JPS6065750A - Cement calcining apparatus using fuel containing large quantity of ash content - Google Patents

Cement calcining apparatus using fuel containing large quantity of ash content

Info

Publication number
JPS6065750A
JPS6065750A JP17312883A JP17312883A JPS6065750A JP S6065750 A JPS6065750 A JP S6065750A JP 17312883 A JP17312883 A JP 17312883A JP 17312883 A JP17312883 A JP 17312883A JP S6065750 A JPS6065750 A JP S6065750A
Authority
JP
Japan
Prior art keywords
ash
combustion furnace
fuel containing
cement
cyclone
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
JP17312883A
Other languages
Japanese (ja)
Inventor
小川 恵右
長岡 光雄
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP17312883A priority Critical patent/JPS6065750A/en
Publication of JPS6065750A publication Critical patent/JPS6065750A/en
Pending legal-status Critical Current

Links

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、低質炭、ボタ、産業廃棄物などの灰分を多く
含む燃料を利用するセメント仮焼装置に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a cement calcination device that utilizes fuel containing a large amount of ash such as low quality coal, bottons, and industrial waste.

従来から、灰分を多く含む燃料を利用してセメント原料
を仮焼することについては、種々研料を仮焼炉へ直接供
給し、仮焼炉の内部で燃焼させるようにしている。した
がって、その灰分はセメント原料に混合され、セメント
クリンカの原料の一部となり、クリンカ生産量が増加す
るという利点があるが、その多量の灰分を考慮してのク
リンカ組成の管理、つまり、クリンカ品質を管理するの
が、きわめて困難である。すなわち、運転に際しては、
仮焼炉出口ガス温度を所定値に保持する関係からして、
吹込み燃料の量は、クリンカの焼成に必要な熱量の変化
に応じて増減し、クリンカ品質に対する影響を除くこと
ができないし、また灰分量が多過ぎて、原料配合上該当
燃料量を抑えなければならなくなる場合も生じる。
Conventionally, in calcining cement raw materials using fuel containing a large amount of ash, various types of abrasives have been directly supplied to a calciner and burned within the calciner. Therefore, the ash content is mixed into the cement raw material and becomes part of the cement clinker raw material, which has the advantage of increasing clinker production. is extremely difficult to manage. In other words, when driving,
From the perspective of maintaining the calciner outlet gas temperature at a predetermined value,
The amount of injected fuel increases or decreases depending on the change in the amount of heat required for burning clinker, and the effect on clinker quality cannot be eliminated.Also, the amount of ash content is too high, and the amount of fuel must be suppressed when blending the raw materials. There may be cases where this is not possible.

本発明は、セメント製造分野における燃料費を低減のた
めに、石炭、とくに、低品質炭、ボタ、オイルシェール
、可燃分を含む産業廃棄物などを利用するとき、セメン
トクリンカの品質に悪影響を与えずにそれら燃料の熱量
を有効利集することができ、二次的副産物として得られ
る前記灰分をクリンカの増量剤として利用し得るセメン
ト仮焼装置を提供することを目的とするものである。
The present invention aims to reduce fuel costs in the field of cement production by using coal, especially low-quality coal, coal, oil shale, industrial waste containing combustibles, etc., which adversely affects the quality of cement clinker. It is an object of the present invention to provide a cement calcination device that can effectively collect the heat of the fuel without causing any problems, and can utilize the ash obtained as a secondary by-product as an extender for clinker.

このため、本発明の構成は、クリンカクーラからの高温
空気を仮焼炉へ供給する高温空気ダクトの途中に設けら
れた集じん性能を有する燃焼炉を備え、かつ、前記燃焼
炉には、灰分を多く含む燃料を燃焼させるバーナと、該
燃焼炉で捕集された灰分を系外に排出する灰分排出シュ
ートとを有することを特徴としている。
Therefore, the configuration of the present invention includes a combustion furnace having dust collection performance provided in the middle of a high-temperature air duct that supplies high-temperature air from a clinker cooler to a calciner, and the combustion furnace has an ash content. The combustion furnace is characterized by having a burner that burns fuel containing a large amount of ash, and an ash discharge chute that discharges ash collected in the combustion furnace to the outside of the system.

以下、本発明の一実施例について、図面を参照しながら
説明する。
An embodiment of the present invention will be described below with reference to the drawings.

図において、1はサスペンションプレヒータ、2は該プ
レヒータ1の最下段サイクロン、3は仮焼炉、4はロー
タリキルン、5はクリンカクー2.6は該クーラ5から
の高温空気を前記仮焼炉3の燃焼用二次空気として供給
する高温空気ダクト、7は粉末のセメント原料供給装置
、8は仮焼原料供給シュート、9は排気ダクト、10は
キルン立上シダクト、11は前記プレヒータ1からの予
熱原料供給シュートである。また図において、実線矢印
は原料やクリンカの流れを示し、点線矢印は空気やガス
の流れを示している。このうち、矢印12は焼成された
高温のクリンカの流れを、矢印15は冷却されて製品と
なったクリンカの流れを、矢印14は該仮焼炉5からサ
イクロン2へのガスの流れを、15はそのガス流により
運搬される仮焼原料の流れを示す。また16は通常の燃
料を使用する仮焼炉バーナ、17は通常の燃料を使用す
るキルンバーナである。なお、ここまでは従来の仮焼炉
付きセメント焼成設備と同様である。
In the figure, 1 is a suspension preheater, 2 is a lowermost cyclone of the preheater 1, 3 is a calciner, 4 is a rotary kiln, 5 is a clinker cooler 2. A high temperature air duct is supplied as secondary air for combustion, 7 is a powder cement raw material supply device, 8 is a calcining raw material supply chute, 9 is an exhaust duct, 10 is a kiln start-up duct, 11 is a preheated raw material from the preheater 1 This is the supply chute. Furthermore, in the figure, solid line arrows indicate the flow of raw materials and clinker, and dotted line arrows indicate the flow of air and gas. Among these, arrow 12 indicates the flow of fired high-temperature clinker, arrow 15 indicates the flow of clinker that has been cooled and becomes a product, and arrow 14 indicates the flow of gas from the calciner 5 to the cyclone 2. indicates the flow of the calcined raw material carried by the gas flow. Further, 16 is a calciner burner that uses normal fuel, and 17 is a kiln burner that uses normal fuel. Note that the process up to this point is the same as the conventional cement firing equipment with a calcining furnace.

さらに説明すると、18は集じん性能を有する燃焼炉で
、前記高温空気ダクト乙の途中に設けられておシ、この
実施例では、サイクロン型の燃焼炉である。19は灰分
を多く含む燃料を燃焼させる燃焼炉バーナ、20は送、
風機、21はサイクロン、22は前記送風機20の吐出
側とサイクロン21の入口側とを接続しているサイクロ
ン入口空気管、23は前記燃焼炉18のダスト排出口と
サイクロン入口空気管22の途中とを接続している高温
灰分排出シュート、24は前記サイクロン21の空気出
口と高温空気ダクト6の途中とを接続しているサイクロ
ン出口空気管、25は低温灰分排出シュート、26は前
記燃焼炉18の炉壁を冷却させるために小量の大気を吸
引する大気吸引管、27は図示されていない主排風機と
サスペンションプレヒータの上部とを接続している主排
気ダクトである。
To explain further, reference numeral 18 denotes a combustion furnace having dust collection performance, which is installed in the middle of the high-temperature air duct B. In this embodiment, it is a cyclone type combustion furnace. 19 is a combustion furnace burner that burns fuel containing a large amount of ash; 20 is a feeder;
A wind fan, 21 is a cyclone, 22 is a cyclone inlet air pipe that connects the discharge side of the blower 20 and the inlet side of the cyclone 21, and 23 is a part between the dust outlet of the combustion furnace 18 and the cyclone inlet air pipe 22 24 is a cyclone outlet air pipe connecting the air outlet of the cyclone 21 and the middle of the high temperature air duct 6, 25 is a low temperature ash discharge chute, and 26 is a high temperature ash discharge chute connecting the combustion furnace 18. An atmospheric air suction pipe 27 that sucks in a small amount of atmospheric air to cool the furnace wall is a main exhaust duct that connects a main exhaust fan (not shown) and the upper part of the suspension preheater.

図示のように構成されたセメント製造設備においては、
灰分を多く含む燃料をバーナー9によシ燃焼炉18内で
燃焼させる。これにより、クリンカクー25からの60
0〜700°C程度の高温空気は1200〜1300°
C程度に昇温されて仮焼炉3に供給される。すなわち、
通常のプロセスにおける仮焼炉で必要とする熱量の1程
度の熱量を、前記灰分を多く燃料でまかならこ、L−A
げ衣スー寸か七の要分は撚修枦18で捕集され、灰分排
出シュート23から排出されるが、その灰分は高温であ
るので、その熱量を有効利用するため、サイクロン21
に導入し、送風機20からの常温空気と熱交換させる。
In the cement manufacturing equipment configured as shown in the diagram,
The fuel containing a large amount of ash is combusted in a combustion furnace 18 by a burner 9. This results in 60
High temperature air of about 0 to 700°C is 1200 to 1300°
The temperature is raised to approximately C and is supplied to the calcining furnace 3. That is,
The amount of heat required in the calciner in a normal process is about 1,000 yen by using fuel with a high ash content.
The essential parts of the grains are collected by the twister 18 and discharged from the ash discharge chute 23, but since the ash has a high temperature, the cyclone 21 is used to effectively utilize the heat.
and exchange heat with the room temperature air from the blower 20.

そしてサイクロン21で昇温した空気は、仮焼炉バーナ
16およびキルンバーナ17の一次空気としても有効利
用できるが、この実施例では。
The air heated by the cyclone 21 can also be effectively used as primary air for the calciner burner 16 and kiln burner 17, but in this embodiment.

出口空気管24から燃焼炉18の手前の高温空気ダクト
乙の途中に供給される。またサイクロン21で冷却され
た灰分は灰分排出シュート25から系外に排出されるが
、この灰分は燃料残分なので、クリンカと混合してセメ
ント粉末としても、化学反応を起こすことがなく、単な
るセメントの増量剤として利用できる。なお大気吸引管
26からの吸引空気は前述のごとく、灰分の内壁への付
着を防ぐために燃焼炉18の旋回流に沿わしめて数か所
に分割供給される。
The air is supplied from the outlet air pipe 24 to the middle of the high-temperature air duct B before the combustion furnace 18. In addition, the ash cooled by the cyclone 21 is discharged from the system through the ash discharge chute 25, but since this ash is a fuel residue, it can be mixed with clinker and used as cement powder without any chemical reaction and is just cement powder. It can be used as a bulking agent. As described above, the suction air from the atmospheric suction pipe 26 is divided and supplied to several locations along the swirling flow of the combustion furnace 18 in order to prevent ash from adhering to the inner wall.

前述のように、仮焼炉を備えたセメント焼成設備におい
ては、灰分を多く含む燃料を燃焼させてその熱量の有効
利用を図ろうとする場合に、その灰分の化学成分とセメ
ントクリ/力の化学成分が異なることの理由で、製品ク
リンカの品質(組成)悪化をまねくことが多いが、本発
明では、クリンカクーラか−らの高温空気を仮焼炉へ供
給する高温空気ダクトの途中に集じん性能を有する燃焼
炉を設けて、該燃焼炉で灰分を多く含む燃料を燃焼させ
るので、クリンカの品質低下をまねくことがなく、灰分
を多く含む燃料を良好に燃焼させてその熱量の有効利用
を図ることができ、かつ、燃焼後の燃料の灰分は該燃焼
炉で捕集して系外に取出し、製品であるセメントクリ/
力の増量剤として有効に利用することができる。
As mentioned above, in cement firing equipment equipped with a calciner, when attempting to effectively utilize the heat by burning fuel containing a large amount of ash, the chemical composition of the ash and the chemistry of the cement The quality (composition) of the product clinker often deteriorates due to different components, but in the present invention, dust is not collected in the middle of the high-temperature air duct that supplies high-temperature air from the clinker cooler to the calciner. Since a combustion furnace with high performance is installed and the fuel containing a large amount of ash is combusted in the combustion furnace, the quality of clinker is not deteriorated, and the fuel containing a large amount of ash can be burnt well and its calorific value can be used effectively. The ash content of the fuel after combustion is collected in the combustion furnace and taken out of the system, and the cement cream product is
It can be effectively used as a force extender.

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

図は本発明の一実施例を示した説明図である。 1噛争・サスペンションブレヒータ、216・最下段サ
イクロン、3・・・仮焼炉、4・・・ロータリキル/、
5・・・クリンカクーラ、6・・・高温空気ダクト、1
8・・・燃焼炉、19・・・燃焼炉バーナ、20・・・
送風機、21・・・サイクロン、22・・・サイクロン
入口空気管、23・・・高温灰分排出シュート、24・
・・サイクロン出口空気管、25・・・低温灰分排出シ
ュート、26・・・大気吸引管。
The figure is an explanatory diagram showing one embodiment of the present invention. 1. Suspension brake heater, 216. Bottom stage cyclone, 3. Calciner, 4. Rotary kill.
5... Clinker cooler, 6... High temperature air duct, 1
8... Combustion furnace, 19... Combustion furnace burner, 20...
Blower, 21... Cyclone, 22... Cyclone inlet air pipe, 23... High temperature ash discharge chute, 24...
...Cyclone outlet air pipe, 25...Low temperature ash discharge chute, 26...Atmospheric suction pipe.

Claims (1)

【特許請求の範囲】[Claims] 1、 クリンカクーラからの高温空気を仮焼炉へ供給す
る高温空気ダクトの途中に設けられた集じん性能を有す
る燃焼炉を備え、かつ、前記燃焼炉には、灰分を多く含
む燃料を燃焼させるバーナと、該燃焼炉で捕集された灰
分を系外に排出する灰分排出シュートとを有することを
特徴とする、灰分を多く含む燃料を利用するセメント仮
焼装置。
1. A combustion furnace with dust collection performance is installed in the middle of a high-temperature air duct that supplies high-temperature air from a clinker cooler to a calciner, and the combustion furnace burns fuel containing a large amount of ash. A cement calcination device using fuel containing a large amount of ash, characterized by having a burner and an ash discharge chute for discharging ash collected in the combustion furnace to the outside of the system.
JP17312883A 1983-09-21 1983-09-21 Cement calcining apparatus using fuel containing large quantity of ash content Pending JPS6065750A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17312883A JPS6065750A (en) 1983-09-21 1983-09-21 Cement calcining apparatus using fuel containing large quantity of ash content

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17312883A JPS6065750A (en) 1983-09-21 1983-09-21 Cement calcining apparatus using fuel containing large quantity of ash content

Publications (1)

Publication Number Publication Date
JPS6065750A true JPS6065750A (en) 1985-04-15

Family

ID=15954641

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17312883A Pending JPS6065750A (en) 1983-09-21 1983-09-21 Cement calcining apparatus using fuel containing large quantity of ash content

Country Status (1)

Country Link
JP (1) JPS6065750A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01121617A (en) * 1987-11-02 1989-05-15 Ishikawajima Harima Heavy Ind Co Ltd Incinerator for industrial wastes
JP2007205640A (en) * 2006-02-02 2007-08-16 Ube Ind Ltd Combustion disposal method and its device for combustible waste

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01121617A (en) * 1987-11-02 1989-05-15 Ishikawajima Harima Heavy Ind Co Ltd Incinerator for industrial wastes
JPH0619228B2 (en) * 1987-11-02 1994-03-16 石川島播磨重工業株式会社 Industrial waste combustion equipment
JP2007205640A (en) * 2006-02-02 2007-08-16 Ube Ind Ltd Combustion disposal method and its device for combustible waste

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