JP2002195524A - Waste treatment facility for sintering cement - Google Patents
Waste treatment facility for sintering cementInfo
- Publication number
- JP2002195524A JP2002195524A JP2000388948A JP2000388948A JP2002195524A JP 2002195524 A JP2002195524 A JP 2002195524A JP 2000388948 A JP2000388948 A JP 2000388948A JP 2000388948 A JP2000388948 A JP 2000388948A JP 2002195524 A JP2002195524 A JP 2002195524A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- kiln
- temperature
- waste
- cement
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
- Y02P40/125—Fuels from renewable energy sources, e.g. waste or biomass
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、産業廃棄物を前処
理してセメント焼成設備に供給するセメント焼成用廃棄
物処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating cement waste, which pretreats industrial waste and supplies it to a cement burning facility.
【０００２】[0002]
【従来の技術】セメントプラントでは、図２に模式的に
示すように、回転窯式の焼成炉（ロータリーキルン１）
の上流側に、ロータリーキルンの排ガスで原料を予熱す
るサイクロン式予熱装置（サスペンションプレヒータ
２）を備え、更に、プレヒータとロータリーキルンの間
に仮焼炉３を設けたニューサスペンションプレヒータ付
きキルン（ＮＳＰキルン）が主に用いられている。この
ＮＳＰキルンは、所要燃料の５０〜６０％を仮焼炉３で
燃焼させ、粉末原料の脱炭酸反応を効率よく促進させ
て、キルンに送入するシステムであり、（１）キルン入
口原料の見掛け脱炭酸率が高く、比焼成能力がＳＰキル
ンの２倍以上に達し、生産性が高い、（２）キルン側で
の所要燃料の４０〜５０％しか焚かないため、焼成帯の
熱負荷が低く寿命が長い、（３）仮焼炉出口ガス温度が
比較的低く（例えば８５０〜９００℃）、ＮＯｘの発生
量が少ない、などの特徴を有している。2. Description of the Related Art In a cement plant, as shown schematically in FIG. 2, a rotary kiln-type firing furnace (rotary kiln 1) is used.
A cyclone type preheating device (suspension preheater 2) for preheating raw materials with exhaust gas from a rotary kiln, and a kiln with a new suspension preheater (NSP kiln) provided with a calciner 3 between the preheater and the rotary kiln Mainly used. This NSP kiln is a system in which 50 to 60% of the required fuel is burned in a calciner 3 to efficiently promote the decarboxylation reaction of the powdered raw material and feed it into the kiln. The apparent decarbonation rate is high, the specific firing capacity is more than twice that of SP kiln and the productivity is high. (2) Only 40 to 50% of the required fuel on the kiln side is fired, so the heat load of the firing zone (3) The calciner outlet gas temperature is relatively low (for example, 850 to 900 ° C.), and the amount of generated NOx is small.
【０００３】かかるＮＳＰキルンでは、サスペンション
プレヒータを構成する最上段のサイクロン式熱交換器
（以下、単にサイクロンという）の入口にセメント原料
を投入すると、投入された原料は、サイクロン内で排気
ガスと熱交換をしつつ遠心分離されサイクロン下部の逆
円錐状に細くなった下端から下方に落ちる。この原料
は、さらに下段のサイクロンの入口ガス流路に供給さ
れ、ガスに同伴されてそのサイクロンに入り遠心分離さ
れる。このように原料は、排気ガスで加熱されながら順
次下段のサイクロンに移っていき、最後に仮焼炉で仮焼
成させ、再下段のサイクロンの下部からロータリーキル
ンに供給される。In such an NSP kiln, when a cement material is introduced into an inlet of a cyclone-type heat exchanger (hereinafter simply referred to as a cyclone) at the uppermost stage constituting a suspension preheater, the introduced material becomes exhaust gas and heat in the cyclone. It is centrifuged while exchanging, and falls downward from the lower end of the inverted cyclone at the bottom of the cyclone. The raw material is further supplied to the lower cyclone inlet gas flow path, and enters the cyclone with the gas and is centrifuged. In this way, the raw materials are sequentially transferred to the lower cyclone while being heated by the exhaust gas, finally calcined in a calciner, and supplied to the rotary kiln from the lower part of the lower cyclone again.
【０００４】[0004]
【発明が解決しようとする課題】近年、自動車用タイ
ヤ、プラスチック等の産業廃棄物（以下、廃棄可燃物と
いう）が大量に発生するため、これを処理して大幅に減
量するために、ＮＳＰキルンを利用することが一部で行
われている。図２に示すように、従来は、廃棄可燃物４
（タイヤチップやプラスチック類）をロータリーキルン
１と仮焼炉３の間（例えば立上りダクト）に供給し、そ
こで焼却し、発生した灰をロータリーキルン１に供給し
てセメント原料の一部とし、燃焼排ガスをプレヒータ２
に供給して熱回収していた。In recent years, a large amount of industrial waste (hereinafter, referred to as waste combustibles) such as automobile tires and plastics is generated. The use of is being done in some places. Conventionally, as shown in FIG.
(Tire chips and plastics) are supplied between the rotary kiln 1 and the calciner 3 (for example, a rising duct) and incinerated there. Preheater 2
To recover the heat.
【０００５】しかし、かかる廃棄可燃物を立上がりダク
トに供給し、燃料として使用しても原料の仮焼には寄与
できても焼成に寄与することはできない問題点があっ
た。また、廃棄可燃物が大量の水分を含む場合には、そ
の蒸発熱によりＮＳＰキルンの運転温度が下がり、熱ロ
スとなるばかりでなく、安定操業を阻害するおそれもあ
った。However, there is a problem that even if such waste combustibles are supplied to a rising duct and used as fuel, they can contribute to calcining of raw materials but cannot contribute to firing. In addition, when the waste combustibles contain a large amount of water, the heat of evaporation lowers the operating temperature of the NSP kiln, causing not only heat loss, but also hindering stable operation.
【０００６】本発明はかかる問題点を解決するために創
案されたものである。すなわち、本発明の目的は、大量
の廃棄可燃物を処理して大幅に減量することができ、水
分による運転温度の変動が少なく、ゴミからの燃料をよ
り有効に燃料のクリンカリングに使用することでキルン
の主燃料を減らすことができるセメント焼成用廃棄物処
理装置を提供することにある。The present invention has been made to solve such a problem. That is, an object of the present invention is to treat a large amount of discarded combustibles to greatly reduce the amount thereof, reduce the fluctuation of the operating temperature due to moisture, and more effectively use fuel from garbage for fuel clinkering. It is an object of the present invention to provide a cement burning waste treatment apparatus capable of reducing the main fuel of a kiln.
【０００７】[0007]
【課題を解決するための手段】本発明によれば、廃棄可
燃物（４）を高温ガス（６）で乾留し乾留ガス（７）を
発生させる外熱式キルン（１２）と、セメント焼成設備
（５）で発生する高温の塩素バイパスガス（６ａ）と低
温のクーラー排ガス（６ｂ）とを混合した高温ガスを前
記外熱式キルンに供給する高温ガス供給装置（１４）
と、外熱式キルンで発生した乾留ガスをセメント焼成設
備のバーナー（５ａ）に供給する乾留ガス供給ライン
（１６）とを備えた、ことを特徴とするセメント焼成用
廃棄物処理装置が提供される。According to the present invention, an externally heated kiln (12) for carbonizing waste combustibles (4) with a high-temperature gas (6) to generate a carbonized gas (7), and a cement burning facility A high-temperature gas supply device (14) for supplying a high-temperature gas obtained by mixing a high-temperature chlorine bypass gas (6a) generated in (5) and a low-temperature cooler exhaust gas (6b) to the externally heated kiln (14).
And a carbonization gas supply line (16) for supplying a carbonization gas generated by the externally heated kiln to a burner (5a) of a cement calcination facility. You.
【０００８】本発明の構成によれば、外熱式キルン（１
２）により廃棄可燃物（塩素，水分を含む産業廃棄物）
を乾留し、乾留ガス供給ライン（１６）により発生した
乾留ガスをセメント焼成設備のバーナー（５ａ）に供給
するので、この乾留ガスの発熱量分のキルンの主燃料を
減らすことができる。また、外熱式キルン（１２）で処
理した乾留灰はセメント焼成設備に供給しないので、塩
素及び水分による悪影響を回避することができ、かつ大
量の廃棄可燃物を処理して大幅に減量することができ
る。According to the structure of the present invention, the externally heated kiln (1)
2) Combustible waste (industrial waste containing chlorine and water)
, And the carbonized gas generated by the carbonized gas supply line (16) is supplied to the burner (5a) of the cement sintering facility. Therefore, it is possible to reduce the main fuel of the kiln by the calorific value of the carbonized gas. In addition, since the dry distillation ash treated in the external heating kiln (12) is not supplied to the cement burning facility, it is possible to avoid the adverse effects of chlorine and moisture, and to treat a large amount of waste combustibles to greatly reduce the amount. Can be.
【０００９】本発明の好ましい実施形態によれば、前記
外熱式キルン（１２）は、中空円筒形の傾斜キルン（１
２ａ）と、該傾斜キルンを外側から間接的に加熱する加
熱ダクト（１２ｂ）とを備え、傾斜キルン内を通過する
廃棄可燃物を高温で乾留する。According to a preferred embodiment of the present invention, the externally heated kiln (12) is a hollow cylindrical inclined kiln (1).
2a), and a heating duct (12b) for indirectly heating the inclined kiln from the outside, and carbonizes waste combustibles passing through the inclined kiln at a high temperature.
【００１０】この構成により、廃棄可燃物（４）を燃焼
させることなく、かつ余分な燃料を消費することなく、
廃棄可燃物を高温で乾留し、バーナー（５ａ）での燃焼
に適した可燃ガス（乾留ガス）を発生させることができ
る。[0010] With this configuration, the waste combustible (4) is not burned and the excess fuel is not consumed.
The combustible waste can be carbonized at a high temperature to generate combustible gas (carbonized gas) suitable for combustion in the burner (5a).
【００１１】また、前記高温ガス供給装置（１４）は、
塩素バイパスガス（６ａ）とクーラー排ガス（６ｂ）を
混合して高温ガス（６）として外熱式キルンに供給する
高温ガス供給ライン（１４ａ）と、塩素バイパスガス
（６ａ）とクーラー排ガス（６ｂ）の一方又は両方に設
けられダンパー装置（１４ｂ）と、ダンパー装置を制御
して高温ガスの温度を調節する温度調節装置（１４ｃ）
とからなる。The high-temperature gas supply device (14) is
A high-temperature gas supply line (14a) for mixing a chlorine bypass gas (6a) and a cooler exhaust gas (6b) and supplying it as a high-temperature gas (6) to an external heating kiln, a chlorine bypass gas (6a) and a cooler exhaust gas (6b) A damper device (14b) provided on one or both of the above, and a temperature controller (14c) for controlling the temperature of the hot gas by controlling the damper device.
Consists of
【００１２】この構成により、約１０５０℃前後の高温
の塩素バイパスガス（６ａ）と、約２５０℃前後の低温
のクーラー排ガス（６ｂ）を混合して、廃棄可燃物の乾
留に適した約５００℃の高温ガス（６）に調節すること
ができる。With this configuration, a high-temperature chlorine bypass gas (6a) at about 1050 ° C. and a low-temperature cooler exhaust gas (6b) at about 250 ° C. are mixed to form a mixture at about 500 ° C. suitable for dry distillation of combustible waste. High temperature gas (6).
【００１３】[0013]
【発明の実施の態様】以下、本発明の好ましい実施形態
を図面を参照しつつ説明する。なお、共通する部分には
同一の符号を付し、重複した説明を省略する。DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings. Note that common portions are denoted by the same reference numerals, and redundant description will be omitted.
【００１４】図１は、本発明のセメント焼成用廃棄物処
理装置の構成図である。本発明のセメント焼成用廃棄物
処理装置１０は、外熱式キルン１２、高温ガス供給装置
１４及び乾留ガス供給ライン１６を備える。FIG. 1 is a structural view of a waste treatment apparatus for cement firing according to the present invention. The waste disposal apparatus for cement firing 10 of the present invention includes an externally heated kiln 12, a high-temperature gas supply unit 14, and a dry distillation gas supply line 16.
【００１５】外熱式キルン１２は、中空円筒形の傾斜キ
ルン１２ａと、傾斜キルン１２ａを外側から間接的に加
熱する加熱ダクト１２ｂとを備える。加熱ダクト１２ｂ
には乾留に適した高温ガス６が供給され、傾斜キルン１
２ａ内を通過する廃棄可燃物４を間接加熱して高温で乾
留し、可燃ガスである乾留ガス７を発生させる。高温ガ
ス６の温度は、廃棄可燃物４を効率よく乾留するのに適
した温度（例えば約５００℃前後）であるのがよい。The external heat type kiln 12 includes a hollow cylindrical inclined kiln 12a and a heating duct 12b for indirectly heating the inclined kiln 12a from outside. Heating duct 12b
Is supplied with high-temperature gas 6 suitable for dry distillation, and the inclined kiln 1
The waste combustibles 4 passing through 2a are indirectly heated and carbonized at a high temperature to generate carbonized gas 7 as combustible gas. The temperature of the high-temperature gas 6 is preferably a temperature (for example, about 500 ° C.) suitable for efficiently carbonizing the waste combustibles 4.
【００１６】高温ガス供給装置１４は、高温ガス供給ラ
イン１４ａ、ダンパー装置１４ｂ及び温度調節装置１４
ｃからなる。高温ガス供給ライン１４ａは、ロータリー
キルン１又は仮焼炉３で発生した塩素ガスの滞留を防ぐ
ためにプレヒータ２から抜き出される高温（約１０５０
℃前後）の塩素バイパスガス６ａとクリンカークーラー
５ｂを出た低温（約２５０℃前後）のクーラー排ガス６
ｂを混合して高温ガス６として外熱式キルン１２に供給
するガスラインである。また、ダンパー装置１４ｂは、
塩素バイパスガス６ａとクーラー排ガス６ｂの一方又は
両方（この例では両方）に設けられ、各ラインの流量を
調節するようになっている。更に、温度調節装置１４ｃ
は、高温ガス６の温度を検出する温度検出器を備え、ダ
ンパー装置１４ｂを制御して高温ガス６の温度を調節す
る。なお、この図で、１４ｄは、高温ガス供給ライン１
４ａのガスの一部を外部に放出するためのダンパー装置
である。The hot gas supply device 14 includes a hot gas supply line 14a, a damper device 14b, and a temperature control device 14
c. The high-temperature gas supply line 14a is provided with a high-temperature (about 1050) drawn from the preheater 2 in order to prevent stagnation of chlorine gas generated in the rotary kiln 1 or the calciner 3.
C.) and a low-temperature (about 250.degree. C.) cooler exhaust gas 6 leaving the clinker cooler 5b.
b is a gas line that mixes b and supplies it as a high-temperature gas 6 to the externally heated kiln 12. In addition, the damper device 14b
It is provided in one or both (in this example, both) of the chlorine bypass gas 6a and the cooler exhaust gas 6b, and adjusts the flow rate of each line. Further, the temperature control device 14c
Is provided with a temperature detector for detecting the temperature of the high-temperature gas 6, and controls the damper device 14b to adjust the temperature of the high-temperature gas 6. In this figure, 14d is the hot gas supply line 1
4a is a damper device for discharging a part of the gas to the outside.
【００１７】乾留ガス供給ライン１６は、外熱式キルン
１２で発生した乾留ガス７をセメント焼成設備５のバー
ナー５ａに供給する。なお、このバーナー５ａには、主
燃料９も供給され、主燃料９と乾留ガス７の両方を同一
のバーナーで燃焼させるようになっている。なお、主燃
料９用のバーナー５ａの他に、乾留ガス７用のバーナー
を別に設けてもよい。The carbonization gas supply line 16 supplies the carbonization gas 7 generated in the externally heated kiln 12 to the burner 5 a of the cement sintering facility 5. The main fuel 9 is also supplied to the burner 5a, and both the main fuel 9 and the carbonization gas 7 are burned by the same burner. In addition to the burner 5a for the main fuel 9, a burner for the carbonization gas 7 may be separately provided.
【００１８】上述した本発明の構成によれば、外熱式キ
ルン１２により廃棄可燃物４（塩素，水分を含む産業廃
棄物）を乾留し、乾留ガス供給ライン１６により発生し
た乾留ガス７をセメント焼成設備５のバーナー５ａに供
給するので、この乾留ガス７の発熱量分のキルンの主燃
料を減らすことができる。また、外熱式キルン１２で処
理した乾留灰はセメント焼成設備５に供給しないので、
水分による悪影響を回避することができ、かつ大量の廃
棄可燃物を処理して大幅に減量することができる。According to the configuration of the present invention described above, the combustible waste 4 (industrial waste containing chlorine and water) is carbonized by the external heating kiln 12, and the carbonized gas 7 generated by the carbonized gas supply line 16 is converted into cement. Since the fuel is supplied to the burner 5a of the baking equipment 5, the main fuel of the kiln can be reduced by the calorific value of the dry distillation gas 7. Also, the dry distillate ash treated in the external heating kiln 12 is not supplied to the cement sintering facility 5,
The adverse effects of moisture can be avoided and a large amount of waste combustibles can be treated to significantly reduce weight.
【００１９】なお、本発明は上述した実施形態に限られ
るものではなく、発明の要旨を逸脱しない範囲で種々の
変更が可能である。It should be noted that the present invention is not limited to the above-described embodiment, and various changes can be made without departing from the gist of the invention.
【００２０】[0020]
【発明の効果】上述したように、本発明によれば、ゴミ
（廃棄可燃物）の乾留ガスをセメント焼成キルンのバー
ナで燃焼させることで、高温（約１４００℃前後）のフ
レームを形成することができ、セメント原料に対してよ
り効率的に熱を伝達することができる。すなわち、セメ
ント原料の焼成部分ではバーナでフレームを形成させる
必要があるがセメントキルンに直接ゴミを投入する方法
ではフレームを作ることはできず、本発明によってそれ
を可能とすることでより良いゴミ（乾留ガス）の有効利
用となる。As described above, according to the present invention, a high-temperature (about 1400 ° C.) frame is formed by burning the carbonized gas of refuse (combustible waste) with the burner of a cement firing kiln. Heat can be more efficiently transferred to the cement raw material. That is, it is necessary to form a frame with a burner in the portion where the cement raw material is fired, but it is not possible to form a frame by directly adding garbage to the cement kiln. Effective use of carbonized gas).
【００２１】従って、本発明のセメント焼成用廃棄物処
理装置は、大量の廃棄可燃物を処理して大幅に減量する
ことができ、水分による運転温度の変動が少なく、ゴミ
からの燃料をより有効に燃料のクリンカリングに使用す
ることでキルンの主燃料を減らすことができる、等の優
れた効果を有する。Accordingly, the waste disposal apparatus for cement firing according to the present invention can treat a large amount of waste combustibles to greatly reduce the amount of waste, has less fluctuation in operating temperature due to moisture, and can more effectively use fuel from waste. By using it for fuel clinker, the main fuel of the kiln can be reduced.
【図１】本発明のセメント焼成用廃棄物処理装置の構成
図である。FIG. 1 is a configuration diagram of a waste treatment apparatus for cement firing according to the present invention.
【図２】従来のＮＳＰキルンの全体構成図である。FIG. 2 is an overall configuration diagram of a conventional NSP kiln.
１ 焼成炉（ロータリーキルン）、２ サスペンション
プレヒータ、３ 仮焼炉、４ 産業廃棄物（廃棄可燃
物）、５ セメント焼成設備、５ａ バーナー、５ｂ
クリンカクーラー、６ 高温ガス、６ａ 塩素バイパス
ガス、６ｂ クーラー排ガス、７ 乾留ガス、８ａ，８
ｂ 排ガス処理装置、９ 主燃料、１０ セメント焼成
用廃棄物処理装置、１２ 外熱式キルン、１２ａ 傾斜
キルン、１２ｂ 加熱ダクト、１４ 高温ガス供給装
置、１４ａ 高温ガス供給ライン、１４ｂ ダンパー装
置、１４ｃ 温度調節装置、１６ 乾留ガス供給ライン1 firing furnace (rotary kiln), 2 suspension preheater, 3 calciner, 4 industrial waste (waste combustible), 5 cement firing equipment, 5a burner, 5b
Clinker cooler, 6 High temperature gas, 6a Chlorine bypass gas, 6b Cooler exhaust gas, 7 Carbonization gas, 8a, 8
b Exhaust gas treatment device, 9 Main fuel, 10 Waste treatment device for cement burning, 12 External heating kiln, 12a Inclined kiln, 12b Heating duct, 14 Hot gas supply device, 14a Hot gas supply line, 14b Damper device, 14c Temperature Controller, 16 carbonization gas supply line
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 ＦＩ テーマコート゛(参考） Ｆ２７Ｂ 7/08 Ｆ２７Ｂ 7/08 ４Ｋ０６１ 7/36 7/36 Ｆ２７Ｄ 17/00 １０１ Ｆ２７Ｄ 17/00 １０１Ｚ １０４ １０４Ｋ 19/00 19/00 Ｚ Ｆターム(参考） 3K061 AA07 AB02 AC13 AC14 CA01 FA10 FA21 KA02 KA16 3K065 AA07 AB02 AC13 AC14 JA13 JA16 3K078 BA08 CA02 CA07 CA21 CA24 4D004 AA07 AA11 BA03 CA27 CB09 CB34 CB42 DA02 DA06 4K056 AA16 BA02 DA02 DA17 DC17 FA08 4K061 AA08 BA12 DA07 FA02 FA03 FA06 GA10 HA05 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F27B 7/08 F27B 7/08 4K061 7/36 7/36 F27D 17/00 101 F27D 17/00 101Z 104 104K 19/00 19/00 ZF term (reference) 3K061 AA07 AB02 AC13 AC14 CA01 FA10 FA21 KA02 KA16 3K065 AA07 AB02 AC13 AC14 JA13 JA16 3K078 BA08 CA02 CA07 CA21 CA24 4D004 AA07 AA11 BA03 CA27 CB09 CB34 CB42 DA02 DA06 DA02 DA02 A02 DC17 FA08 4K061 AA08 BA12 DA07 FA02 FA03 FA06 GA10 HA05
Claims (3)
留し乾留ガス（７）を発生させる外熱式キルン（１２）
と、セメント焼成設備（５）で発生する高温の塩素バイ
パスガス（６ａ）と低温のクーラー排ガス（６ｂ）とを
混合した高温ガスを前記外熱式キルンに供給する高温ガ
ス供給装置（１４）と、外熱式キルンで発生した乾留ガ
スをセメント焼成設備のバーナー（５ａ）に供給する乾
留ガス供給ライン（１６）とを備えた、ことを特徴とす
るセメント焼成用廃棄物処理装置。An external heat kiln (12) for carbonizing waste combustibles (4) with a high-temperature gas (6) to generate a carbonized gas (7).
A high-temperature gas supply device (14) for supplying a high-temperature gas obtained by mixing a high-temperature chlorine bypass gas (6a) and a low-temperature cooler exhaust gas (6b) generated in a cement firing facility (5) to the external heat type kiln; And a dry distillation gas supply line (16) for supplying dry distillation gas generated in the external heating kiln to a burner (5a) of a cement firing facility.
形の傾斜キルン（１２ａ）と、該傾斜キルンを外側から
間接的に加熱する加熱ダクト（１２ｂ）とを備え、傾斜
キルン内を通過する廃棄可燃物を高温で乾留する、こと
を特徴とする請求項１に記載のセメント焼成用廃棄物処
理装置。2. The external heat type kiln (12) includes a hollow cylindrical inclined kiln (12a) and a heating duct (12b) for indirectly heating the inclined kiln from the outside. The waste treatment apparatus for cement burning according to claim 1, wherein the passing combustible waste is carbonized at a high temperature.
バイパスガス（６ａ）とクーラー排ガス（６ｂ）を混合
して高温ガス（６）として外熱式キルンに供給する高温
ガス供給ライン（１４ａ）と、塩素バイパスガス（６
ａ）とクーラー排ガス（６ｂ）の一方又は両方に設けら
れダンパー装置（１４ｂ）と、ダンパー装置を制御して
高温ガスの温度を調節する温度調節装置（１４ｃ）とか
らなる、ことを特徴とする請求項１に記載のセメント焼
成用廃棄物処理装置。3. A high-temperature gas supply line (14a) for mixing a chlorine bypass gas (6a) and a cooler exhaust gas (6b) and supplying the mixture as a high-temperature gas (6) to an external heating kiln. ) And chlorine bypass gas (6
a) and a damper device (14b) provided in one or both of the cooler exhaust gas (6b) and a temperature control device (14c) for controlling the temperature of the hot gas by controlling the damper device. The waste treatment device for cement firing according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000388948A JP4360477B2 (en) | 2000-12-21 | 2000-12-21 | Waste treatment equipment for cement firing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000388948A JP4360477B2 (en) | 2000-12-21 | 2000-12-21 | Waste treatment equipment for cement firing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002195524A true JP2002195524A (en) | 2002-07-10 |
| JP4360477B2 JP4360477B2 (en) | 2009-11-11 |
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ID=18855599
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000388948A Expired - Lifetime JP4360477B2 (en) | 2000-12-21 | 2000-12-21 | Waste treatment equipment for cement firing |
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| JP (1) | JP4360477B2 (en) |
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|---|---|---|---|---|
| JP2006206752A (en) * | 2005-01-28 | 2006-08-10 | Mitsubishi Materials Corp | System of producing fuel from waste in cement manufacturing facility and cement manufacturing method using system of producing fuel from waste |
| JP2008280244A (en) * | 2008-07-18 | 2008-11-20 | Sumitomo Osaka Cement Co Ltd | Method of processing organic based waste |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2006206752A (en) * | 2005-01-28 | 2006-08-10 | Mitsubishi Materials Corp | System of producing fuel from waste in cement manufacturing facility and cement manufacturing method using system of producing fuel from waste |
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| CN100451519C (en) * | 2006-12-31 | 2009-01-14 | 北京市琉璃河水泥有限公司 | Residual heat generating system used for new type nonaqueous cement production line |
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| JP2010043269A (en) * | 2009-09-24 | 2010-02-25 | Sumitomo Osaka Cement Co Ltd | Method for treating biomass |
| JP2010155779A (en) * | 2010-01-28 | 2010-07-15 | Mitsubishi Materials Corp | Method for treatment of halogen-containing waste material using cement production facility |
| CN104236304A (en) * | 2014-09-29 | 2014-12-24 | 南京新中磁电技术工程有限公司 | Novel external heating type gas rotary kiln |
| CN104236304B (en) * | 2014-09-29 | 2016-11-30 | 南京新中磁电技术工程有限公司 | A kind of Novel external heat type combustion gas rotary kiln |
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| JP2021098619A (en) * | 2019-12-20 | 2021-07-01 | 太平洋セメント株式会社 | Fuel-producing apparatus and fuel-producing method for combustible waste |
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