Industries Co., Ltd. Agent
Patent Attorney Tomi Hisashi Koyama
Claims (1)
成設備によって、セメント原料の一部に可燃分を含む原
料を利用してセメントクリンカを製造する方法において
、前記可燃分を含む原料を前記石炭と同じ粉砕装置でそ
の石炭に混入して粉砕し、その輸送装置および仮焼バー
ナも石炭用のそれらを共用して仮焼炉にその粉末を供給
して、前記可燃分の熱量をセメント原料の焼成熱に利用
することを特徴とする、石炭焚きセメント原料仮焼方法
。1. In a method of manufacturing cement clinker using raw materials containing combustibles as a part of the cement raw materials using cement clinker firing equipment that uses coal as the main fuel in a calcining furnace, the raw materials containing combustibles are replaced with the coal. The powder is mixed with the coal and pulverized in the same pulverizer as the pulverizer, and the transportation device and calcining burner are also used for coal, and the powder is supplied to the calciner, and the calorific value of the combustible content is transferred to the cement raw material. A coal-fired cement raw material calcination method characterized by utilizing the heat of calcination.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2678082A JPS58145648A (en) | 1982-02-23 | 1982-02-23 | Coal-burning cement raw material calcining process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2678082A JPS58145648A (en) | 1982-02-23 | 1982-02-23 | Coal-burning cement raw material calcining process |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58145648A true JPS58145648A (en) | 1983-08-30 |
Family
ID=12202812
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2678082A Pending JPS58145648A (en) | 1982-02-23 | 1982-02-23 | Coal-burning cement raw material calcining process |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58145648A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10342959B2 (en) | 2014-03-31 | 2019-07-09 | Toray Industries, Inc. | Balloon catheter |
-
1982
- 1982-02-23 JP JP2678082A patent/JPS58145648A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10342959B2 (en) | 2014-03-31 | 2019-07-09 | Toray Industries, Inc. | Balloon catheter |
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