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JPS593950B2 - How to make quicklime - Google Patents

How to make quicklime

Info

Publication number
JPS593950B2
JPS593950B2 JP16582380A JP16582380A JPS593950B2 JP S593950 B2 JPS593950 B2 JP S593950B2 JP 16582380 A JP16582380 A JP 16582380A JP 16582380 A JP16582380 A JP 16582380A JP S593950 B2 JPS593950 B2 JP S593950B2
Authority
JP
Japan
Prior art keywords
quicklime
rotary kiln
preheating furnace
burner
ore
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
Application number
JP16582380A
Other languages
Japanese (ja)
Other versions
JPS5678459A (en
Inventor
ミドリ 井上
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP16582380A priority Critical patent/JPS593950B2/en
Publication of JPS5678459A publication Critical patent/JPS5678459A/en
Publication of JPS593950B2 publication Critical patent/JPS593950B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は石灰石および(または)ドロマイトからの生石
灰の製造に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the production of quicklime from limestone and/or dolomite.

石灰石は炭酸カルシウムを、ドロマイトは炭酸カルシウ
ムと炭酸ムグネシウムとの複合物を夫々主成とする天然
の鉱物資源で、本発明はこれらの鉱物を焼成して生石灰
を製造する方法である。
Limestone is a natural mineral resource mainly composed of calcium carbonate, and dolomite is a composite of calcium carbonate and magnesium carbonate, respectively, and the present invention is a method for producing quicklime by calcining these minerals.

従来、生石灰を製造するには竪形針、あるいはロータリ
ーキルンにより石灰石を焼成していた。
Traditionally, quicklime was produced by burning limestone in a vertical kiln or a rotary kiln.

竪形針の場合は直径が約100mm!以上の天然の原石
を用い、また直径30〜501の石炭、特に無煙炭を使
用して炉内の口塞りを防止し、原料の完全焼成を行って
いた。
In the case of a vertical needle, the diameter is approximately 100mm! The raw materials were completely fired by using the above-mentioned natural raw stones and by using coal, especially anthracite, with a diameter of 30 to 50 mm to prevent the furnace from clogging.

しかしこの方法では原料が大塊のため焼成に時間を要し
、不完全焼成となり易く、かつ回分方法であるため、生
産量も、たとえば1回につき30屯位が限度で能率が極
めて悪かった。
However, in this method, since the raw materials are in large chunks, it takes time to fire them, tends to result in incomplete firing, and since it is a batch method, the production volume is limited to, for example, 30 tons per batch, which is extremely inefficient.

一方ロータリーキルンによる場合は原石を重油バーナー
で焼成するので、石油の大量消費とその経費の膨張に悩
まされた。
On the other hand, when using a rotary kiln, the raw ore is burned in a heavy oil burner, resulting in large amounts of oil consumption and increased costs.

本発明は上記従来技術の欠点を解消するために研究した
もので、その主要な目的な生石灰の焼成方法を合理化し
てエネルギーの節約を図る番と在る。
The present invention was developed to solve the above-mentioned drawbacks of the prior art, and its main purpose is to streamline the quicklime sintering method to save energy.

さらにこれを詳細に説明すれば、本発明は竪形予熱炉と
、ローターキルンとを組み合せて連続作業を実施する方
法で、そのため竪形予熱炉内に粉状乃至粒状の石炭また
はコークスと、原料鉱石の20〜50へ粉砕物との均密
に混合した焼成すべき材料を装入し、空気を充分に供給
しながら約800Q−約1000℃で焼成し、全体の約
70係を焼成して下方のロータリーキルンに移行させる
To explain this in more detail, the present invention is a method of performing continuous operation by combining a vertical preheating furnace and a rotor kiln. The materials to be fired, which were intimately mixed with the crushed material, were charged into 20 to 50 parts of the ore, and fired at about 800 Q - about 1000 °C while supplying sufficient air, and about 70 parts of the whole were fired. Transfer to the rotary kiln below.

ロータリーキルン内ではバーナーの火焔を放射して内容
物の湯度を約1000℃に保持して焼成を完結させる。
Inside the rotary kiln, the flame from the burner is radiated to maintain the temperature of the contents at about 1000°C to complete the firing.

この方法を能率的に実施するためには原料及び固形燃料
の粒状化と材料の均密な混合、充分な空気の送入、口塞
りを起させずに材料の下方への徐々な移動を竪形予熱炉
で実施することにより焼成温度を約800’−1000
℃の範囲内で焼成せしめることが必要である。
In order to carry out this method efficiently, it is necessary to granulate the raw materials and solid fuel, mix the materials homogeneously, introduce sufficient air, and gradually move the materials downward without causing blockage. Firing temperature is approximately 800'-1000 by performing in a vertical preheating furnace.
It is necessary to carry out firing within the range of ℃.

そして全体の約70係が竪形予熱炉で焼成されるよう焼
成速度を調節する。
Then, the firing speed is adjusted so that about 70 pieces of the total are fired in the vertical preheating furnace.

ロータリーキルン内での焼成は後方に取り付けたバーナ
ーから微粉炭を噴出させ、これに着火した火焔により焼
成温度約1000℃を保持して行われることは前記のよ
うであり、これによって石油に替えて石炭資源の有効な
利用を行うことも本発明の別の目的であり、またロータ
リーキルンは回転速度を調整して焼成材料の滞留時間を
調節し、これにより焼成を完結せしめることが可能であ
る。
As mentioned above, pulverized coal is ejected from a burner installed at the rear of the rotary kiln, and the ignited flame maintains the firing temperature at approximately 1,000°C. It is another object of the present invention to make effective use of resources, and the rotation speed of the rotary kiln can be adjusted to adjust the residence time of the firing material, thereby completing the firing.

本発明の実施例を添付図面により説明すると、1はホッ
パーで、原料石灰石及び(または)ドロマイトを主成分
とする天然鉱石原料を予め20%〜50%の小塊に破砕
して投入する。
An embodiment of the present invention will be described with reference to the accompanying drawings. Reference numeral 1 denotes a hopper into which a natural ore material containing limestone and/or dolomite as a main component is crushed in advance into small pieces of 20% to 50% and then charged.

鉱石原料を小塊にすることは、前記のように焼成を容易
にし、かつ予熱炉の収容量を増大するためにも必要であ
る。
Forming the ore raw material into small agglomerates is necessary to facilitate calcination as described above and also to increase the capacity of the preheating furnace.

2もまたホッパーで2X以下の粒状あるいは粉状の石炭
またはコークスを投入する。
2 is also a hopper into which 2X or less granular or powdered coal or coke is charged.

ついで細粒にした鉱石原料と粉状石炭またはコークスと
を3で均密に混合して、燃焼効率を高める。
Next, the finely granulated ore raw material and powdered coal or coke are mixed homogeneously in Step 3 to increase combustion efficiency.

また粉状石炭の利用によりコストも安価で入手も容易で
ある。
Furthermore, the use of powdered coal is inexpensive and easily available.

次に混合した原料と粉状石炭またはコークスとを予熱炉
4内に投入する。
Next, the mixed raw materials and powdered coal or coke are put into the preheating furnace 4.

予熱炉は初め着火しなければならないが、後は常時燃焼
が継続しているので、そのまま投入すればよい。
The preheating furnace must first be ignited, but after that the combustion continues all the time, so you can simply put it into the furnace.

現在、試用中の予熱炉は大きさ直径6m、高さ20mの
炉で約−昼夜で燃焼率70チに達し、順次下方のロータ
リーキルン5に移行させる。
The preheating furnace currently being tested is a furnace with a diameter of 6 m and a height of 20 m, which reaches a combustion rate of about 70 inches in day and night, and will be gradually transferred to the rotary kiln 5 below.

ロータリーキルン5ではキルンを回転しムラ焼を防止し
ながら後方よりバーナー6で完全に内容物を焼成して生
石灰を製造する。
In the rotary kiln 5, the contents are completely burned with a burner 6 from the rear while rotating the kiln to prevent uneven firing to produce quicklime.

このバーナー6は焼成温度の降下を防止するものであり
、その燃料は従来通り重油を用いてもよいが、前記のよ
うに微粉炭を用いて費用を節約するとともに石油資源を
節約することもできる。
This burner 6 prevents the firing temperature from dropping, and its fuel may be conventional heavy oil, but as mentioned above, pulverized coal can be used to save costs and petroleum resources. .

焼成した生石灰はロータリーキルンより排出され、下方
に配設した網目10%角の金網7により10へ以上の塊
状の生石灰と10%未満の粉状の生石灰に篩分けられる
The burned quicklime is discharged from the rotary kiln and is sieved by a wire mesh 7 with a mesh size of 10% square arranged below into lumpy quicklime with a size of 10% or more and powdery quicklime with a size of less than 10%.

篩分けられた10〜以上の塊状の生石灰はそのまま用い
、10へ未満の粉状の生石灰は水和して消石灰として用
いる。
The sifted quicklime in the form of lumps of 10 or more is used as is, and the powder quicklime of less than 10 is hydrated and used as slaked lime.

以上述べてきたようにこの発明は予熱炉とロータリーキ
ルンとを組合せて使用することを1つの特徴とし、これ
により連続作業を可能とし、燃料費の節約及び生産量の
増大をもたらす。
As described above, one feature of the present invention is the use of a preheating furnace and a rotary kiln in combination, which enables continuous operation, resulting in fuel cost savings and increased production.

また天然原料と粉末の石炭を一定粒径に破砕し、かつ均
密に混合して燃焼効率を高めかつ燃料の有効利用を図る
ことができる等資源節約時代にマツチした効果を奏する
In addition, natural raw materials and powdered coal can be crushed to a certain particle size and mixed homogeneously to increase combustion efficiency and effectively utilize fuel, making it suitable for the era of resource conservation.

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

図はこの発明を説明するための全体図である。 1・・・・・・原料ホッパー、2・・・・・・石炭ホッ
パー、3・・・・・・混合部分、4・・・・・・予熱炉
、5・・・・・・ロータリーキルン、6・・・・・・バ
ーナー、I・・・・・・金網。
The figure is an overall view for explaining the present invention. 1... Raw material hopper, 2... Coal hopper, 3... Mixing section, 4... Preheating furnace, 5... Rotary kiln, 6 ...Burner, I...Wire mesh.

Claims (1)

【特許請求の範囲】[Claims] 1 石灰石および(または)ドロマイトを主成分として
含む鉱石を20〜50〜に粉砕し、該鉱石との混合率が
5〜10係になるように石炭及びコークスのうちから選
れた粉状乃至粒状の固形燃料を均密に混合し、該混合材
料を竪形予熱炉内で十分な空気を通人しなから力焼温度
範囲800°〜1000℃において約70チの焼成を行
い、次にロータリーキルンに移行し、バーナーの火焔に
より焼成を完結させ、生成物を冷却、収取することを特
徴とする生石灰を製造する方法。
1. Powdered or granular ore containing limestone and/or dolomite as a main component is crushed to 20 to 50 parts, and the mixture ratio with the ore is 5 to 10 parts.Powder or granule selected from coal and coke of solid fuel are homogeneously mixed, and the mixed material is calcined in a vertical preheating furnace for about 70 inches at a power firing temperature range of 800° to 1000°C with sufficient air passing through, and then heated in a rotary kiln. A method for producing quicklime, which is characterized in that the calcination is completed by the flame of a burner, and the product is cooled and collected.
JP16582380A 1980-11-27 1980-11-27 How to make quicklime Expired JPS593950B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16582380A JPS593950B2 (en) 1980-11-27 1980-11-27 How to make quicklime

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16582380A JPS593950B2 (en) 1980-11-27 1980-11-27 How to make quicklime

Publications (2)

Publication Number Publication Date
JPS5678459A JPS5678459A (en) 1981-06-27
JPS593950B2 true JPS593950B2 (en) 1984-01-26

Family

ID=15819670

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16582380A Expired JPS593950B2 (en) 1980-11-27 1980-11-27 How to make quicklime

Country Status (1)

Country Link
JP (1) JPS593950B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60124456U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 construction lifting equipment
JPS60124455U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 Frame structure for crane installation
JPS60124457U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 construction lifting equipment
JPS60124454U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 construction lifting equipment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60124456U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 construction lifting equipment
JPS60124455U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 Frame structure for crane installation
JPS60124457U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 construction lifting equipment
JPS60124454U (en) * 1984-01-31 1985-08-22 ナショナル住宅産業株式会社 construction lifting equipment

Also Published As

Publication number Publication date
JPS5678459A (en) 1981-06-27

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