JPH09117733A - Method for melting incineration ashe and its melting furnace - Google Patents

Method for melting incineration ashe and its melting furnace

Info

Publication number
JPH09117733A
JPH09117733A JP7280385A JP28038595A JPH09117733A JP H09117733 A JPH09117733 A JP H09117733A JP 7280385 A JP7280385 A JP 7280385A JP 28038595 A JP28038595 A JP 28038595A JP H09117733 A JPH09117733 A JP H09117733A
Authority
JP
Japan
Prior art keywords
furnace
furnace body
ash
melting
incineration
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
JP7280385A
Other languages
Japanese (ja)
Inventor
Kouji Itsunuki
耕治 五貫
Naoya Takakusa
直也 高草
Takao Aoba
隆生 青葉
Yoshito Sakaguchi
良人 坂口
Etsuo Murata
悦夫 村田
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.)
Chugai Ro Co Ltd
Naniwa Roki Co Ltd
Original Assignee
Chugai Ro Co Ltd
Naniwa Roki Co 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 Chugai Ro Co Ltd, Naniwa Roki Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP7280385A priority Critical patent/JPH09117733A/en
Publication of JPH09117733A publication Critical patent/JPH09117733A/en
Pending legal-status Critical Current

Links

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  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the local erosion of furnace walls and to prolong the life of a furnace by allowing the erosion to progress evenly over the entire surface of the walls in the furnace, unlike a furnace fixed with a melt storage section, as incineration ashes melt in the rotating furnace body and the molten slag comes into contact successively with the inside walls of the furnace. SOLUTION: This melting furnace consists of the approximately cylindrical furnace body 10 of a horizontal installation type which is internally lined with refractory thermal insulating materials 10a and has apertures 11a, 11b of a small diameter at both ends, a rotating mechanism 15 which supports and rotates this furnace body, a direct fire burner which is mounted at either of these apertures, an incineration ashe supply pipe 5 to be mounted at either of the apertures, a hood 26 which encloses the other aperture and a tilting mechanism 20 which tilts the furnace body. The local erosion of the furnace is prevented by bringing the melt into uniform contact with the inside walls of the furnace. As a result, the melting furnace for the incineration ashes constituted to melt the in-furnace incineration ashes with a direct fire burner while rotating the furnace body and the discharge the molten incineration ash melt from the other aperture 11b is obtd.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は下水汚泥の焼却灰、
産業廃棄物の焼却灰あるいは飛灰等の焼却灰の溶融方法
およびその溶融炉に関するものである。
TECHNICAL FIELD The present invention relates to incineration ash of sewage sludge,
The present invention relates to a method for melting incineration ash such as incineration ash of industrial waste or fly ash, and a melting furnace therefor.

【0002】[0002]

【従来の技術】従来、産業廃棄物の処理方法として種々
の方法が提案されているが、その一つとして産業廃棄物
を焼却し、その焼却灰を溶融した後、固化することによ
り減容化と重金属類の封じ込みを図って投棄する方法が
ある。この方法において、焼却灰を溶融するには、たと
えば特開平7−155721等公報に開示されているよ
うに、焼却灰を定置型溶融炉の貯留部に供給し、これを
バーナにより加熱して溶融する方法が広く採用されてい
る。
2. Description of the Related Art Conventionally, various methods have been proposed as a method for treating industrial waste, one of which is to incinerate the industrial waste, melt the incinerated ash, and then solidify it to reduce the volume. And there is a method to throw away the heavy metals. In this method, in order to melt the incinerated ash, for example, as disclosed in Japanese Patent Laid-Open No. 7-155721, the incinerated ash is supplied to a storage part of a stationary melting furnace and heated by a burner to melt it. The method of doing is widely adopted.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、前記方
法は定置固定された溶融炉で焼却灰を溶融するため、溶
融スラグ(溶融物)は常に一定位置に貯留されている。
そして、溶融炉の内部は耐火断熱材が内張されるが、こ
の耐火断熱材のうち溶融スラグが接する貯留部部分、す
なわち、溶融スラグとの接触部が一定であるため、この
部分における侵蝕が激しく、炉の補修を頻繁に行なわな
ければならないという課題を有する。したがって、本発
明は溶融物を炉の一定位置に貯留することなく万偏なく
炉内壁に接触させて溶融する焼却灰の溶融方法およびそ
の溶融炉を提供することを目的とする。
However, since the above method melts the incineration ash in the fixed and fixed melting furnace, the molten slag (melt) is always stored at a fixed position.
Then, the inside of the melting furnace is lined with a refractory heat insulating material, but in this refractory heat insulating material, the storage portion portion where the molten slag is in contact, that is, the contact portion with the molten slag is constant, so erosion in this portion It has a serious problem that the furnace must be frequently repaired. Therefore, an object of the present invention is to provide a method for melting incinerator ash, which melts a molten material by uniformly contacting the inner wall of the furnace without storing the molten material in a certain position of the furnace, and a melting furnace therefor.

【0004】[0004]

【課題を解決するための手段】本発明は、前記目的を達
成するために、請求項1においては、水平軸を中心とし
て回転可能な炉本体内に焼却灰を投入し、前記炉本体を
回転させながら直火バーナにより前記焼却灰を加熱して
溶融するようにしたものである。請求項2においては、
前記直火バーナを酸素バーナとするものである。請求項
3においては、前記焼却灰をペレット化されたものであ
る。請求項4においては、溶融炉を、耐火断熱材が内張
され、かつ、両端開口部が小径となった横設置型略円筒
体の炉本体と、該炉本体を支持して回転させる回転機構
と、前記開口部のいずれか一方に取付ける直火バーナ
と、前記開口部の一方に取り付ける焼却灰供給管と、前
記他方の開口部を囲むフードと、前記炉本体を傾動させ
る傾動機構とからなり、前記直火バーナにより溶融され
た焼却灰溶融物を前記他方の開口部から排出するように
したものである。
According to the present invention, in order to achieve the above object, in claim 1, incinerator ash is charged into a furnace body rotatable about a horizontal axis to rotate the furnace body. The incineration ash is heated and melted by an open flame burner while being heated. In claim 2,
The open flame burner is an oxygen burner. In Claim 3, the incineration ash is pelletized. In Claim 4, a furnace main body of a horizontal installation type substantially cylindrical body in which a refractory heat insulating material is lined and both end openings have a small diameter, and a rotating mechanism for supporting and rotating the furnace main body. A direct flame burner attached to any one of the openings, an incinerator ash supply pipe attached to one of the openings, a hood surrounding the other opening, and a tilting mechanism for tilting the furnace body. The incineration ash melted by the open flame burner is discharged from the other opening.

【0005】[0005]

【発明の実施の形態】つぎに、本発明の実施の形態を図
にしたがって説明する。まず、本発明にかかる溶融炉T
を使用して焼却灰を溶融する方法を図1に示すフローに
したがって説明する。ホッパー1に投入された下水汚泥
等の焼却灰は定量フィーダ2によって造粒機3に送られ
て所定形状のペレットとなり灰ペレット供給装置4に貯
留され、ここから下記するように灰ペレット供給管5に
より一定量ずつ溶融炉T内へ供給されるとともに、直火
バーナ7で加熱され溶融する。この熔融炉Tは下記に詳
述するように、水平軸を中心に回転する横設置型略円筒
体の炉本体10を備え、焼却灰の溶融物は開口部(溶融
スラグ抽出口)11bから水封ピット40内の冷却水中
に落下固化したのち、コンベア41にて搬出される。ま
た、開口部11bから噴出する炉内ガスは排気ファン3
2によりフード26からバグフィルタ33に入り、ここ
で浮遊飛灰等を捕集されるようになっている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described with reference to the drawings. First, the melting furnace T according to the present invention
A method of melting the incineration ash by using the will be described according to the flow shown in FIG. Incinerated ash such as sewage sludge that has been put into the hopper 1 is sent to the granulator 3 by the quantitative feeder 2 and formed into pellets of a predetermined shape, which are stored in the ash pellet supply device 4, from which the ash pellet supply pipe 5 will be described below. Is supplied into the melting furnace T by a constant amount, and is heated and melted by the open flame burner 7. As will be described in detail below, this melting furnace T includes a horizontally installed substantially cylindrical furnace body 10 that rotates about a horizontal axis, and the molten incineration ash melts from the opening (molten slag extraction port) 11b with water. After being dropped and solidified in the cooling water in the sealing pit 40, it is carried out by the conveyor 41. Further, the gas in the furnace ejected from the opening 11b is exhausted by the exhaust fan 3
2 enters the bag filter 33 from the hood 26, where floating fly ash and the like are collected.

【0006】つぎに、前記溶融炉Tについて詳述する。
この溶融炉Tは、大略、炉本体10と、該炉本体10を
支持して回転させる回転機構15と、炉本体10を傾動
する傾動機構20と、灰ペレット供給管5および直火バ
ーナ7と、フード26とからなる。そして、炉本体10
は耐火断熱材10aが内張され、かつ、両端開口部11
a,11bが小径となった横設置型円筒体からなり、一
方の開口部11aは下記する灰ペレット供給管5と直火
バーナ7の装着部を構成し、他方の開口部11bは溶融
スラグ抽出口となっている。また、この溶融スラグ抽出
口11bは円形開口部12aに4個の三角状切欠き12
bを等間隔で設けた構成となっている(図3参照)。な
お、13は炉本体10の胴部外周に設けた2本のレール
で、このレール13,13の各対向側面は下記する支持
台16に取付けたストッパーコロ13aと当接するよう
になっている。
Next, the melting furnace T will be described in detail.
The melting furnace T generally includes a furnace body 10, a rotating mechanism 15 that supports and rotates the furnace body 10, a tilting mechanism 20 that tilts the furnace body 10, an ash pellet supply pipe 5, and an open flame burner 7. , Hood 26. And the furnace body 10
Is lined with a fireproof heat insulating material 10a and has openings 11 at both ends.
a and 11b are horizontal installation type cylindrical bodies having a small diameter, one opening 11a constitutes a mounting portion for an ash pellet supply pipe 5 and an open flame burner 7 described below, and the other opening 11b extracts molten slag. Has become a mouth. The molten slag extraction port 11b has four triangular notches 12 in the circular opening 12a.
b is provided at equal intervals (see FIG. 3). Reference numeral 13 denotes two rails provided on the outer circumference of the body of the furnace body 10, and the respective opposing side surfaces of the rails 13 and 13 are adapted to contact a stopper roller 13a attached to a support base 16 described below.

【0007】前記回転機構15は、図2,4に示すよう
に、上面に前記炉本体10の各レール13を支持する各
一対のコロ17を備えた支持台16と、この支持台16
の側方に前記レール13,13間に位置するように起立
して設けた支持板19と、前記支持台16に設置され、
少なくとも前記コロ17の一つを駆動するモータ18と
からなる。
As shown in FIGS. 2 and 4, the rotating mechanism 15 has a support base 16 provided with a pair of rollers 17 for supporting the rails 13 of the furnace body 10 on the upper surface, and the support base 16.
A support plate 19 standing upright so as to be located between the rails 13 and 13, and installed on the support base 16.
It comprises at least a motor 18 for driving one of the rollers 17.

【0008】前記傾動機構20は地上に設置され、上部
に軸受22を備えた支持柱21と、該支持柱21に設け
たモータあるいはハンドル23等からなり、前記支持板
19の上部中央から外方に突出した回転軸24を前記軸
受22を介してモータ23に連結し、モータ23の駆動
により炉本体10を所定角度傾動するようになってい
る。
The tilting mechanism 20 is installed on the ground, and is composed of a support column 21 having a bearing 22 on the upper portion thereof, a motor or a handle 23 provided on the support column 21, and the like. The rotating shaft 24 protruding to the above is connected to the motor 23 via the bearing 22, and the driving of the motor 23 tilts the furnace body 10 by a predetermined angle.

【0009】前記灰ペレット供給管5と直火バーナ7と
は、図2,4に示すように前記開口部11aを閉鎖し、
相対回転可能に適宜手段にて着脱可能な円板状カバー2
5の中心に対して対称位置に円板状カバー25を貫通し
て設けられたもので、灰ペレット供給管5の先端は、灰
ペレットWを炉本体10の溶融貯留部Aに供給できるよ
うに炉内に突出している。また、直火バーナ7は、実施
例においては酸素バーナであり、O2源とLPG等の燃
料源に接続されている。なお、O2源を空気吸着分離機
(PSA)としてもよい。
The ash pellet supply pipe 5 and the open flame burner 7 close the opening 11a as shown in FIGS.
A disk-shaped cover 2 which is relatively rotatable and can be attached and detached by an appropriate means.
5 is provided so as to penetrate the disk-shaped cover 25 at a symmetrical position with respect to the center of the ash pellet 5, and the tip of the ash pellet supply pipe 5 can supply the ash pellet W to the molten reservoir A of the furnace body 10. It projects into the furnace. Further, the direct flame burner 7 is an oxygen burner in the embodiment, and is connected to an O 2 source and a fuel source such as LPG. The O 2 source may be an air adsorption separator (PSA).

【0010】前記フード26は下方に開放するとともに
上部一側に開口部27を備えたもので、図示しないレー
ル上に載置され、ロッド先端にスプリング等の弾性体2
9を備えたシリンダ28により図2に示すように前記炉
本体10の開口部11b外方に近接し、また、シリンダ
28によりa方向に移動して炉本体10から離間するよ
うになっている。また、フード26にはフード内に連通
する廃気管30が取り付けられ、この廃気管30は摺動
継手31を介して排気ファン32に接続するバグフィル
タ33に接続している。
The hood 26 is opened downward and has an opening 27 on one side of the upper part. The hood 26 is mounted on a rail (not shown), and the elastic body 2 such as a spring is attached to the tip of the rod.
As shown in FIG. 2, a cylinder 28 provided with 9 is arranged to approach the outside of the opening 11b of the furnace main body 10, and is moved in the direction a by the cylinder 28 to be separated from the furnace main body 10. A waste air pipe 30 communicating with the inside of the hood is attached to the hood 26, and the waste air pipe 30 is connected to a bag filter 33 connected to an exhaust fan 32 via a sliding joint 31.

【0011】つぎに、前記構成からなる溶融炉Tの操業
について説明する。まず、図2に示すように、炉本体1
0を水平状態とするとともに、開口部11aに灰ペレッ
ト供給管5と直火バーナ7とを取り付けた円板状カバー
25を図示しない手段で相対回転自在に取り付け、か
つ、フード26をシリンダ28で移動してその開口部2
7で前記炉本体10の開口部11bの外方を覆う一方、
排気ファン32を駆動する。
Next, the operation of the melting furnace T having the above construction will be described. First, as shown in FIG. 2, the furnace body 1
0 is in a horizontal state, the ash pellet supply pipe 5 and the open flame burner 7 are attached to the opening 11a so as to be rotatable relative to each other by means not shown, and the hood 26 is attached to the cylinder 28. Moving and opening 2
While covering the outside of the opening 11b of the furnace body 10 with 7,
The exhaust fan 32 is driven.

【0012】そして、モータ18により前記ローラ17
を回転することにより炉本体10を回転しながら直火バ
ーナ7を点火して炉本体10を加熱し、炉温が700〜
800℃になると、灰ペレットWを灰ペレット供給装置
4から一定割合で炉内に供給する。そして、灰ペレット
Wが炉内の溶融貯留部Aの容積の0.7〜0.8(図5
参照)に達すると、一時灰ペレットWの炉内投入を停止
して昇温のみを続行し、灰ペレットWが溶融スラグ状態
(炉温がたとえば1400℃)となると、再度灰ペレッ
トWを炉内に連続投入する。この場合、灰ペレットWは
図5に示すように溶融貯留部Aの一炉壁側から投入され
るため、炉本体10の回転にともない溶融スラグSに巻
込まれるように溶融スラグS内に供給され、急速に溶融
される。
Then, the roller 17 is driven by the motor 18.
By rotating the furnace body 10 to ignite the open flame burner 7 to heat the furnace body 10, and the furnace temperature is 700 to
When the temperature reaches 800 ° C., the ash pellets W are supplied from the ash pellet supply device 4 into the furnace at a constant rate. Then, the ash pellet W has a volume of 0.7 to 0.8 (FIG.
When the ash pellets W are in a molten slag state (the furnace temperature is, for example, 1400 ° C.), the ash pellets W are temporarily charged in the furnace again. Continuously add to. In this case, since the ash pellets W are charged from one furnace wall side of the melting storage portion A as shown in FIG. 5, the ash pellets W are supplied into the molten slag S so as to be caught in the molten slag S as the furnace body 10 rotates. , Rapidly melted.

【0013】前記のように、灰ペレットWの連続投入に
より溶融スラグS面が上昇し、開口部11bの切欠き1
2bが最下点に達すると、溶融スラグSが一定量流出
し、この流出溶融スラグSは下方の水封ピット40内に
落下し、冷却水により冷却固化したのち、コンベア41
により所定場所に搬出される。なお、前記炉本体10は
2分間で1回転し、1分間に2回の割合で溶融スラグS
を流出させるのが好ましい。
As described above, the molten slag S surface rises due to the continuous charging of the ash pellets W, and the notch 1 of the opening 11b is formed.
When 2b reaches the lowest point, a certain amount of the molten slag S flows out, the outflowing molten slag S falls into the water sealing pit 40 below, and is cooled and solidified by the cooling water, and then the conveyor 41.
Is carried out to a predetermined place. The furnace body 10 rotates once every two minutes, and the molten slag S is melted at a rate of twice a minute.
Is preferably drained.

【0014】溶融炉Tの操業を停止するには、灰ペレッ
トWの炉内供給を停止するとともに直火バーナ7を消化
すると同時に炉本体10の回転を停止し、炉内温度が一
定温度に低下した後、排気ファン32の駆動を停止す
る。そして、炉本体10から円板状カバー25を取り外
すとともに、シリンダ28によりフード26を炉本体1
0から離間する。
In order to stop the operation of the melting furnace T, the supply of ash pellets W in the furnace is stopped, the open flame burner 7 is extinguished, and at the same time the rotation of the furnace body 10 is stopped so that the temperature in the furnace falls to a constant temperature. After that, the drive of the exhaust fan 32 is stopped. Then, the disk-shaped cover 25 is removed from the furnace body 10, and the hood 26 is attached to the furnace body 1 by the cylinder 28.
Separate from 0.

【0015】つぎに、モータあるいはハンドル23を操
作して炉本体10の開口部11bを下方に傾動させ、炉
内の溶融貯留部Aに残っている溶融スラグSを水封ピッ
ト40に投入する。その後、炉本体10を水平状態に戻
すとともに、フード26および円板状カバー25を元の
状態として次の操業を待機するものである。
Next, the motor or the handle 23 is operated to tilt the opening 11b of the furnace body 10 downward, and the molten slag S remaining in the molten storage portion A in the furnace is charged into the water sealing pit 40. After that, the furnace body 10 is returned to the horizontal state, and the hood 26 and the disk-shaped cover 25 are returned to the original state to stand by for the next operation.

【0016】なお、前記説明では、直火バーナ7を灰ペ
レット供給管5側に配設し酸素バーナとしたが、図6に
示すようにフード側に配設してもよい。また、焼却灰も
ペレット化することなく灰状のものでもよい。この場
合、灰を前述のように溶融貯留部Aの炉壁側から供給す
ると、溶融スラグSに巻き込まれて溶融スラグS内に供
給されるから、ほとんど飛散することなく溶融すること
ができる。さらに、焼却灰は下水汚泥焼却灰に限らない
ことは言うまでもない。
In the above description, the open flame burner 7 is arranged on the ash pellet supply pipe 5 side to be an oxygen burner, but it may be arranged on the hood side as shown in FIG. Also, the incinerated ash may be in the form of ash without being pelletized. In this case, if the ash is supplied from the furnace wall side of the molten storage portion A as described above, it is caught in the molten slag S and supplied into the molten slag S, so that the ash can be melted with almost no scattering. Further, it goes without saying that the incineration ash is not limited to the sewage sludge incineration ash.

【0017】[0017]

【発明の効果】以上の説明で明らかなように、請求項1
の発明によれば焼却灰は回転する炉本体内で溶融し、こ
の溶融スラグは炉内壁を順次接触するため、従来の溶融
貯留部を固定したものと異なり侵蝕が炉内壁全面にわた
って均一に進行し、耐火材侵蝕の影響の大きい炉本体の
寿命を大巾に延ばすことができる。請求項2のように直
火バーナを酸素バーナとすれば、高温火炎が得られ、そ
の輻射熱伝達効果による溶融の高効率化を得ることがで
きるとともに、低Nox化、廃ガス量低下による焼却灰
の炉外飛散を低下することができる。請求項3のように
焼却灰をペレットとすれば、炉内供給量を正確にコント
ロールすることができるとともに、投入時の飛散を防止
できる。請求項4に示すように溶融炉を構成すれば、前
記効果の他に、炉本体の両側に位置するフードおよび直
火バーナと焼却灰供給管を炉本体から分離できるため、
傾動機構により炉本体の貯留部に残る溶融物も容易に流
出することができる。しかも、炉本体は略円筒形で単純
な形状であるため耐火材の張替えも容易に行なうことが
できるという効果を奏する。
As is apparent from the above description, claim 1
According to the invention of claim 1, since the incineration ash is melted in the rotating furnace body, and this molten slag sequentially contacts the inner wall of the furnace, the erosion progresses uniformly over the entire inner wall of the furnace unlike the conventional one in which the molten reservoir is fixed. The life of the furnace body, which is greatly affected by the corrosion of the refractory material, can be greatly extended. When the direct-burning burner is an oxygen burner as in claim 2, a high-temperature flame can be obtained, and the efficiency of melting can be improved by the radiant heat transfer effect thereof. Outside the furnace can be reduced. When the incinerated ash is formed into pellets as in the third aspect, it is possible to accurately control the supply amount in the furnace and prevent scattering at the time of charging. If the melting furnace is configured as shown in claim 4, in addition to the above effects, the hood and the open flame burners and the incinerator ash supply pipe located on both sides of the furnace body can be separated from the furnace body.
The tilting mechanism also allows the melt remaining in the storage portion of the furnace body to easily flow out. Moreover, since the furnace body is substantially cylindrical and has a simple shape, the refractory material can be replaced easily.

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

【図1】 本発明にかかる溶融炉とその操業フローを示
す図。
FIG. 1 is a diagram showing a melting furnace according to the present invention and an operation flow thereof.

【図2】 溶融炉の断面図。FIG. 2 is a sectional view of a melting furnace.

【図3】 図2の開口部(抽出口)の拡大正面図。FIG. 3 is an enlarged front view of the opening (extraction port) of FIG.

【図4】 図2の側面図。FIG. 4 is a side view of FIG.

【図5】 図2のV−V線断面図。5 is a sectional view taken along line VV of FIG.

【図6】 溶融炉の他の実施例を示す部分断面図。FIG. 6 is a partial sectional view showing another embodiment of the melting furnace.

【符号の説明】[Explanation of symbols]

4…灰ペレット供給装置、5…灰ペレット供給管、7…
直火バーナ、10…炉本体、10a…断熱材、11a,
11b…開口部、13…レール、15…回転機構、17
…コロ、18…モータ、20…傾動機構、21…支持
柱、22…軸受、23…ハンドル、24…回転軸、25
…円板状カバー、26…フード、32…排気ファン、3
3…バグフィルタ、40…水封ピット、W…灰ペレッ
ト。
4 ... Ash pellet supply device, 5 ... Ash pellet supply pipe, 7 ...
Open flame burner, 10 ... Furnace body, 10a ... Insulation material, 11a,
11b ... Aperture, 13 ... Rail, 15 ... Rotation mechanism, 17
... roller, 18 ... motor, 20 ... tilting mechanism, 21 ... support pillar, 22 ... bearing, 23 ... handle, 24 ... rotary shaft, 25
… Disc-shaped cover, 26… Hood, 32… Exhaust fan, 3
3 ... Bag filter, 40 ... Water sealing pit, W ... Ash pellet.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 青葉 隆生 大阪府大阪市西区京町堀2丁目4番7号 中外炉工業株式会社内 (72)発明者 坂口 良人 大阪府大阪市西区京町堀2丁目4番7号 中外炉工業株式会社内 (72)発明者 村田 悦夫 大阪府八尾市上尾町5丁目1番地の8 株 式会社ナニワ炉機研究所内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Takao Aoba 2-4-7 Kyomachibori, Nishi-ku, Osaka-shi, Osaka Inside Chugai Furnace Industry Co., Ltd. (72) Yoshito Sakaguchi 2-chome, Kyomachibori, Nishi-ku, Osaka-shi, Osaka No. 4-7 Chugai Furnace Industry Co., Ltd. (72) Inventor, Etsue Murata Eight-share company, Naniwa Reactor Research Institute, 5-1, Ageo-cho, Yao-shi, Osaka

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 水平軸を中心として回転可能な炉本体内
に焼却灰を投入し、前記炉本体を回転させながら直火バ
ーナにより前記焼却灰を加熱して溶融することを特徴と
する焼却灰の溶融方法。
1. An incinerator ash which is put into a furnace body rotatable about a horizontal axis, and the incinerator ash is heated and melted by an open flame burner while rotating the furnace body, and the incinerator ash is melted. Melting method.
【請求項2】 前記直火バーナが酸素バーナであること
を特徴とする前記請求項1に記載の焼却灰の溶融方法。
2. The method for melting incineration ash according to claim 1, wherein the direct burner is an oxygen burner.
【請求項3】 前記焼却灰がペレット化されたものであ
ることを特徴とする前記請求項1,2のいずれかに記載
の焼却灰の溶融方法。
3. The method for melting incinerated ash according to claim 1, wherein the incinerated ash is pelletized.
【請求項4】 耐火断熱材が内張され、かつ、両端開口
部が小径となった横設置型略円筒体の炉本体と、該炉本
体を支持して回転させる回転機構と、前記開口部のいず
れか一方に取付ける直火バーナと、前記開口部の一方に
取り付ける焼却灰供給管と、前記他方の開口部を囲むフ
ードと、前記炉本体を傾動させる傾動機構とからなり、
前記直火バーナにより溶融された焼却灰溶融物を前記他
方の開口部から排出するようにしたことを特徴とする焼
却灰の溶融炉。
4. A furnace body of a horizontal installation type substantially cylindrical body in which a refractory heat insulating material is lined and openings at both ends have a small diameter, a rotating mechanism for supporting and rotating the furnace body, and the opening. An open flame burner attached to any one of the above, an incinerator ash supply pipe attached to one of the openings, a hood surrounding the other opening, and a tilting mechanism for tilting the furnace body,
The incinerator ash melting furnace, wherein the incinerated ash melted by the open flame burner is discharged from the other opening.
JP7280385A 1995-10-27 1995-10-27 Method for melting incineration ashe and its melting furnace Pending JPH09117733A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7280385A JPH09117733A (en) 1995-10-27 1995-10-27 Method for melting incineration ashe and its melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7280385A JPH09117733A (en) 1995-10-27 1995-10-27 Method for melting incineration ashe and its melting furnace

Publications (1)

Publication Number Publication Date
JPH09117733A true JPH09117733A (en) 1997-05-06

Family

ID=17624292

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7280385A Pending JPH09117733A (en) 1995-10-27 1995-10-27 Method for melting incineration ashe and its melting furnace

Country Status (1)

Country Link
JP (1) JPH09117733A (en)

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