JPH0810734Y2 - Waste liquid processing equipment - Google Patents

Waste liquid processing equipment

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Publication number
JPH0810734Y2
JPH0810734Y2 JP1993012491U JP1249193U JPH0810734Y2 JP H0810734 Y2 JPH0810734 Y2 JP H0810734Y2 JP 1993012491 U JP1993012491 U JP 1993012491U JP 1249193 U JP1249193 U JP 1249193U JP H0810734 Y2 JPH0810734 Y2 JP H0810734Y2
Authority
JP
Japan
Prior art keywords
waste
hearth
furnace
heating fluid
waste liquid
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 - Lifetime
Application number
JP1993012491U
Other languages
Japanese (ja)
Other versions
JPH0674825U (en
Inventor
茂 山崎
Original Assignee
大阪熱管理工業株式会社
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 大阪熱管理工業株式会社 filed Critical 大阪熱管理工業株式会社
Priority to JP1993012491U priority Critical patent/JPH0810734Y2/en
Publication of JPH0674825U publication Critical patent/JPH0674825U/en
Application granted granted Critical
Publication of JPH0810734Y2 publication Critical patent/JPH0810734Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Incineration Of Waste (AREA)

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】本考案は、各種産業の生産設備や
消費設備などから発生する廃液や廃棄物、あるいは水処
理装置で水処理された後に残留する廃液や含水率の高い
廃棄物の処理装置に関する。
[Industrial application] The present invention is intended to treat waste liquids and wastes generated from production and consumption facilities of various industries, or waste liquids and wastes having a high water content remaining after water treatment by a water treatment device. Regarding the device.

【0002】[0002]

【従来の技術】90%以上の含水率の高い廃液等の廃棄
物を処理する方法としては、大別して水処理によって行
う場合と、濃縮焼却して処理する方法がある。
2. Description of the Related Art As a method for treating waste such as a waste liquid having a high water content of 90% or more, there are roughly classified water treatment and concentrated incineration treatment.

【0003】前者の水処理方法では、有機質や特に溶剤
を含んだ廃水を水処理によって処理するには大きな設置
面積と設備を必要とするばかりでなく維持管理のための
ランニングコストが嵩み、且つ例え水処理を行っても最
終的には汚泥が発生し、これを焼却しなければならな
い。また水処理後の処理水も水質汚濁法の規制により規
制値以下に落とすことは非常に困難であり、これを外部
に放流することができないのが現状である。
In the former water treatment method, not only a large installation area and equipment are required to treat wastewater containing organic substances and especially solvents by water treatment, but also running costs for maintenance are high, and Even if water is treated, sludge will eventually be generated and must be incinerated. In addition, it is very difficult to reduce the treated water after the water treatment to the regulated value or less due to the regulation of the Water Pollution Law, and it is the current situation that this cannot be discharged to the outside.

【0004】また後者の濃縮焼却処理方法では、廃液等
の廃棄物を濃縮装置で水分を蒸発させて焼却可能な程度
まで乾燥させた上で焼却処理を行っているが、この場合
でも濃縮装置での濃縮効率が悪いため、大きな設置面
積、設備費、人件費、あるいは維持管理のためのランニ
ングコストが嵩み、企業の廃液、廃棄物処理に対する悩
みは深刻なものがある。
In the latter method of concentrating incineration, the waste such as waste liquid is incinerated after being dried to the extent that it can be incinerated by evaporating the water content in the concentrating device. Due to its poor efficiency of concentration, large installation area, equipment cost, labor cost, or running cost for maintenance and management increase, and there are serious worries about waste liquid and waste treatment by companies.

【0005】[0005]

【考案が解決しようとする課題】本考案は、上述の問題
点に鑑み、生産設備や消費設備あるいは水処理設備より
発生する廃液等の含水率の高い廃棄物を加熱蒸気等の加
熱流体による間接加熱によって効率的に蒸発させて焼却
処理を容易することを目的とする。
SUMMARY OF THE INVENTION In view of the above problems, the present invention is directed to the indirect use of heating fluid such as heating steam with waste having a high water content such as waste liquid generated from production equipment, consumption equipment or water treatment equipment. The purpose is to evaporate efficiently by heating to facilitate the incineration process.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に、請求項1の考案に係る廃棄物処理装置にあっては、
参照符号を付して示せば、炉本体1に多段状に複数の炉
床2を設けると共に、炉床2に環状の加熱用流体流通
用中空部3を径方向適当間隔に多重層に形成して該炉床
表面4が凹凸状に形成すると共に、該炉床2の一部を切
欠して廃棄物の落下口9を形成し、該落下口9を挟んで
その周辺に前記中空部3に連通する加熱用流体流入菅1
0と加熱用流体流出菅11とを設け、且つ少なくとも前
記流入菅10と流出菅11とに沿う部分に堰壁12,1
3を、流入菅側堰壁12が流出菅側堰壁13よりも高く
なるよう突設し、該炉本体1の中心部に回転軸5を縦設
し、該回転軸5に放射状に水平アーム6を周方向に複数
個突設し、これらの水平アーム6に前記凹凸状炉床面4
上の廃棄物を周方向に移送する吊り環状の移送用紐状体
7を吊設してなる構成を採用するものである。
In order to achieve the above object, in the waste treatment apparatus according to the invention of claim 1,
If indicated by reference numerals, the furnace body 1 is provided with a plurality of hearths 2 in multiple stages, and annular hearths 3 for heating fluid flow are formed in each hearth 2 in multiple layers at appropriate radial intervals. Then, the hearth surface 4 is formed to have an uneven shape, and a part of the hearth 2 is cut out to form a drop port 9 for waste, and the hollow part 3 is provided around the drop port 9 to sandwich it. Fluid inflow pipe 1 communicating with
0 and a heating fluid outflow tube 11 are provided, and weir walls 12, 1 are provided at least along the inflow tube 10 and the outflow tube 11.
3, the inflow pipe side weir wall 12 is projected so as to be higher than the outflow pipe side weir wall 13, a rotary shaft 5 is vertically provided in the center of the furnace body 1, and a horizontal arm is radially provided on the rotary shaft 5. A plurality of 6 are projected in the circumferential direction, and the uneven hearth surface 4 is provided on these horizontal arms 6.
A configuration is adopted in which a suspending annular transfer string 7 for suspending the above waste in the circumferential direction is suspended.

【0007】[0007]

【作用】請求項1の考案に係る廃棄物処理装置によれ
ば、廃液等の廃棄物を炉本体1の炉床2に設けた環状中
空部3を流通する加熱用流体の熱交換によって炉床表面
4からの間接加熱により該廃棄物に含まれる水分を蒸発
させて濃縮することを特徴とする。廃棄物を直接的に焼
却用バーナーなどで加熱することも考えられるが、この
場合には熱損失が大きく、また排煙の発生率が大である
が、本考案のように廃棄物を加熱管などで間接加熱し、
水分を蒸発させるようにすることによって熱エネルギー
を有効に利用することができると共に、排煙の発生がな
く公害の発生率が格段に少なく、その後の焼却処理を容
易することができる。
According to the waste treatment apparatus of the first aspect of the present invention, waste such as waste liquid is exchanged through the annular hollow portion 3 provided in the hearth 2 of the furnace body 1 by heat exchange with the heating fluid. It is characterized in that the water contained in the waste is evaporated and concentrated by indirect heating from the surface 4. It may be possible to heat the waste directly with a burner for incineration, but in this case, the heat loss is large and the smoke generation rate is large, but as in the present invention, the waste is heated by a heating pipe. Indirect heating with
By evaporating the water content, the thermal energy can be effectively used, the smoke generation is not generated, and the generation rate of pollution is remarkably low, and the subsequent incineration process can be facilitated.

【0008】また本考案によれば、炉床表面4の内部に
加熱用流体流通用中空部3を形成することによって炉床
表面4が凹凸状となり、炉床表面4に接触する廃棄物の
接触面積が大となってそれだけ熱効率がよく、廃棄物に
含有する水分の蒸発を促進する作用がある。
Further, according to the present invention, by forming the heating fluid circulating hollow portion 3 inside the hearth surface 4, the hearth surface 4 becomes uneven, and the contact of the waste material contacting the hearth surface 4 Since the area is large, the thermal efficiency is high, and it has the effect of promoting the evaporation of the water contained in the waste.

【0009】更にまた本考案によれば、炉床2の一部を
切欠して廃棄物の落下口9を形成し、該落下口9を挟ん
でその周辺に前記中空部3に連通する加熱用流体流入菅
10と加熱用流体流出菅11とを設け、且つ少なくとも
前記流入菅10と流出菅11とに沿う部分に堰壁12,
13を、流入菅側堰壁12が流出菅側堰壁13よりも高
くなるよう突設してなるため、炉床2上の含水率の高い
廃棄物は炉床2上の堰壁12,13によって外部に溢流
することなく滞留せしめた状態で加熱蒸発されると共
に、蒸発されないで残留した廃棄物は突出量の低い流出
菅側堰壁13より、該堰壁13を溢流して落下口9より
下方の炉床2上に順次落下せしめられ、このようにして
該下方の炉床2上に順次落下する間に、廃棄物に含んだ
水分は完全に蒸発させられ、これによって廃棄物を焼却
可能の程度まで確実に乾燥させることができる。
Furthermore, according to the present invention, a part of the hearth 2 is cut away to form a waste material drop port 9, and the drop port 9 is sandwiched between the hollow part 3 for heating. A fluid inflow pipe 10 and a heating fluid outflow pipe 11 are provided, and a weir wall 12, at least in a portion along the inflow pipe 10 and the outflow pipe 11.
Since the inflow pipe side weir wall 12 is provided so as to be higher than the outflow pipe side weir wall 13, the wastes having a high water content on the hearth 2 are the weir walls 12, 13 on the hearth 2. The waste that is not vaporized is heated and vaporized in a state of being retained without overflowing to the outside, and the waste that has not been vaporized overflows the weir wall 13 from the outflow pipe side weir wall 13 with a small amount of protrusion and falls through the fall port 9 The water contained in the waste is completely evaporated during the successive drops on the lower hearth 2 and thus on the lower hearth 2, thereby incinerating the waste. It can be dried to the extent possible.

【0010】また本考案によれば、炉本体1の中心部に
回転軸5を縦設し、該回転軸5に放射状に水平アーム6
を周方向に複数個突設し、これらの水平アーム6に前記
凹凸状炉床面4上の廃棄物を周方向に移送する吊り環状
の移送用紐状体7を吊設してなることを特徴とする。炉
本体1に投入された廃棄物は、炉床2の表面4からの熱
源に触れて加熱されることになるが、これら廃棄物に対
して加熱効率を上げるために炉床表面4に載置される廃
棄物を順次周方向に移送しながら攪拌加熱する必要があ
る。この移送手段として、本考案は上述のように炉本体
1の中心部に回転軸5を縦設し、該回転軸5に放射状に
水平アーム6を周方向に複数個突設し、これらの水平ア
ーム6に移送用紐状体7を吊設し、該移送用紐状体7が
炉床表面4に接触しながら且つ該表面4上の廃棄物を周
方向に攪拌移送するようになっている。移送用紐状体4
は、廃棄物を攪拌移送する役割と共に、該紐状体4が炉
床表面4に接触しながら周方向に移動することによって
炉床表面4を常に清掃して該表面4に廃棄物が付着しな
いようにする役目を有し、これによって長期間使用する
も熱効率の減退を防止するようになっている。
Further, according to the present invention, the rotary shaft 5 is vertically installed at the center of the furnace body 1, and the horizontal arms 6 are radially arranged on the rotary shaft 5.
A plurality of projections in the circumferential direction, and a suspension ring-shaped transfer string 7 for suspending the waste on the uneven hearth surface 4 in the circumferential direction is hung on these horizontal arms 6. Characterize. The wastes thrown into the furnace body 1 are heated by touching the heat source from the surface 4 of the hearth 2. The wastes are placed on the hearth surface 4 in order to increase the heating efficiency of these wastes. It is necessary to stir and heat the generated waste while sequentially transferring it in the circumferential direction. As the transfer means, the present invention has a rotary shaft 5 vertically installed at the center of the furnace body 1 as described above, and a plurality of horizontal arms 6 are radially provided on the rotary shaft 5 so as to project in the circumferential direction. A transfer string 7 is suspended on the arm 6 so that the transfer string 7 is in contact with the hearth surface 4 and the waste on the surface 4 is stirred and transferred in the circumferential direction. . Transport string 4
Has a role of stirring and transferring the waste, and the string-shaped body 4 moves in the circumferential direction while being in contact with the hearth surface 4 so that the hearth surface 4 is always cleaned so that the waste does not adhere to the surface 4. This has the function of preventing the deterioration of thermal efficiency even after long-term use.

【0011】しかるに、炉床2には、間接加熱手段とし
て、環状の加熱用流体流通用中空部3が径方向適当間隔
に多重層に形成されて該炉床表面4が凹凸状を呈してい
るため、単に移送用紐状体7を炉床表面4に垂らすだけ
では、該紐状体7は凹凸状表面4の凹部4aには比較的
に接触度はよいが、凸部4bに該紐状体4が接触しない
か接触度が不十分であるという現象が生じる。
However, in the hearth 2, as an indirect heating means, annular heating fluid circulating hollow portions 3 are formed in multiple layers at appropriate radial intervals so that the hearth surface 4 has an uneven shape. Therefore, if the transfer cord 7 is simply hung on the hearth surface 4, the cord 7 has a relatively good contact with the concave portion 4a of the uneven surface 4, but the protrusion 4b has the cord shape. The phenomenon that the body 4 does not contact or the degree of contact is insufficient occurs.

【0012】本考案は、この点に注目して移送用紐状体
7を輪状、即ち吊り環状にして水平アームに吊設するこ
とによって、該紐状体7の環状部が凸部4bに充分に接
触することが分かった。このように本考案によれば、移
送用紐状体7を吊り環状に形成することよって、炉床表
面4の全域を該移送用紐状体7によって均一に清掃する
ことができ、これによって該表面4の清掃効率を上げる
ことになり、長期間にわたって安定した熱効率を上げる
ことができるに至ったものである。
In the present invention, paying attention to this point, the transfer string-like body 7 is looped, that is, hung on a horizontal arm so that the annular part of the string-like body 7 is sufficiently formed on the convex portion 4b. Was found to come into contact with. As described above, according to the present invention, by forming the transfer cord-shaped body 7 in a suspension ring shape, the entire area of the hearth surface 4 can be uniformly cleaned by the transfer cord-shaped body 7. The cleaning efficiency of the surface 4 is improved, and the stable thermal efficiency can be improved over a long period of time.

【0013】[0013]

【実施例】図1は、本考案の一実施例を示し、多段廃液
処理炉を示す。該図において、多段廃液処理炉を形成す
る竪形炉本体1には、その内壁に沿って上下に多段状に
加熱用炉床2が設けられている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an embodiment of the present invention, showing a multi-stage waste liquid treatment furnace. In the figure, a vertical furnace body 1 forming a multi-stage waste liquid treatment furnace is provided with heating hearths 2 in multi-steps vertically along the inner wall thereof.

【0014】該炉床2には、図2(a)にも良く示され
るように、円環状の加熱用流体流通用中空部3が同心状
に多重層に設けられ、その各円環状の中空部3の一部は
切欠されて落下口9を形成し、その落下口9を挟んで各
中空部3に連通する流入管10と排出管11とが略径方
向に設けられている。このように炉床2には円環状の中
空部3が多重層に形成されているため、炉床表面4は図
1に良く表れているように凹凸状を呈している。このよ
うに炉床2の表面4が凹凸状を呈するため、廃棄物に対
する接触面接が大となって熱効率を上げ、それだけ廃棄
物に含有する水分の蒸発を速めることができる。
As shown in FIG. 2 (a), the hearth 2 is provided with a plurality of annular heating fluid circulating hollow portions 3 concentrically in multiple layers. A part of the portion 3 is cut out to form a drop port 9, and an inflow pipe 10 and a discharge pipe 11 which communicate with each hollow portion 3 with the drop port 9 sandwiched therebetween are provided in a substantially radial direction. Since the annular hollow portion 3 is formed in multiple layers in the hearth 2 as described above, the hearth surface 4 has an uneven shape as well shown in FIG. In this way, since the surface 4 of the hearth 2 has an uneven shape, the contact surface contact with the waste becomes large, the thermal efficiency is increased, and the evaporation of the moisture contained in the waste can be accelerated accordingly.

【0015】図2の(b)は、上記落下口9を挟んだ断
面を示すもので、各加熱用炉床2の上面において前記流
入管10に沿った部分と、前記排出管11に沿った部分
と、炉床5の中心側の部分、即ち回転軸5側の端縁とに
はそれぞれ堰壁12,13,14が設けられ、そのうち
排出管11に沿う堰壁13の高さは他の堰壁12,14
よりも若干低く形成され、これによって炉床2上に滞留
する廃液が流入管10側の炉床2上面から矢印のように
排出管11側上面に移送され、落下口9から廃液が次段
の炉床2上に落下するようにしてある。
FIG. 2 (b) shows a cross section sandwiching the above-mentioned dropping port 9, and a portion along the inflow pipe 10 on the upper surface of each heating hearth 2 and along the discharge pipe 11 are shown. Weir walls 12, 13, and 14 are provided in the portion and the center-side portion of the hearth 5, that is, the end on the rotating shaft 5 side, of which the height of the weir wall 13 along the discharge pipe 11 is different. Weir walls 12, 14
It is formed to be slightly lower than that, whereby the waste liquid staying on the hearth 2 is transferred from the upper surface of the hearth 2 on the side of the inflow pipe 10 to the upper surface of the discharge pipe 11 as shown by the arrow, and the waste liquid is discharged from the drop port 9 to the next stage. It is designed to fall onto the hearth 2.

【0016】また図3に示すように、炉本体1の中心部
に、炉本体1の下部に設置された電動機(図示せず)に
よって回転駆動する回転軸5が縦設され、該回転軸5に
放射状に延びる水平アーム6が周方向等間隔に4本突設
され、これらの水平アーム6に前記凹凸状炉床面4上の
廃棄物を周方向に移送する金属チェン等からなる移送用
紐状体7,8が吊設され、その下端部は炉床2の炉床表
面4に充分に接触している。従って、回転軸5の回転に
伴って移送用紐状体7,8は炉床表面4を摺接しながら
円運動を行うようになっている。
Further, as shown in FIG. 3, a rotary shaft 5 rotatably driven by an electric motor (not shown) installed in the lower part of the furnace body 1 is vertically installed at the center of the furnace body 1, and the rotary shaft 5 Four horizontal arms 6 that radially extend in the circumferential direction are projected at equal intervals in the circumferential direction, and a transfer string composed of a metal chain or the like for transferring the waste on the uneven hearth surface 4 to the horizontal arms 6 in the circumferential direction. The shaped bodies 7 and 8 are suspended, and the lower ends thereof are in sufficient contact with the hearth surface 4 of the hearth 2. Therefore, with the rotation of the rotary shaft 5, the transfer cord-shaped bodies 7 and 8 perform circular motion while slidingly contacting the hearth surface 4.

【0017】この移送用紐状体7,8は、図4の(a) 〜
(c) に示すように、その両端部が水平アーム6に連結さ
れて環状に形成された移送用紐状体8と一本の紐状体7
とを適当に組み合わせて設けられたもので、特に本考案
は環状に形成された移送用紐状体8を設けたことを特徴
とし、該環状の紐状体8によって炉床表面4の凹部のみ
ならず凸部にも該紐状体8が摺接して、炉床表面4を効
率的に清掃することができる。
The transfer cords 7 and 8 are shown in FIGS.
As shown in (c), both ends thereof are connected to the horizontal arm 6 to form a transfer string-like body 8 and a single string-like body 7.
In particular, the present invention is characterized in that the transfer cord-shaped member 8 formed in an annular shape is provided, and only the concave portion of the hearth surface 4 is provided by the annular cord-shaped member 8. Of course, the cord-like body 8 also comes into sliding contact with the convex portion, and the hearth surface 4 can be efficiently cleaned.

【0018】なお、炉本体1の頂部には炉本体内に発生
した廃棄蒸気(ベーパー)を送り出すためのベーパー管
15が設けられている。
At the top of the furnace body 1, there is provided a vapor pipe 15 for sending out waste steam (vapor) generated in the furnace body.

【0019】しかして、廃液ポンプ16により送液され
る廃液は廃液導入管17によって炉本体1の頂部より炉
床2上に導入される。炉床2上の廃液は堰壁12,13
に囲繞されて炉床2上に滞留される。
The waste liquid sent by the waste liquid pump 16 is introduced from the top of the furnace body 1 onto the hearth 2 by the waste liquid introducing pipe 17. The waste liquid on the hearth 2 is the weir walls 12, 13
And is retained on the hearth 2.

【0020】炉本体1内では、回転軸5から放射状に延
びる水平アーム6の移送用紐状体7が炉床2の凹凸状表
面4に充分な接触面積を持って接触し、矢印方向に一分
間に0.4〜3回転の割合でゆっくりと回転するように
なっており、これによって該廃液は、加熱用炉床2上に
おいて移送用紐状体7,8によって図3に示すように回
転軸5回りに順次攪拌移送され、その移送途上において
炉床表面4で間接加熱、即ち炉本体1に設けた加熱用流
体流通用中空部3を流通する加熱流体と熱交換が行わ
れ、水蒸気となって外部に排出されると共に、蒸発され
ないで残留した廃液は、突出量の低い堰壁13を溢流し
て、落下口9より下段の加熱用炉床2上に落下され、該
下段の炉床2上で同様に攪拌移送され、その移送途上で
該廃液に含まれた水分は蒸発して濃縮され、これによっ
て最終的に生成されたケーキ状物と濃縮液とからなる濃
縮物は更に落下口9から適宜焼却用炉床(図示せず)上
に落下され、ここで濃縮物は完全に焼却されることにな
る。なお、加熱用流体流通用中空部3には、焼却工程に
よって発生する高温の排気ガスからなる加熱流体を流通
させても、該排気ガスを伝熱ボイラーに導入して該熱源
によって加熱蒸気を発生させ、この加熱蒸気を流通させ
るようにしてもよい。
In the furnace main body 1, the transfer string 7 of the horizontal arm 6 extending radially from the rotary shaft 5 contacts the uneven surface 4 of the hearth 2 with a sufficient contact area, and moves in the direction of the arrow. It is designed to rotate slowly at a rate of 0.4 to 3 revolutions per minute, whereby the waste liquid is rotated on the heating hearth 2 by the transfer cords 7 and 8 as shown in FIG. The mixture is sequentially stirred and transferred around the shaft 5, and in the course of the transfer, indirect heating is performed on the hearth surface 4, that is, heat exchange is performed with the heating fluid flowing through the heating fluid distribution hollow portion 3 provided in the furnace body 1, and steam is generated. Then, the waste liquid remaining without being evaporated overflows the weir wall 13 with a small amount of projection, and is dropped onto the heating hearth 2 at the lower stage through the drop port 9, and the furnace floor at the lower stage is discharged. Similarly, the water contained in the waste liquid was agitated and transferred on 2 and the water contained in the waste liquid during the transfer. Is evaporated and concentrated, and the finally formed concentrate consisting of the cake and the concentrated liquid is further dropped from the dropping port 9 onto the incinerator hearth (not shown), where it is concentrated. The material will be completely incinerated. Even if a heating fluid composed of high-temperature exhaust gas generated in the incineration process is circulated in the heating fluid circulation hollow portion 3, the exhaust gas is introduced into a heat transfer boiler to generate heating steam by the heat source. Then, the heated steam may be circulated.

【0021】[0021]

【考案の効果】請求項1の考案に係る廃棄物処理装置に
よれば、炉床に設けた加熱用流体流通用中空部を流通さ
せる加熱流体の熱交換により、即ち間接加熱により該廃
液に含まれる水分を蒸発させて濃縮するようにしたた
め、熱エネルギーを有効に利用することができると共
に、排煙の発生がなく公害の発生率が格段に少ない処理
を行うことができる。
According to the waste treatment apparatus of the first aspect of the invention, the waste liquid is contained in the waste liquid by heat exchange of the heating fluid flowing through the heating fluid circulation hollow portion provided in the hearth, that is, by indirect heating. Since the generated water is evaporated and concentrated, the heat energy can be effectively used, and the treatment can be performed with no smoke emission and a significantly lower pollution rate.

【0022】また本考案によれば、廃棄物を連続的に移
送する移送用紐状体を熱交換面である炉床表面に接する
ようにして設けてなるため、その攪拌作用によって効率
的に水分を蒸発させることができると共に、該移送用紐
状体によって炉床表面を常に清掃して熱効率の減退を防
ぐことができる。
Further, according to the present invention, since the transfer cord-like body for continuously transferring the waste is provided so as to be in contact with the hearth surface which is the heat exchange surface, the stirring action thereof effectively causes the moisture content. In addition to being able to evaporate, the transfer-cord-like body can constantly clean the hearth surface to prevent a decrease in thermal efficiency.

【0023】また本考案によれば、上記移送用紐状体
は、輪状、即ち吊り環状に形成されてなるため、凹凸表
面を形成する炉床表面の表面全域に均一に移送用紐状体
が接触し、より一層炉床表面の清掃効率を上げることが
でき、これによる熱交換効率の減退を長期間にわたって
防ぐことができ、長期間安定して使用することが可能で
ある。
Further, according to the present invention, since the transfer string-like member is formed in a ring shape, that is, a hanging ring shape, the transfer string-like member is uniformly distributed over the entire surface of the hearth surface forming the uneven surface. By making contact with each other, it is possible to further improve the cleaning efficiency of the hearth surface, it is possible to prevent a decrease in heat exchange efficiency due to this, for a long period of time, and it is possible to use it stably for a long time.

【0024】また本考案によれば、炉床表面の内部に加
熱用流体流通用中空部を形成することによって炉床表面
が凹凸状となり、炉床表面に接触する廃棄物の接触面積
が大となってそれだけ熱効率がよく、廃棄物に含有する
水分の蒸発を促進する効果がある。
Further, according to the present invention, by forming the heating fluid circulating hollow portion inside the hearth surface, the hearth surface becomes uneven, and the contact area of the waste material contacting the hearth surface is increased. As a result, the heat efficiency is good and it has the effect of promoting the evaporation of the water contained in the waste.

【0025】更にまた本考案によれば、炉床の一部を切
欠して廃棄物の落下口を形成し、該落下口を挟んでその
周辺に前記中空部に連通する加熱用流体流入菅と加熱用
流体流出菅とを設け、且つ少なくとも前記流入菅と流出
菅とに沿う部分に堰壁を、流入菅側堰壁が流出菅側堰壁
よりも高くなるよう突設してなるため、炉床上の含水率
の高い廃棄物は炉床上の堰壁によって外部に溢流するこ
となく滞留せしめた状態で加熱蒸発されると共に、蒸発
されないで残留した廃棄物は突出量の低い流出菅側堰壁
より、該堰壁を溢流して落下口より下方の炉床上に順次
落下せしめられ、このようにして該下方の炉床上に順次
落下する間に、廃棄物に含んだ水分は完全に蒸発させら
れ、これによって廃棄物を焼却可能の程度まで確実に乾
燥させることができる。
Further, according to the present invention, a part of the hearth is cut out to form a drop port for waste, and a heating fluid inflow pipe is provided around the drop port for communicating with the hollow portion. A heating fluid outflow pipe is provided, and a weir wall is provided at least along the inflow pipe and the outflow pipe so that the inflow pipe side weir wall is higher than the outflow pipe side weir wall. The waste with a high water content on the floor is heated and evaporated by the weir wall on the hearth without being spilled to the outside, and the waste that has not been evaporated remains on the outflow pipe side weir wall with a low protrusion amount. As a result, the overflow of the weir wall is caused to sequentially drop onto the hearth below the drop port, and the water contained in the waste is completely evaporated during the successive drops onto the hearth below. This ensures that the waste is dried to the extent that it can be incinerated. That.

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

【図1】本考案に係る廃液処理装置の一実施例を示す。FIG. 1 shows an embodiment of a waste liquid treatment apparatus according to the present invention.

【図2】図2(a)は、同装置の炉床の内部構造を一部
切欠して示す一部欠切平面図である。図2の(b)は、
同炉床の要部縦断面図である。
FIG. 2A is a partially cutaway plan view showing a partially cutaway internal structure of a hearth of the same apparatus. FIG. 2B shows
It is a principal part longitudinal cross-sectional view of the hearth.

【図3】同炉床の平面図である。FIG. 3 is a plan view of the hearth.

【図4】図4の(a)、(b)及び(c)はそれぞれ水
平アームに環状及び一条状の移送用紐状体を吊設して炉
床表面に接触した状態を示す説明図である。
4 (a), (b) and (c) of FIG. 4 are explanatory views showing a state in which a ring-shaped and linear strip-shaped transfer cord-like body is hung on a horizontal arm and is in contact with the hearth surface. is there.

【符号の説明】[Explanation of symbols]

1 炉本体 2 炉床 3 加熱用流体流通用中空部 4 炉床表面 5 回転軸 6 水平アーム 7 移送用紐状体 8 移送用紐状体 12 堰壁 13 堰壁 DESCRIPTION OF SYMBOLS 1 Furnace main body 2 Hearth 3 Hollow portion for heating fluid flow 4 Hearth surface 5 Rotating shaft 6 Horizontal arm 7 String for transfer 8 String for transfer 12 Weir wall 13 Weir wall

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】炉本体に多段状に設けた複数の各炉床に環
状の加熱用流体流通用中空部を径方向適当間隔に多重層
に形成して該炉床表面を凹凸状に形成すると共に、該炉
床の一部を切欠して廃棄物の落下口を形成し、該落下口
を挟んでその周辺に前記中空部に連通する加熱用流体流
入菅と加熱用流体流出菅とを設け、且つ少なくとも前記
流入菅と流出菅とに沿う部分に堰壁を、流入菅側堰壁が
流出菅側堰壁よりも高くなるよう突設し、該炉本体の中
心部に縦設した回転軸に放射状に水平アームを周方向に
複数個突設し、これらの水平アームに前記凹凸状炉床面
上の廃棄物を周方向に移送する吊り環状の移送用紐状体
を吊設してなる廃液等廃棄物の処理装置。
1. A furnace to form multi-layer in each of a plurality of hearth provided in the multi-stage in the main body of the heating fluid passing hollow portions of the annular radially appropriate intervals to form the furnace floor surface uneven With the furnace
Cut off a part of the floor to form a drop port for waste.
A heating fluid flow that communicates with the hollow portion around the
An inlet pipe and a heating fluid outlet pipe are provided, and at least the above
The weir wall is located along the inflow pipe and the outflow pipe, and the weir wall on the inflow pipe side is
Projected to be higher than the weir wall on the outflow pipe side , a plurality of horizontal arms are radially projected in the circumferential direction on a rotary shaft vertically provided at the center of the furnace body, and the uneven furnace is provided on these horizontal arms. An apparatus for treating waste such as waste liquid, in which a suspending ring-shaped transfer string-like object for suspending waste on the floor in the circumferential direction is suspended.
JP1993012491U 1993-03-19 1993-03-19 Waste liquid processing equipment Expired - Lifetime JPH0810734Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993012491U JPH0810734Y2 (en) 1993-03-19 1993-03-19 Waste liquid processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993012491U JPH0810734Y2 (en) 1993-03-19 1993-03-19 Waste liquid processing equipment

Publications (2)

Publication Number Publication Date
JPH0674825U JPH0674825U (en) 1994-10-21
JPH0810734Y2 true JPH0810734Y2 (en) 1996-03-29

Family

ID=11806867

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993012491U Expired - Lifetime JPH0810734Y2 (en) 1993-03-19 1993-03-19 Waste liquid processing equipment

Country Status (1)

Country Link
JP (1) JPH0810734Y2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5142435A (en) * 1974-10-09 1976-04-10 Nippon Telegraph & Telephone
JPS5315316A (en) * 1976-07-29 1978-02-13 Nissan Chem Ind Ltd Preparation of itaconic acid and citraconic acid

Also Published As

Publication number Publication date
JPH0674825U (en) 1994-10-21

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