JPS60141653A - Quick lime manufacturing apparatus - Google Patents

Quick lime manufacturing apparatus

Info

Publication number
JPS60141653A
JPS60141653A JP24481783A JP24481783A JPS60141653A JP S60141653 A JPS60141653 A JP S60141653A JP 24481783 A JP24481783 A JP 24481783A JP 24481783 A JP24481783 A JP 24481783A JP S60141653 A JPS60141653 A JP S60141653A
Authority
JP
Japan
Prior art keywords
air
quicklime
fine powder
crusher
collection device
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.)
Granted
Application number
JP24481783A
Other languages
Japanese (ja)
Other versions
JPH0329734B2 (en
Inventor
大塚 将光
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.)
Ube Corp
Original Assignee
Ube Industries 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP24481783A priority Critical patent/JPS60141653A/en
Publication of JPS60141653A publication Critical patent/JPS60141653A/en
Publication of JPH0329734B2 publication Critical patent/JPH0329734B2/ja
Granted legal-status Critical Current

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  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Disintegrating Or Milling (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】 本発明は生石灰の製造装置に係り、更に詳しくは、生石
灰と水分を含んだ空気とが接触しないように構成した生
石灰の粉砕装置を主体とした生石灰の製造装置に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for producing quicklime, and more particularly to an apparatus for producing quicklime which is mainly comprised of a quicklime crushing apparatus configured to prevent contact between quicklime and air containing moisture. It is.

生石灰は水分を含むと、 CaO+J(20−+Ca(
OH)2吉いうように水と反応し、消石灰となってしま
う。
When quicklime contains water, it becomes CaO+J(20-+Ca(
OH) 2 As mentioned above, it reacts with water and becomes slaked lime.

なお、生石灰は例えば鉄鋼の製造において使用されるが
、その場合は、精検時に、生石灰を装入して酸素を吹込
み、脱酸素5脱けい素、脱りん。
Note that quicklime is used, for example, in the manufacture of steel, and in that case, during inspection, quicklime is charged and oxygen is blown in to remove oxygen, remove silicon, and dephosphorize.

脱硫等を行い1不純物を取除いた溶鋼を作るが。Molten steel is made by removing one impurity through desulfurization, etc.

その場合に、水分を含んでいる消石灰や水分を吸着して
いる生石灰を用いると、その水分は溶鋼内に水素として
残留し、これが鋼の性質を悪くシ。
In that case, if slaked lime that contains moisture or quicklime that absorbs moisture is used, the moisture will remain in the molten steel as hydrogen, which will deteriorate the properties of the steel.

特に、特殊鋼を生産する場合は問題になる。This is especially a problem when producing special steel.

そこで、従来においては焼成炉から出て来た生石灰を分
級機内において分級する場合に、生石灰と水分を含んだ
空気とが接触しないように分級機内に窒素ノjスを吹き
込むか、あるいは1別個の脱湿装置によって脱湿したド
ライエヤーを供給しつつ、粉砕分級を行なっていた。
Therefore, in the past, when the quicklime that came out of the kiln was classified in a classifier, a nitrogen gas was blown into the classifier to prevent the quicklime from coming into contact with air containing moisture, or a separate Crushing and classification was carried out while supplying dry air that had been dehumidified by a dehumidifier.

しかし1窒素ガスを使用すると、窒素ガスの吹送装置と
窒素ガス代が必要となり、又脱湿装置により脱湿したド
ライエヤーを供給しようとすると。
However, if 1 nitrogen gas is used, a nitrogen gas blowing device and nitrogen gas cost are required, and if you try to supply dry air that has been dehumidified by a dehumidifier.

これらの装置は別個に必要となり、いずれにしても、経
済的に不利であったり、あるいは、装置全体が大型化す
るという欠点があった。
These devices are required separately, and in any case, there is a disadvantage that it is economically disadvantageous or that the entire device becomes large.

本発明は5以上のような従来の欠点を除去するために成
されたもので、生石灰と水分を含んだ空気とを接触させ
ず、生石灰が水分と反応して消石灰となりでしまうこと
を防止することができ、しかも、経済的な生石灰の製造
装置を提供することを目的としている。
The present invention was made in order to eliminate the above-mentioned drawbacks of the conventional method, and it prevents quicklime from coming into contact with moisture-containing air, thereby preventing quicklime from reacting with moisture and turning into slaked lime. The purpose of the present invention is to provide an economical apparatus for producing quicklime.

本発明においては、上記の目的を達成するだめに、生石
灰焼成炉の冷却帯にある冷却用空気が水分を含んでい々
いことを利用して、これを7閉じられた系を構成する粉
砕機及び分級機等のだめの搬送用空気として用いる構造
を採用した。
In order to achieve the above object, the present invention takes advantage of the fact that the cooling air in the cooling zone of the quicklime kiln contains moisture and crushes it into a closed system. The structure is designed to be used as transport air for waste machines, classifiers, etc.

以下1図面に示す実施例に基づいて本発明の詳細な説明
する。
The present invention will be described in detail below based on an embodiment shown in one drawing.

第1図は本発明の一実施例を説明するもので。FIG. 1 illustrates one embodiment of the present invention.

図において符号1で示すものはベルトコンベアで。In the figure, the symbol 1 is a belt conveyor.

これによって石灰石が石灰焼成炉2内に投入される。As a result, limestone is charged into the lime kiln 2.

石灰焼成炉2は、その上端部が予熱帯C1中間部分が焼
成帯B、下端部が冷却帯Aとなっている。
The lime calcining furnace 2 has a preheating zone C1 at its upper end, a firing zone B at its middle portion, and a cooling zone A at its lower end.

そして、冷却帯Aの部分には空気供給口ろから冷却用空
気が送り込まれ、焼成された生石灰の冷却を行なう。
Cooling air is fed into the cooling zone A from the air supply port to cool the calcined quicklime.

又、予熱帯C側には排ガスファン4が接続されており、
この排ガスファン4によって吸引された石灰焼成炉2内
の排ガスは、集塵器5によってダストを除去された後、
大気中に排出されるか、あるいは、その排ガスのもつ熱
量を何らかの熱源として利用される。
In addition, an exhaust gas fan 4 is connected to the preheating zone C side.
The exhaust gas in the lime kiln furnace 2 sucked by the exhaust gas fan 4 has dust removed by the dust collector 5, and then
Either it is exhausted into the atmosphere, or the amount of heat contained in the exhaust gas is used as a heat source.

一方1石灰焼成炉2を出た生石灰は輸送器6によって輸
送され2エアーロツクフイーダ7によって断気しながら
粉砕機9内に投入される。
On the other hand, the quicklime leaving the 1-lime calcining furnace 2 is transported by a transporter 6 and fed into a crusher 9 by a 2-air lock feeder 7 while being degassed.

粉砕機9によって粉砕された生石灰は、後述するように
脱湿された空気流にのって分級機10側に導かれ、ここ
で分級され、粗粉は粉砕機9側に戻され、微粉のみが空
気流に乗りて配管11を介してサイクロンやバッグフィ
ルタ等から成る微粉補集装置12側へ導かれ、ここで補
集され、補集された微粉はエアーロックフィーダ13に
より断気しながら製品タンク14に貯えられる。
The quicklime crushed by the crusher 9 is guided to the classifier 10 by a dehumidified air flow as described later, where it is classified, and the coarse powder is returned to the crusher 9, leaving only fine powder. The particles are guided by the air flow through piping 11 to a fine powder collection device 12 consisting of a cyclone, a bag filter, etc., where they are collected. It is stored in tank 14.

微粉を補集された後のガスは、誘引ファン15により誘
引され、空気用配管16を通って粉砕機9側に吹込まれ
る。
After the fine powder has been collected, the gas is attracted by the induction fan 15 and blown into the crusher 9 side through the air pipe 16.

符号17で示すものは熱交換器で2この熱交換器の一端
は石灰焼成炉2の冷却帯Aの上部に設けられたガス抽出
]」18に送入管22によって接続されており、他端は
ファン19と送入管22を介して前記微粉補集装置12
と誘引ファン15との間に接続されている。
17 is a heat exchanger 2 One end of this heat exchanger is connected to the gas extraction pipe 22 provided at the upper part of the cooling zone A of the lime kiln 2 by an inlet pipe 22, and the other end is connected to the is connected to the fine powder collection device 12 via the fan 19 and the inlet pipe 22.
and the induction fan 15.

熱交換器17に用いられる冷却用の空気はファ/20を
介して供給され、熱交換器17内において、前記冷却帯
Aから吸引されるドライエヤーとの熱交換を行ない、加
熱された冷却用空気は焼成用バーナ21の燃焼用空気と
して用いられる。
The cooling air used in the heat exchanger 17 is supplied through the fan/20, and within the heat exchanger 17, heat exchange is performed with the dry air sucked from the cooling zone A, and the heated cooling air is heated. is used as combustion air for the firing burner 21.

冷却帯Aに吹き込まれる冷却用空気は、燃焼後の生石灰
に対する冷却作用を与えるが、高温の生石灰と接触する
ことにより2例えばろ50℃〜400℃前後に加熱され
ており、この空気が熱交換器17側へ導かれ、熱交換が
行なわれて70〜80℃前後の空気となり2分級機1o
側の搬送用空気および分級用空気としで用いらねる。
The cooling air blown into the cooling zone A has a cooling effect on the quicklime after combustion, but when it comes into contact with the high-temperature quicklime, it is heated to, for example, 50°C to 400°C, and this air is used for heat exchange. The air is guided to the container 17 side, heat exchange is performed, and the air becomes around 70 to 80℃.2 Classifier 1o
It is used as conveying air and classification air on the side.

本実施例では1以上のように構成さ′i1ており。In this embodiment, there are one or more i1.

密閉系の装置内において、搬送用の空気および分級用の
空気として1石灰焼成炉の冷却帯の空気を用いており、
従来のように窒素カスや脱湿装置によって脱湿した空気
を用いなくて済み、極めて経済的である。
In the closed system, air from the cooling zone of the lime kiln is used as transport air and classification air.
It is extremely economical because there is no need to use nitrogen scum or air dehumidified by a dehumidifier as in the conventional method.

又、冷却用の空気は焼成直後の旨温の生石灰と接触する
ため、含まれていた水分が完全に除去され、脱湿状態と
なったドライエヤーとなっているため、このドライエヤ
ーを分級機例の搬送用空気および分級用空気として利用
すれば、生石灰と空気中の水分との接触は全く無く、焼
成さねた生石灰が水と反応して消石灰となってしまうと
いう現象は全く生じることがない。
In addition, since the cooling air comes into contact with the hot quicklime immediately after firing, the moisture contained in it is completely removed and the dry air is in a dehumidified state. When used as conveying air and classification air, there is no contact between quicklime and moisture in the air, and the phenomenon that burned quicklime reacts with water to become slaked lime never occurs.

第2図は本発明の他の実施例を説明するもので。FIG. 2 illustrates another embodiment of the invention.

図中、第1図と同一部分には同一符号を付し、その説明
は省略する。
In the figure, the same parts as in FIG. 1 are given the same reference numerals, and the explanation thereof will be omitted.

本実施例にあっては、熱交換器17の冷却媒体として空
気を用いず、水を用いている。この水は。
In this embodiment, water is used as the cooling medium for the heat exchanger 17 instead of air. This water.

石灰焼成炉2の冷却帯Aから吸引された高温のドライエ
ヤーと熱交換されるため、蒸気又は温水となって排出さ
れるが、これらは回収されて熱源その他として利用する
ことができる。23はポンプなどの送水機である。
Since heat is exchanged with the high-temperature dry air sucked from the cooling zone A of the lime kiln 2, it is discharged as steam or hot water, which can be recovered and used as a heat source or other purposes. 23 is a water supply device such as a pump.

以トの説明から明らかなように4本発明によれば1密閉
系の装置において1分級機側の微粉搬送用や分級用の空
気として石灰焼成炉の冷却帯から吸引されたドライエヤ
ーを利用しているため、焼成された生石灰と空気中の水
分との接触は生じず。
As is clear from the following explanation, according to the present invention, dry air sucked from the cooling zone of a lime kiln is used as air for transporting fine powder and for classification on the classifier side in a closed system device. Because of this, there is no contact between the calcined quicklime and moisture in the air.

生石灰が水と反応して消石灰となってしまうという欠点
は全く生じない。
There is no disadvantage that quicklime reacts with water to become slaked lime.

又、搬送用や分級用の空気として石灰焼成炉側から吸引
される空気を利用しているため、窒素ガスや別個の脱湿
装置から得られた空気を利用する必要がなく、大幅なコ
ストダウンと装置の簡略化が実現できる。
In addition, since air sucked from the lime kiln side is used as air for transportation and classification, there is no need to use nitrogen gas or air obtained from a separate dehumidification device, resulting in significant cost reductions. This makes it possible to simplify the equipment.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図および第2図は本発明のそれぞれ異なった実施例
を示す概略構成図である。 2・ ・・焼成炉、乙・・・・冷却空気吸引[1゜7.
1ろ・・・・エヤーロックダンパ、9・・・・粉砕機、
10・・・・分級機、12・・・・微粉補集装置、14
・・・・製品タンク、16・・・・空気用配管117・
・・・熱交換器、18・・・・カス抽出口。 21・・・・バーナ、22・・・・送入管特許出願人 
宇部興産株式会社
FIGS. 1 and 2 are schematic configuration diagrams showing different embodiments of the present invention. 2. Firing furnace, B... Cooling air suction [1°7.
1Ro...Air lock damper, 9...Crusher,
10... Classifier, 12... Fine powder collection device, 14
...Product tank, 16...Air piping 117.
... Heat exchanger, 18... Dregs extraction port. 21...Burner, 22...Feed pipe Patent applicant
Ube Industries Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 石灰焼成炉と、この石灰焼成炉で焼成された生石灰を粉
砕する粉砕機と、この粉砕機によって粉砕された生石灰
を空気流に乗せて分級する分級機と1分級された微粉を
空気流にのせて運んできて微粉補集装置によって製品と
して補集する微粉補集装置を備えた生石灰の製造装置に
おいて、前記微粉補集装置と粉砕機の間を配管で接続し
、粉砕機と分級機と搬送用空気系を密閉系として外気か
ら遮断した構成にすると共に、この搬送用空気および分
級用空気として石灰焼成炉の冷却帯から吸引されたドラ
イエヤーを用いうるように1石灰焼成炉の冷却帯のガス
抽出口と微粉補集装置の後方に空気用配管の途中との間
に、送入管を設けたことを特徴とする生石灰の製造装置
A lime kiln, a crusher that crushes the quicklime fired in the lime kiln, a classifier that classifies the quicklime crushed by the crusher by placing it on an air stream, and a classifier that places the classified fine powder on an air stream. In an equipment for producing quicklime, which is equipped with a fine powder collection device that transports quicklime and collects it as a product using a fine powder collection device, the fine powder collection device and the crusher are connected by piping, and the crusher, classifier, and conveyor are connected by piping. In addition to constructing the air system as a closed system isolated from the outside air, the gas in the cooling zone of the lime calcining furnace was designed so that dry air drawn from the cooling zone of the lime calcining furnace could be used as the conveying air and classification air. A quicklime production device characterized by providing an inlet pipe between the extraction port and the middle of the air piping behind the fine powder collection device.
JP24481783A 1983-12-27 1983-12-27 Quick lime manufacturing apparatus Granted JPS60141653A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24481783A JPS60141653A (en) 1983-12-27 1983-12-27 Quick lime manufacturing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24481783A JPS60141653A (en) 1983-12-27 1983-12-27 Quick lime manufacturing apparatus

Publications (2)

Publication Number Publication Date
JPS60141653A true JPS60141653A (en) 1985-07-26
JPH0329734B2 JPH0329734B2 (en) 1991-04-25

Family

ID=17124390

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24481783A Granted JPS60141653A (en) 1983-12-27 1983-12-27 Quick lime manufacturing apparatus

Country Status (1)

Country Link
JP (1) JPS60141653A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020203630A1 (en) * 2019-03-29 2020-10-08 Jfeスチール株式会社 Method and apparatus for producing quick lime using coke dry quenching facility and heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020203630A1 (en) * 2019-03-29 2020-10-08 Jfeスチール株式会社 Method and apparatus for producing quick lime using coke dry quenching facility and heat exchanger
JPWO2020203630A1 (en) * 2019-03-29 2020-10-08
CN113614048A (en) * 2019-03-29 2021-11-05 杰富意钢铁株式会社 Method and apparatus for producing quick lime using coke dry fire extinguishing equipment and heat exchanger
EP3950634A4 (en) * 2019-03-29 2022-06-01 JFE Steel Corporation Method and apparatus for producing quick lime using coke dry quenching facility and heat exchanger

Also Published As

Publication number Publication date
JPH0329734B2 (en) 1991-04-25

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