JPS6158750B2 - - Google Patents

Info

Publication number
JPS6158750B2
JPS6158750B2 JP54109714A JP10971479A JPS6158750B2 JP S6158750 B2 JPS6158750 B2 JP S6158750B2 JP 54109714 A JP54109714 A JP 54109714A JP 10971479 A JP10971479 A JP 10971479A JP S6158750 B2 JPS6158750 B2 JP S6158750B2
Authority
JP
Japan
Prior art keywords
waste gas
heat exchange
firing
cold air
partition plate
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
JP54109714A
Other languages
Japanese (ja)
Other versions
JPS5634086A (en
Inventor
Masamitsu Ootsuka
Yasunao Kimura
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 JP10971479A priority Critical patent/JPS5634086A/en
Publication of JPS5634086A publication Critical patent/JPS5634086A/en
Publication of JPS6158750B2 publication Critical patent/JPS6158750B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は石灰石、ドロマイト、マグネサイトお
よびそれらに類似の原料(以下、「被焼成物」と
いう)を重油燃料あるいはガス燃料などの燃料で
焼成する廃熱回収装置(廃熱回収用の熱交換器)
を備えた二重円筒形式の竪形焼成炉に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a waste heat recovery device (waste heat exchanger for heat recovery)
This relates to a double cylindrical vertical kiln equipped with a double cylinder type vertical kiln.

従来の二重円筒式の竪形焼成炉では例えば、特
公昭52−46560号公報に示されているように廃熱
回収用の熱交換器を炉本体の内筒上部に装置し、
焼成後の廃ガスによつて燃焼用空気を加熱してい
る。
In the conventional double cylindrical vertical firing furnace, for example, as shown in Japanese Patent Publication No. 52-46560, a heat exchanger for waste heat recovery is installed in the upper part of the inner cylinder of the furnace body.
Combustion air is heated by waste gas after firing.

しかし、このような廃熱回収用の熱交換器を内
蔵した従来の竪形焼成炉では下記のような欠点が
あつた。
However, conventional vertical kilns having built-in heat exchangers for waste heat recovery have the following drawbacks.

(1) 炉本体内に設置のため、熱交換器のサイズが
限定され、伝熱面積を大きくして熱回収量を増
すことが不可能であつた。
(1) Since the heat exchanger was installed inside the furnace body, the size of the heat exchanger was limited, making it impossible to increase the heat transfer area and increase the amount of heat recovery.

(2) 廃ガスが熱交換器の下部より流入し、上部よ
り排出するため、重力方向と逆に廃ガスが流れ
るのでダストが浮遊状態となり、熱交換器のパ
イプ内にダストが膠着してパイプを閉塞する。
(2) Since the waste gas flows in from the bottom of the heat exchanger and is discharged from the top, the waste gas flows in the opposite direction to the direction of gravity, causing dust to become suspended and stick to the inside of the heat exchanger pipes, causing the pipes to become clogged. occlude.

(3) パイプ閉塞などの障碍があつた場合、炉本体
内に設置のため掃除が困難である。
(3) If there is a problem such as a pipe blockage, it is difficult to clean because it is installed inside the furnace body.

(4) 炉本体内に設置のため点検ができない。(4) It cannot be inspected because it is installed inside the furnace.

本発明は上記の欠点をなくし最大限の熱回収と
その有効利用を計る石灰石の焼成を円滑に行う竪
形焼成炉を得るため、炉本体の内部に炉本体とほ
ぼ同心円形の内筒を設け、燃焼手段から燃焼ガス
を炉本体と内筒との間の焼成空間に吹込み、前記
燃焼ガスの一部を吹込点から被焼成物と対向流と
して上昇させて焼成を行わせた後、この焼成後の
ダストを含んだ燃焼廃ガスによつて前記燃焼手段
へ供給する空気を加熱する廃熱回収装置と、前記
燃焼ガスの他部を吹込点から被焼成物と並行流と
して降下させて焼成を行わせるとともに、前記降
下させた燃焼ガスを内筒の下部内筒空間内を上昇
させた後、前記燃焼手段に還流させる手段とを有
してなる廃熱回収装置を備えた竪形焼成炉におい
て、前記廃熱回収装置を炉本体の外部に設置する
とともに、この廃熱回収装置を、上部に前記焼成
炉の内部に連通する廃ガス流入室と、この下方に
第1の仕切り板を介して設けた熱交換室と、さら
にこの下方に第2の仕切り板を介して設けられ、
廃ガス排出口を有した廃ガス排出室とから構成
し、前記熱交換室には、下部に被加熱空気である
冷空気の導入口と、上部に前記焼成炉の燃焼手段
に連通した加熱空気の排出口を設け、かつ、この
熱交換室内に上下両端部がそれぞれ前記第1の仕
切り板および第2の仕切り板を貫通して前記廃ガ
ス流入室内と前記廃ガス排出室内に開口され、そ
の軸線を上下方向に向けて円周方向に多数配置さ
れた廃ガス導管を設け、さらに、この熱交換室内
に上部に前記第1の仕切り板に近接した位置に冷
空気流出口と、下部に前記熱交換室の冷空気の導
入口付近に位置した冷空気流入口とを有し、その
軸線を上下方向に向けて円周方向に適宜の間隔を
おいて覆数本配置された冷空気送給管を設けてな
る廃熱回収装置を備えた竪形焼成炉とすることに
よつて確実、かつ、有効的な熱交換を行わせるよ
うにし、焼成炉の熱源単位を格段に減ずることが
できるようにしたものである。
In order to eliminate the above-mentioned drawbacks and obtain a vertical kiln that smoothly performs the firing of limestone with maximum heat recovery and effective utilization, the present invention provides a circular inner cylinder approximately concentric with the kiln body inside the kiln main body. , After blowing combustion gas from the combustion means into the firing space between the furnace body and the inner cylinder, and causing a part of the combustion gas to rise from the injection point as a counterflow to the object to be fired, the firing is performed. a waste heat recovery device that heats the air supplied to the combustion means with combustion waste gas containing dust after firing, and firing by lowering the other part of the combustion gas from an injection point in parallel flow with the object to be fired. and a means for causing the descended combustion gas to rise in the lower inner cylinder space of the inner cylinder and then to flow back to the combustion means. The waste heat recovery device is installed outside the furnace main body, and the waste heat recovery device is provided with a waste gas inflow chamber communicating with the inside of the kiln at the top, and a first partition plate below the waste gas inflow chamber. A heat exchange chamber is provided below the heat exchange chamber, and a second partition plate is provided below the heat exchange chamber.
The heat exchange chamber includes an inlet for cold air, which is air to be heated, in the lower part, and heated air in communication with the combustion means of the kiln in the upper part. A discharge port is provided in the heat exchange chamber, and both upper and lower ends thereof penetrate through the first partition plate and the second partition plate, respectively, and are opened into the waste gas inflow chamber and the waste gas discharge chamber. A large number of waste gas conduits are arranged in the circumferential direction with their axes facing up and down, and furthermore, a cold air outlet is provided in the upper part of the heat exchange chamber at a position close to the first partition plate, and a cold air outlet is provided in the lower part of the heat exchange chamber at a position close to the first partition plate. A cold air inlet located near the cold air inlet of the heat exchange chamber, and several cold air supply tubes arranged at appropriate intervals in the circumferential direction with their axes facing up and down. By using a vertical kiln equipped with a waste heat recovery device provided with pipes, reliable and effective heat exchange can be carried out, and the number of heat source units in the kiln can be significantly reduced. This is what I did.

つぎに本発明の廃熱回収装置を備えた竪形焼成
炉の一実施例を図面によつて説明する。
Next, one embodiment of a vertical firing furnace equipped with a waste heat recovery device of the present invention will be described with reference to the drawings.

第1図は本発明の廃熱回収装置をそなえた竪形
焼成炉である。
FIG. 1 shows a vertical kiln equipped with the waste heat recovery device of the present invention.

竪形焼成炉は炉本体1内にほぼ同心円形の内筒
2を設け、その間を焼成空間3a,3b,3c,
3d,3eとするとともに、焼成空間に上段11
a、中段11b、及び下段12の3段のブリツジ
を設けて内筒2を炉本体1と結合する。
The vertical firing furnace has a nearly concentric circular inner cylinder 2 in the furnace body 1, with firing spaces 3a, 3b, 3c,
3d and 3e, and an upper stage 11 in the firing space.
The inner cylinder 2 is connected to the furnace body 1 by providing three bridges: a, a middle stage 11b, and a lower stage 12.

そして内筒2の所要位置に中間壁4を設けて内
筒空間5を上部空間5aと下部空間5bとに分け
るとともに、上段ブリツジ11aの上方及び下段
ブリツジ12の下方に焼成空間3と上下部空間5
a,5bとを通ずる通気孔6a,6bをそれぞれ
設ける。
An intermediate wall 4 is provided at a predetermined position of the inner cylinder 2 to divide the inner cylinder space 5 into an upper space 5a and a lower space 5b, and a firing space 3 and an upper and lower space above the upper bridge 11a and below the lower bridge 12. 5
Ventilation holes 6a and 6b are provided, respectively, to communicate with a and 5b.

そして、炉本体1の外側に上段バーナ9aと下
段バーナ9bとを設け、それぞれ燃焼室10a,
10bを経て上段ブリツジ11a下方及び中間ブ
リツジ11b下方から焼成空間3へ開口する。
Then, an upper burner 9a and a lower burner 9b are provided outside the furnace body 1, and combustion chambers 10a and 10b are provided, respectively.
10b and opens into the firing space 3 from below the upper bridge 11a and from below the intermediate bridge 11b.

燃焼空間3は上部通気孔6aより上方を予熱焼
成空間3a、上部通気孔6aと上段バーナ9aと
の間を上部焼成空間3b、上段バーナ9aと下段
バーナ9bとの間を中部焼成空間3c、下段バー
ナ9bと下部通気孔6bとの間を下部焼成空間3
d、および下部通気孔6bより下方を冷却焼成空
間3e、とに分けられる。
The combustion space 3 includes a preheating firing space 3a above the upper ventilation hole 6a, an upper firing space 3b between the upper ventilation hole 6a and the upper stage burner 9a, a middle firing space 3c between the upper stage burner 9a and the lower stage burner 9b, and a lower stage between the upper stage burner 9a and the lower stage burner 9b. The lower firing space 3 is located between the burner 9b and the lower ventilation hole 6b.
d, and a cooling firing space 3e below the lower ventilation hole 6b.

なお、各ブリツジ11a,11b,12は炉本
体1と内筒2との間の上下方向における適当な位
置に円周方向に適当な間隔をおいて設けられてお
り、各焼成空間3b,3c,3d,3eを被焼成
物が円滑に降下するのに差支えないように設定さ
れている。
The bridges 11a, 11b, 12 are provided at appropriate positions in the vertical direction between the furnace body 1 and the inner cylinder 2 at appropriate intervals in the circumferential direction, and each bridge 11a, 11b, 12 is provided in each firing space 3b, 3c, 3d and 3e are set so as to allow the object to be fired to descend smoothly.

そして、上下段のバーナ9a,9bもその焼成
室10a,10bとともに炉本体1の円周方向に
第1図に示すように2段に限ることなく設置され
る。なお、これらバーナ9a,9b、焼成室10
a,10bは焼成手段を構成する。
The burners 9a and 9b in the upper and lower stages are also installed in the circumferential direction of the furnace body 1 along with the firing chambers 10a and 10b, without being limited to two stages as shown in FIG. In addition, these burners 9a, 9b, the firing chamber 10
a and 10b constitute firing means.

バーナ9a,9bへの空気は送風機(図示して
ない)から導管22を経て廃熱回収装置15に入
り、内筒2内より抽気され廃熱回収装置15内に
導入された廃ガスと熱交換によつて加熱された
後、導管23を経て環状導管13aに圧送され、
ついで導管25によつて上、下段バーナ9a,9
bに供給されるとともに導管27によつてインゼ
クタ14に供給される。
Air to the burners 9a and 9b enters the waste heat recovery device 15 from a blower (not shown) through the conduit 22, and exchanges heat with the waste gas extracted from the inner cylinder 2 and introduced into the waste heat recovery device 15. After being heated by
Then, the upper and lower burners 9a, 9 are connected through the conduit 25.
b and to the injector 14 by a conduit 27.

廃熱回収装置15は炉本体1の外部において炉
本体1と併設される。そして内筒2の内部とつぎ
に述べる廃熱回収装置15の廃ガス導入口15d
とは廃ガス抽出管19によつて連通される。
The waste heat recovery device 15 is installed outside the furnace body 1 and alongside the furnace body 1 . The inside of the inner cylinder 2 and the waste gas inlet 15d of the waste heat recovery device 15 described below
and is communicated with by a waste gas extraction pipe 19.

第2図は本発明の廃熱回収装置の縦断面図であ
る。
FIG. 2 is a longitudinal sectional view of the waste heat recovery device of the present invention.

廃熱回収装置15の本体は、中間に位置する熱
交換室15bと、この熱交換室15bの上部と下
部にそれぞれ第1の仕切り板15mおよび第2の仕
切り板15nを介して廃ガス流入室15aおよび
廃ガス排出室15cとを結合させることによつて
構成される。
The main body of the waste heat recovery device 15 includes a heat exchange chamber 15b located in the middle, and a waste gas inflow chamber via a first partition plate 15m and a second partition plate 15n at the upper and lower parts of the heat exchange chamber 15b, respectively. 15a and a waste gas discharge chamber 15c are combined.

廃ガス流入室15aは両側に廃ガス導入口15
d,15dを設け、それぞれは廃ガス抽出管19
に直結され、竪形焼成炉の内筒2の内部に連通し
ている。
The waste gas inlet chamber 15a has waste gas inlets 15 on both sides.
d and 15d are provided, each of which has a waste gas extraction pipe 19.
It is directly connected to and communicates with the inside of the inner cylinder 2 of the vertical firing furnace.

熱交換室15bは第2図に示すように細長い円
筒状を呈し、上部に熱交換を終えた加熱空気の排
出口15eを設け、下部に冷空気の導入口15f
を設けている。
The heat exchange chamber 15b has an elongated cylindrical shape as shown in FIG. 2, and has an exhaust port 15e for heated air after heat exchange at the top, and an inlet 15f for cold air at the bottom.
has been established.

加熱空気の排出口15eは前述のように導管2
3を介して環状導管13aに連通されており、ま
た冷空気の導入口15fは導管22を介して送風
機(図示していない)の送風口に連通されてい
る。加熱空気の排出口15eは熱交換室15bの
上部に設けた熱空気室15gにとりつけられ、ま
た冷空気の導入口15fは熱交換室15bの下部
に設けた冷空気室15hにとりつけられる。
The heated air outlet 15e is connected to the conduit 2 as described above.
3 to the annular conduit 13a, and the cold air inlet 15f communicates to the air outlet of a blower (not shown) via the conduit 22. The heated air outlet 15e is attached to a hot air chamber 15g provided in the upper part of the heat exchange chamber 15b, and the cold air inlet 15f is attached to a cold air chamber 15h provided in the lower part of the heat exchange chamber 15b.

熱空気室15gまたは冷空気室15hと熱交換
室15bとは、それぞれ透孔15i,15jによ
つて連通されている。
The hot air chamber 15g or the cold air chamber 15h and the heat exchange chamber 15b are communicated through through holes 15i and 15j, respectively.

熱交換室15bの内部には一定の間隔をおいて
平板状の邪魔板15kを多数とりつける。
A large number of flat baffle plates 15k are installed at regular intervals inside the heat exchange chamber 15b.

邪魔板15kは大小2種類に分けられる。 The baffle plate 15k is divided into two types, large and small.

大型の邪魔板15k1は外径が殆んど熱交換室1
5bの内径に近いほどの大きさに設計され、中央
に冷空気通過用の孔15lをあける。
Large baffle plate 15k 1 has almost the outer diameter of heat exchange chamber 1
5b, and has a hole 15l in the center for passing cold air.

小径の邪魔板15k2は、その外端と熱交換室1
5bとの内壁との間に若干のすき間15pをあ
け、このすき間15pより加熱される空気を上昇
させる。
The small diameter baffle plate 15k 2 has its outer end and the heat exchange chamber 1
A slight gap 15p is provided between the inner wall and the inner wall 5b, and heated air is allowed to rise through this gap 15p.

この大小2種の邪魔板15k1,15k2を熱交換
室15bの全長にわたつて一つおきに直列に並べ
る。
These two types of large and small baffle plates 15k 1 and 15k 2 are arranged in series over the entire length of the heat exchange chamber 15b, every other one.

熱交換室15bの内部には邪魔板15k1,15
k2を貫通して廃ガス導管としての多数の直管15
sを列設する。
Baffle plates 15k 1 , 15 are provided inside the heat exchange chamber 15b.
Numerous straight pipes 15 as waste gas conduits passing through k 2
Arrange s.

この直管15sは第2図に示すように、その上
端は第1の仕切り板15mを貫通して若干廃ガス流
入室15a内に突出して開口している。また、直
管15sの下端は第2の仕切り板15nを貫通し
て廃ガス排出室15c内に突出して開口してい
る。
As shown in FIG. 2, the straight pipe 15s has its upper end penetrating the first partition plate 15m and slightly protruding into the waste gas inlet chamber 15a. Further, the lower end of the straight pipe 15s passes through the second partition plate 15n and projects into the exhaust gas discharge chamber 15c.

そして、これらの直管15sの間には、その上
下端が前記第1、第2の仕切り板15m、15n
を貫通せず、直管15sと平行に、かつ、円周方
向に適宜の間隔をおいて配置された複数本(本実
施例では6本)の冷空気送給管15tが設けられ
ており、これらは前記邪魔板15kに取付けられ
ている。この冷空気送給管15tの上端部には、
第1の仕切り板15mに近接して冷空気流出口1
5t2が管壁の1部を切欠かれて開口されてお
り、また、冷空気送給管15tの下端部には前記
熱交換室15bの冷空気導入口15fの付近に位
置して冷空気流入口15t1が管壁の1部を切欠
かれて開口されて設けられている。
The upper and lower ends of the straight pipes 15s are connected to the first and second partition plates 15m and 15n.
A plurality of (six in this embodiment) cold air supply pipes 15t are provided, which do not penetrate through the straight pipe 15s and are arranged at appropriate intervals in the circumferential direction, and are arranged parallel to the straight pipe 15s. These are attached to the baffle plate 15k. At the upper end of this cold air supply pipe 15t,
Cold air outlet 1 adjacent to the first partition plate 15m
5t2 is opened by cutting a part of the pipe wall, and a cold air inlet is located at the lower end of the cold air supply pipe 15t near the cold air inlet 15f of the heat exchange chamber 15b. 15t1 is provided by cutting out a part of the tube wall and opening it.

このような冷空気送給管15tを設けることに
よつて、この冷空気送給管15tの内部に、前記
熱交換室15bの冷空気導入口15fから導入さ
れた冷空気の1部が冷空気流入口15t1から流
入し、冷空気送給管15t内を上昇して冷空気流
出口15t2から排出され、第1の仕切り板15
mを全面にわたつて均等に冷却する。
By providing such a cold air supply pipe 15t, a part of the cold air introduced from the cold air introduction port 15f of the heat exchange chamber 15b is transferred into the inside of the cold air supply pipe 15t. It flows in from the inflow port 15t1, rises within the cold air supply pipe 15t, and is discharged from the cold air outlet 15t2, and then passes through the first partition plate 15.
Cool evenly over the entire surface.

これは高温度の廃ガスに直接接触する第1の仕
切り板15mの温度上昇および腐食を防ぎ、熱膨
張による直管15sの配置バランスを保持するた
めである。
This is to prevent temperature rise and corrosion of the first partition plate 15m, which is in direct contact with high-temperature waste gas, and to maintain a balance in the arrangement of the straight pipes 15s due to thermal expansion.

廃ガス排出室15cは第2図に示すように先細
まりの円錐形を呈し、先端に廃ガス排出室15q
を形成する。
As shown in FIG. 2, the exhaust gas discharge chamber 15c has a tapered conical shape, and the exhaust gas discharge chamber 15q is located at the tip.
form.

廃ガス排出室15qは導管28を介して排風機
(図示してない)の吸込口に連通されている。
The waste gas discharge chamber 15q is communicated via a conduit 28 with an inlet of an exhaust fan (not shown).

次に、このように構成された本発明の作動を説
明する。
Next, the operation of the present invention configured as described above will be explained.

上段バーナ9aの燃焼室10aで燃焼した廃ガ
スの一部は上部焼成空間3bで被焼成物と対向流
となつて被焼成物を加熱しながらブリツジ11a
の間隙から上昇した後、予熱燃焼空間3aへ上昇
を続け、被焼成物を予熱的に加熱した後、排風手
段(図示してない)によつて炉本体1外に排出さ
れる。
A part of the waste gas combusted in the combustion chamber 10a of the upper stage burner 9a flows counter-currently to the object to be fired in the upper firing space 3b, heating the object to be fired while passing through the bridge 11a.
After rising from the gap, it continues to rise to the preheating combustion space 3a, and after preheating the object to be fired, it is discharged to the outside of the furnace body 1 by an exhaust means (not shown).

また、廃ガスの一部は上部通気孔6aより内筒
2の上部内筒空間5aに入り、さらに廃ガス抽出
管19を経由して廃熱回収装置15の廃ガス導入
口15dより廃ガス流入室15a内に流入する。
In addition, a part of the waste gas enters the upper inner cylinder space 5a of the inner cylinder 2 through the upper ventilation hole 6a, and further passes through the exhaust gas extraction pipe 19 and flows into the waste gas inlet 15d of the waste heat recovery device 15. It flows into the chamber 15a.

この廃ガスは第1の仕切り板15mを貫通して
廃ガス流入室15a内に突出している直管15s
の開口より直管15s内に流入し、直管15s内
を下降する。
This waste gas passes through the first partition plate 15m and projects into the waste gas inflow chamber 15a through a straight pipe 15s.
It flows into the straight pipe 15s through the opening of the straight pipe 15s and descends inside the straight pipe 15s.

一方、冷空気は導管22を経て冷空気の導入口
15fより熱交換室15bに設けられた冷空気室
15hに入り、さらに透孔15jより熱交換室1
5bの下部に送りこまれる。
On the other hand, the cold air passes through the conduit 22, enters the cold air chamber 15h provided in the heat exchange chamber 15b from the cold air inlet 15f, and then enters the heat exchange chamber 1 from the through hole 15j.
It is sent to the lower part of 5b.

この冷空気は熱交換室15bの下部より上部に
向つて進行する。
This cold air advances from the lower part to the upper part of the heat exchange chamber 15b.

その際、冷空気は大型の邪魔板15k1の孔15
1と小型の邪魔板15k2の円周端と熱交換室15
bの内壁との間のすき間15pとを交互に通りな
がら、直管15s内の廃ガスと熱交換を行い、熱
空気となる。
At that time, the cold air is passed through the hole 15 of the large baffle plate 15k1.
1 and small baffle plate 15k 2 circumferential end and heat exchange chamber 15
It exchanges heat with the waste gas in the straight pipe 15s while passing alternately through the gaps 15p between the air and the inner wall of the pipe b, and becomes hot air.

この熱空気は熱交換室15bの上部にあけられ
た透孔15jより熱空気室15gに入り、さらに
排出口15eから導管23を経由して環状導管1
3aに送られる。この熱空気は環状導管13にに
送られるとともにインゼクタ14に供給される。
This hot air enters the hot air chamber 15g through the through hole 15j formed in the upper part of the heat exchange chamber 15b, and then passes through the conduit 23 from the discharge port 15e to the annular conduit 1.
Sent to 3a. This hot air is sent to an annular conduit 13 and supplied to an injector 14.

一方、前記冷空気室15hから熱交換室15b
の下部に送りこまれた冷空気の1部は、円周方向
に適宜の間隔をおいて複数本配置された冷空気送
給管15t内に、冷空気流入口15t1から導入
され、冷空気送給管15t内を上昇して上部の冷
空気流出口15t2から熱交換室15bの上端部
に排出され、第1の仕切り板15mの全面を均等
に冷却する。従つて、高温度雰囲気にさらされる
第1の仕切り板15mの温度上昇および腐食が防
止されるとともに、この第1の仕切り板15mに
取付られた直管(廃ガス導管)15sの配置バラ
ンスが保持され、また、その変形も防止される。
On the other hand, from the cold air chamber 15h to the heat exchange chamber 15b
A part of the cold air sent to the lower part of the is introduced from the cold air inlet 15t1 into the cold air supply pipes 15t, which are arranged in plurality at appropriate intervals in the circumferential direction, and the cold air is supplied to the lower part of the cold air. The air rises inside the tube 15t and is discharged from the upper cold air outlet 15t2 to the upper end of the heat exchange chamber 15b, uniformly cooling the entire surface of the first partition plate 15m. Therefore, the temperature rise and corrosion of the first partition plate 15m exposed to the high temperature atmosphere are prevented, and the arrangement balance of the straight pipe (waste gas conduit) 15s attached to the first partition plate 15m is maintained. and its deformation is also prevented.

また、熱交換を終えた廃ガスは直管15sの下
端より廃ガス排出室15cに集められ、さらに排
出口15qより排風機(図示してない)によつて
系外に排出される。
Further, the waste gas that has undergone heat exchange is collected into the waste gas discharge chamber 15c from the lower end of the straight pipe 15s, and is further discharged outside the system from the discharge port 15q by an exhaust fan (not shown).

このように、ダストを含んだ焼成炉の廃ガスは
直管15s内を上から下に向けて重力方向に流れ
るので、ダストが直管15sの内壁に付着しよう
とする現象が防止され、ダストが膠着して直管1
5sを閉塞することがない。
In this way, the waste gas from the firing furnace containing dust flows from top to bottom in the direction of gravity within the straight pipe 15s, so that the phenomenon of dust adhering to the inner wall of the straight pipe 15s is prevented, and the dust is Sticky straight pipe 1
5s will not be occluded.

上段バーナ9aの燃焼ガスの他の一部は、中部
焼成空間3cを被焼成物と平行流となつてともに
降下(C→の流れ)し、中段ブリツジ11bの間
隙を経て下段ブリツジ12に至る間、中部焼成空
間3c、下部焼成空間3dで被焼成物を加熱し、
下段ブリツジ12の間隙を経て冷却焼成空間3e
に入るとすぐ下部通気孔6bより内筒下部空間5
bに入る(D→の流れ)。その後、廃ガスは内筒
下部空間5b内を上昇し、中間壁4に遮ぎられ導
管21を経て第一環状管13aよりの空気ととも
にインゼクタ14に吸引された後燃焼室10bの
二次空気として供給されるようになつている。
The other part of the combustion gas from the upper stage burner 9a descends together with the object to be fired through the intermediate firing space 3c in a parallel flow (flow of C→), and reaches the lower stage bridge 12 through the gap of the intermediate stage bridge 11b. , heating the object to be fired in the middle firing space 3c and the lower firing space 3d;
The cooling firing space 3e passes through the gap of the lower bridge 12.
Immediately after entering the inner cylinder lower space 5 from the lower ventilation hole 6b
Enter b (flow of D→). After that, the waste gas rises in the inner cylinder lower space 5b, is blocked by the intermediate wall 4, passes through the conduit 21, and is sucked into the injector 14 together with the air from the first annular pipe 13a, and then becomes secondary air in the combustion chamber 10b. supply is becoming available.

下段バーナ9bの燃焼ガスも、その一部は上昇
して上段バーナ9aの燃焼ガスと合体してA流ま
たはB流となつて予熱焼成空間3aまたは廃熱回
収装置15を経て排出される。また、他の一部は
上段バーナ9aの降下C流ガスと合体し、下段ブ
リツジ12の間隙及び下部通気孔6bを経てD流
とともにインゼクタ14に吸引されるようになつ
ている。
A part of the combustion gas from the lower stage burner 9b also rises and combines with the combustion gas from the upper stage burner 9a to become a stream A or a stream B and is discharged through the preheating firing space 3a or the waste heat recovery device 15. The other part is combined with the descending C flow gas of the upper stage burner 9a, passes through the gap of the lower stage bridge 12 and the lower ventilation hole 6b, and is sucked into the injector 14 along with the D flow.

そして、上段バーナ9aには理論空気量よりも
比較的少量の空気を、下段バーナ9bには比較的
多量の空気を送ることによつて焼成効果を増大す
るようになつている。
The firing effect is increased by sending a relatively small amount of air to the upper burner 9a and a relatively large amount of air to the lower burner 9b than the theoretical air amount.

そして、上、中、下の三段のブリツジ11a,
11b,12はいずれもその上方が屋根形にとが
つて被焼成物が降下しやすくなつている。
Then, the three stages of bridges 11a, upper, middle, and lower,
Both of 11b and 12 have a roof-shaped upper part, making it easier for the object to be fired to descend.

なお、本発明では、廃熱回収装置15を炉本体
とは別個に外部に設置することによつて、内筒2
の上部空間5aが空間部となり、高温廃ガスの通
気孔6a,6bでダストによる閉塞がなくなり、
通気圧損が少なくなつて廃熱回収装置15の下部
の廃ガス排出口15qに接続される排風機(図示
せず)の風圧を下げることが可能となり、電力が
節減される。
In addition, in the present invention, by installing the waste heat recovery device 15 outside separately from the furnace main body, the inner cylinder 2
The upper space 5a becomes a space, and the ventilation holes 6a and 6b for high-temperature waste gas are no longer blocked by dust.
Since the ventilation pressure loss is reduced, it becomes possible to lower the wind pressure of the exhaust fan (not shown) connected to the waste gas outlet 15q at the bottom of the waste heat recovery device 15, and power is saved.

内筒2は2つの管、すなわち外管7aと内管7
bとよりなり、これらは互に適宜すき間を置いた
同心円的に配置されその間に冷却空間8を形成す
る。この冷却空間8へは送風機17から導管30
を経て冷風が圧送され、冷却空間8を上昇しつつ
外管7aの熱を得て熱風となり導管29b,29
cを経て第2環状導管13bに集められ導管26
a,26bによつてバーナ9a,9bに送りこま
れる。
The inner tube 2 has two tubes, an outer tube 7a and an inner tube 7.
b, which are arranged concentrically with appropriate gaps between them, forming a cooling space 8 therebetween. A conduit 30 is connected from the blower 17 to this cooling space 8.
The cold air is force-fed through the cooling space 8, gains heat from the outer tube 7a, and becomes hot air through the conduits 29b and 29.
c, and is collected in the second annular conduit 13b and conduit 26
a, 26b to the burners 9a, 9b.

また、炉底空気は、送風機17から導管30,
31によつて導かれ、焼成物搬出装置内を経て冷
却焼成空間3eに入り、被焼成物と対向流となつ
て上昇し、下段ブリツジ12によつて邪魔されつ
つバーナ9a,9bからのC流と合し、下方通気
孔6bから内筒下部空間5b内へD流となつて流
入する。
Further, the hearth bottom air is transferred from the blower 17 to the conduit 30,
31, enters the cooling firing space 3e through the fired product carrying out device, rises as a counterflow to the fired product, and is obstructed by the lower bridge 12 as the C flow from the burners 9a and 9b flows. and flows into the inner cylinder lower space 5b from the lower ventilation hole 6b as a flow D.

なお、焼成物搬出装置は、炉本体1の下方に配
置され、ほぼ円錐状の分配体32とその直下にカ
ム状に形成された排出体33を有する環状搬出テ
ーブル34とよりなる。そして前記排出体33は
モータ37の回転を減速機36によつて減速した
後、ピンギヤ35を経て駆動される。
The fired product delivery device is disposed below the furnace body 1 and includes an annular delivery table 34 having a substantially conical distribution body 32 and a cam-shaped discharge body 33 directly below the distribution body 32. The discharge body 33 is driven via a pin gear 35 after the rotation of the motor 37 is reduced by a speed reducer 36 .

本発明の石灰石などの竪形焼成炉は上述のよう
な構造であるから、送入手段(図示せず)によつ
て被焼成物が炉本体1と内筒2との間の予熱焼成
空間3aに投入され、バーナ9a,9bから被焼
成物と対向流となつて上昇するA流によつて予熱
されつつ降下し、ついで内筒2に設けた上部通気
孔6a位置よりも降下して、上部、中部、下部焼
成空間3b,3c,3dにおいて所要の焼成を受
け、下段ブリツジ12の間隙を抜け落ちた後、冷
却焼成空間3eで冷却され、焼成物搬出装置に至
る。この間、上段バーナ9aの空気量よりも下段
バーナ9bの空気量が多くしてあるから被焼成物
は良好に焼成される。
Since the vertical firing furnace for limestone, etc. of the present invention has the above-described structure, the materials to be fired are transported to the preheated firing space 3a between the furnace body 1 and the inner cylinder 2 by the feeding means (not shown). , and descends while being preheated by flow A which rises from the burners 9a and 9b as a counterflow to the object to be fired, and then descends from the position of the upper ventilation hole 6a provided in the inner cylinder 2, and the upper , middle and lower firing spaces 3b, 3c, and 3d, and after falling through the gap of the lower bridge 12, it is cooled in the cooling firing space 3e and reaches the fired product delivery device. During this time, since the amount of air in the lower stage burner 9b is greater than the amount of air in the upper stage burner 9a, the object to be fired is fired satisfactorily.

以上の説明から明らかなように、本発明は特許
請求の範囲に記載したような構成にしたので、焼
成炉から炉外に排出されるダストを含んだ廃ガス
が廃熱回収装置の廃ガス導管内に上部から流入し
て管内を下降し、下部から排出されるため、廃ガ
スは重力方向へ流れることになり、従来の重力方
向とは逆に廃ガスが流れる場合のようにダストが
管内で浮遊して管内壁に付着したり、膠着しやす
くなるという現象を回避することができ、廃ガス
導管の閉塞を防止することができる。従つて、高
い熱交換効率を長期にわたつて維持することがで
き、その能力を最大限に発揮できる。
As is clear from the above description, since the present invention has the configuration as described in the claims, the waste gas containing dust discharged from the firing furnace to the outside of the furnace is transferred to the waste gas conduit of the waste heat recovery device. Since the waste gas flows in the upper part of the pipe, descends inside the pipe, and is discharged from the lower part, the waste gas flows in the direction of gravity. It is possible to avoid the phenomenon of floating and adhering to the inner wall of the pipe or becoming likely to stick together, and it is possible to prevent clogging of the waste gas pipe. Therefore, high heat exchange efficiency can be maintained over a long period of time, and its ability can be maximized.

そして、廃熱回収装置の熱交換室には、前記多
数の廃ガス導管の間において、円周方向に適宜の
間隔をおいて配置された冷空気送給管によつて、
第1の仕切り板がその全面にわたつて均等に冷却
されるため、高温度雰囲気にさらされる第1の仕
切り板の温度上昇および腐食が防止され、このた
め、第1の仕切り板に取付けられる多数の廃ガス
導管の配置バランスがくるつたり、導管自体が変
形することがなく、廃熱回収装置の作動が確実に
維持される。
The heat exchange chamber of the waste heat recovery device is provided with cold air supply pipes arranged at appropriate intervals in the circumferential direction between the plurality of waste gas pipes.
Since the first partition plate is cooled evenly over its entire surface, the temperature increase and corrosion of the first partition plate exposed to the high temperature atmosphere are prevented, and therefore the large number of parts attached to the first partition plate are prevented from increasing. The operation of the waste heat recovery device is reliably maintained without the waste gas conduit being unbalanced or the conduit itself being deformed.

そして、このような効果を有する廃熱回収装置
を焼成炉本体の外部に設置したので、従来の焼成
炉のように炉本体の内容積に限定されることな
く、伝熱面積を大きくすることができ、焼成炉の
廃熱を余すことなく使用でき、熱回収量を増大さ
せることが可能な効果と相いまつて、最大限の熱
回収とその有効利用を長期にわたつて確実に行う
ことができるとともに、焼成炉の熱源単位を格段
に減ずることができるものである。
Since the waste heat recovery device with this effect is installed outside the firing furnace body, the heat transfer area can be increased without being limited to the internal volume of the furnace body as in conventional firing furnaces. This makes it possible to fully utilize the waste heat of the kiln, and together with the effect of increasing the amount of heat recovery, it is possible to ensure maximum heat recovery and its effective use over a long period of time. At the same time, the number of heat source units of the kiln can be significantly reduced.

なお、廃熱回収装置を焼成炉の外部に設けるこ
とによつて、廃熱回収装置の内部点検、補修が容
易になるとともに、熱交換室の耐熱性能も下げる
ことも可能になり、安価な材質のものも使用でき
ることになる。
In addition, by installing the waste heat recovery device outside the kiln, internal inspection and repair of the waste heat recovery device becomes easier, and it is also possible to lower the heat resistance performance of the heat exchange chamber, making it possible to use cheaper materials. You can also use the.

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

第1図は本発明の廃熱回収装置をそなえた石灰
石焼成炉の縦断面図、第2図は廃熱回収装置の縦
断面図、第3図は第2図のA.A断面図(拡大)で
ある。 1は炉本体、2は内筒、3は焼成空間であつて
3aは予熱焼成空間、3bは上部焼成空間、3c
は中部焼成空間、3dは下部焼成空間、3eは冷
却焼成空間、4は中間壁、5は内筒空間であつ
て、5aは上部内筒空間、5bは下部内筒空間、
6a,6bは通気孔、7aは内管、7bは内管、
8は冷却空間、9aは上段バーナ、9bは下段バ
ーナ、10a,10bは焼成室、11aは上段ブ
リツジ、11bは中段ブリツジ、12は下段ブリ
ツジ、13aは環状導管、13bは第2環状導
管、14はインゼクタ、15は廃熱回収装置、1
7は送風機、19は廃ガス抽出管、21,22,
23,25,27,28,29b,29c,31
は導管、32は分配体、33は排出体、34は環
状搬出テーブル、35はピンギヤ、36は減速
機、37はモータである。15aは廃熱回収装置
15の廃ガス流入室(以下、廃熱回収装置に係る
もの)、15bは熱交換室、15cは廃ガス排出
室、15dは廃ガス導入口、15eは加熱空気の
排出口、15fは冷空気の導入口、15gは熱空
気室、15hは冷空気室、15i,15jは透
孔、15kは邪魔板であつて、15k1は大形、1
5k2は小形を指す。15lは冷空気通過用の孔、
15m,15nは仕切り板、15sは直管(廃ガ
ス導管)、15tは冷空気送給管、,15pはすき
間、15qは廃ガス排出口である。
Fig. 1 is a longitudinal sectional view of a limestone kiln equipped with the waste heat recovery device of the present invention, Fig. 2 is a longitudinal sectional view of the waste heat recovery device, and Fig. 3 is a sectional view (enlarged) of AA of Fig. 2. be. 1 is a furnace body, 2 is an inner cylinder, 3 is a firing space, 3a is a preheating firing space, 3b is an upper firing space, 3c
3d is a middle firing space, 3d is a lower firing space, 3e is a cooling firing space, 4 is an intermediate wall, 5 is an inner cylinder space, 5a is an upper inner cylinder space, 5b is a lower inner cylinder space,
6a and 6b are ventilation holes, 7a is an inner pipe, 7b is an inner pipe,
8 is a cooling space, 9a is an upper burner, 9b is a lower burner, 10a and 10b are firing chambers, 11a is an upper bridge, 11b is a middle bridge, 12 is a lower bridge, 13a is an annular conduit, 13b is a second annular conduit, 14 is an injector, 15 is a waste heat recovery device, 1
7 is a blower, 19 is a waste gas extraction pipe, 21, 22,
23, 25, 27, 28, 29b, 29c, 31
32 is a conduit, 32 is a distribution body, 33 is a discharge body, 34 is an annular delivery table, 35 is a pin gear, 36 is a speed reducer, and 37 is a motor. 15a is a waste gas inflow chamber of the waste heat recovery device 15 (hereinafter referred to as the waste heat recovery device), 15b is a heat exchange chamber, 15c is a waste gas discharge chamber, 15d is a waste gas inlet, and 15e is a heated air discharge chamber. The outlet, 15f is a cold air inlet, 15g is a hot air chamber, 15h is a cold air chamber, 15i, 15j are through holes, 15k is a baffle plate, 15k 1 is a large size, 1
5k 2 refers to small size. 15l is a hole for passing cold air,
15m and 15n are partition plates, 15s is a straight pipe (waste gas conduit), 15t is a cold air supply pipe, 15p is a gap, and 15q is a waste gas outlet.

Claims (1)

【特許請求の範囲】[Claims] 1 炉本体の内部に炉本体とほぼ同心円形の内筒
を設け、燃焼手段から燃焼ガスを炉本体と内筒と
の間の焼成空間に吹込み、前記燃焼ガスの一部を
吹込点から被焼成物と対向流として上昇させて焼
成を行わせた後、この焼成後のダストを含んだ燃
焼廃ガスによつて前記燃焼手段へ供給する空気を
加熱する廃熱回収装置と、前記燃焼ガスの他部を
吹込点から被焼成物と並行流として降下させて焼
成を行わせるとともに、前記降下させた燃焼ガス
を内筒の下部内筒空間内を上昇させた後、前記燃
焼手段に還流させる手段とを有してなる廃熱回収
装置を備えた竪形焼成炉において、前記廃熱回収
装置を炉本体の外部に設置するとともに、この廃
熱回収装置を、上部に前記焼成炉の内部に連通す
る廃ガス流入室と、この下方に第1の仕切り板を
介して設けた熱交換室と、さらにこの下方に第2
の仕切り板を介して設けられ、廃ガス排出口を有
した廃ガス排出室とから構成し、前記熱交換室に
は、下部に被加熱空気である冷空気の導入口と、
上部に前記焼成炉の燃焼手段に連通した加熱空気
の排出口を設け、かつ、この熱交換室内に上下両
端部がそれぞれ前記第1の仕切り板および第2の
仕切り板を貫通して前記廃ガス流入室内と前記廃
ガス排出室内に開口され、その軸線を上下方向に
向けて円周方向に多数配置された廃ガス導管を設
け、さらに、この熱交換室内に上部に前記第1の
仕切り板に近接した位置に冷空気流出口と、下部
に前記熱交換室の冷空気の導入口付近に位置した
冷空気流入口とを有し、その軸線を上下方向に向
けて円周方向に適宜の間隔をおいて複数本配置さ
れた冷空気送給管を設けてなる廃熱回収装置を備
えたことを特徴とする竪形焼成炉。
1. A circular inner cylinder approximately concentric with the furnace body is provided inside the furnace body, combustion gas is blown from the combustion means into the firing space between the furnace body and the inner cylinder, and a part of the combustion gas is directed from the injection point to the surrounding area. a waste heat recovery device that heats the air supplied to the combustion means by the combustion waste gas containing dust after firing by raising it as a counterflow to the fired product; Means for causing the other part to descend from the injection point in a parallel flow with the object to be fired to perform firing, and for causing the descended combustion gas to ascend within the lower inner cylinder space of the inner cylinder and then to flow back to the combustion means. In a vertical firing furnace equipped with a waste heat recovery device, the waste heat recovery device is installed outside the furnace body, and the waste heat recovery device is communicated with the inside of the furnace at the top. a heat exchange chamber provided below this through a first partition plate, and a second heat exchange chamber provided below this through a first partition plate.
a waste gas discharge chamber provided through a partition plate and having a waste gas discharge port;
A heated air outlet communicating with the combustion means of the kiln is provided in the upper part, and the upper and lower ends of the heat exchange chamber pass through the first partition plate and the second partition plate, respectively, and the waste gas is discharged into the heat exchange chamber. A large number of waste gas conduits are opened in the inflow chamber and the waste gas discharge chamber, and are arranged circumferentially in a large number with their axes directed in the vertical direction, and further, in the heat exchange chamber, the first partition plate is provided in the upper part. A cold air outlet is provided at a close position, and a cold air inlet is located at a lower part near the cold air inlet of the heat exchange chamber, and the axis thereof is directed in the vertical direction and is spaced at appropriate intervals in the circumferential direction. A vertical firing furnace characterized by being equipped with a waste heat recovery device comprising a plurality of cold air supply pipes arranged at intervals.
JP10971479A 1979-08-30 1979-08-30 Waste heat recovery device for vertical baking furnace Granted JPS5634086A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10971479A JPS5634086A (en) 1979-08-30 1979-08-30 Waste heat recovery device for vertical baking furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10971479A JPS5634086A (en) 1979-08-30 1979-08-30 Waste heat recovery device for vertical baking furnace

Publications (2)

Publication Number Publication Date
JPS5634086A JPS5634086A (en) 1981-04-06
JPS6158750B2 true JPS6158750B2 (en) 1986-12-12

Family

ID=14517356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10971479A Granted JPS5634086A (en) 1979-08-30 1979-08-30 Waste heat recovery device for vertical baking furnace

Country Status (1)

Country Link
JP (1) JPS5634086A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0333245U (en) * 1989-08-11 1991-04-02

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0752698B2 (en) * 1989-01-20 1995-06-05 太陽誘電株式会社 Method for manufacturing monolithic ceramic capacitor

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51121406A (en) * 1975-04-18 1976-10-23 Tokyo Cokes Kk Cupola
JPS5246560A (en) * 1975-10-13 1977-04-13 Hitachi Ltd Heat transfer system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51121406A (en) * 1975-04-18 1976-10-23 Tokyo Cokes Kk Cupola
JPS5246560A (en) * 1975-10-13 1977-04-13 Hitachi Ltd Heat transfer system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0333245U (en) * 1989-08-11 1991-04-02

Also Published As

Publication number Publication date
JPS5634086A (en) 1981-04-06

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