JPH03284341A - Method and apparatus for granulation treatment of molten sludge - Google Patents
Method and apparatus for granulation treatment of molten sludgeInfo
- Publication number
- JPH03284341A JPH03284341A JP2081134A JP8113490A JPH03284341A JP H03284341 A JPH03284341 A JP H03284341A JP 2081134 A JP2081134 A JP 2081134A JP 8113490 A JP8113490 A JP 8113490A JP H03284341 A JPH03284341 A JP H03284341A
- Authority
- JP
- Japan
- Prior art keywords
- water
- disk
- sludge
- rotating disk
- melting furnace
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Treatment Of Sludge (AREA)
- Glanulating (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、熱風溶融炉により溶融された汚泥溶融体の造
粒処理方法及びその処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for granulating molten sludge melted in a hot-air melting furnace and a processing apparatus therefor.
従来艮生
シールドトンネル掘削工法による工事で排出される泥土
、浄水場での凝集沈澱工程から排出される含水泥土、下
水汚泥等の各種の汚泥の処分地の確保は近年大きな社会
問題となってきており、これらの汚泥の燃焼、溶融によ
る減容化だけでなく、再資源化が求められている。In recent years, securing a disposal site for various types of sludge, such as mud discharged from construction using the conventional Ashi shield tunnel excavation method, water-containing mud discharged from the coagulation and sedimentation process at water treatment plants, and sewage sludge, has become a major social issue in recent years. Therefore, in addition to reducing the volume of sludge by burning and melting it, recycling is required.
その−環として、本呂願人は、先に、特願平1−301
35号により、含水汚泥の乾燥、昇温、溶融を効果的に
組合せることにより、熱効率を高め、経済的に含水泥土
を溶融処理することのできる処理方法及びその装置を提
案した。As a link to this, Honro Ganto previously filed the patent application No. 1-301.
No. 35 proposed a treatment method and apparatus that can economically melt and process hydrous sludge by increasing thermal efficiency by effectively combining drying, heating, and melting of hydrous sludge.
これにより、各種汚泥の経済的な溶融処理が可能になり
、減容化が達成できるようになったが。This has made it possible to economically melt and process various types of sludge and achieve volume reduction.
従来、汚泥を溶融して得られた汚泥溶融体は、せいぜい
骨材、道路の敷石等に使用されるに過ぎなかった。Conventionally, sludge melts obtained by melting sludge have been used at most as aggregates, road paving stones, and the like.
そこで、汚泥溶融体を適当な粒径の球状体に造粒すれば
、その用途が拡大し、又付加価値も増大する。Therefore, if the sludge melt is granulated into spherical bodies with an appropriate particle size, its uses will be expanded and its added value will also increase.
さて、一般に溶融体を微小な小球状に造粒する手段とし
ては、水平回転円盤上面の中心にある高さから溶融体を
落下させることにより、円盤の回転により溶融体に与え
られる遠心力と、接線方向の力により溶融体の滴は円盤
上を半径方向及び円周方向に転動し球形に成形されて、
円盤周囲より空気中を落下しその間に冷却され、さらに
水中に落下させて冷却固化させる回転円盤型急速造粒機
が知られている。Now, generally speaking, as a means of granulating a molten material into minute spheres, the molten material is dropped from a height at the center of the upper surface of a horizontally rotating disk, and the centrifugal force applied to the molten material by the rotation of the disk; The tangential force causes the melt drop to roll on the disk in the radial and circumferential directions, shaping it into a spherical shape.
A rotating disk type rapid granulator is known in which the material falls through the air from around the disk, is cooled during that time, and is further dropped into water to cool and solidify.
なお、回転円盤による溶融物質の急速造粒装置の先行技
術としては、特公昭52−30149号公報がある。Note that Japanese Patent Publication No. 52-30149 is a prior art of a rapid granulation device for molten material using a rotating disk.
ところで、従来のこの型の造粒装置では、溶融体は溶融
炉の溶融体排出口より一旦とりべに取り。By the way, in this type of conventional granulation device, the molten material is once taken into a ladle from the molten material outlet of the melting furnace.
別の位置に設置された造粒装置の円盤上に供給して造粒
するようにされており、溶融体排出口も回転円盤も大気
中に露出させて設けられていた。したがって、溶融体と
ともに排出される溶融炉内の熱ガス及び排出口より炉内
に逆流する常温の空気により熱効率が低下する欠点があ
った。又、回転円板は平板として形成され、遠心力によ
り抛出される造粒体は水平方向に投出され、温度の低い
大気により急速に冷却されて凝固するので、強度が低下
する欠点があった。The melt was supplied onto a disc of a granulating device installed at a separate location for granulation, and both the melt outlet and the rotating disc were exposed to the atmosphere. Therefore, there is a drawback that thermal efficiency is reduced due to the hot gas inside the melting furnace that is discharged together with the melt and the room temperature air that flows back into the furnace from the exhaust port. In addition, the rotating disk is formed as a flat plate, and the granules ejected by centrifugal force are thrown out in a horizontal direction and are rapidly cooled and solidified by the low-temperature atmosphere, which has the disadvantage of decreasing strength. Ta.
が 決しようとする課
本発明は、従来の汚泥溶融体の造粒処理方法及び装置の
上述の実状にかんがみ、熱効率が良く、かつ強度の大き
い汚泥溶融物造粒体を得ることのできる汚泥溶融体の造
粒処理方法及び装置を提供することを課題とする。In view of the above-mentioned actual conditions of the conventional sludge melt granulation method and apparatus, the present invention provides a sludge melt that can obtain sludge melt granules with good thermal efficiency and high strength. An object of the present invention is to provide a granulation processing method and apparatus.
のための
上記の課題を解決させるため1本発明の方法は熱風溶融
炉により溶融された汚泥溶融体を水平回転円盤上面中心
に落下させ小球状に造粒し、該円盤の周囲より空中に抛
出して冷却し水中に落下させて固化して回収する汚泥溶
融体の造粒処理方法において。In order to solve the above-mentioned problems, the method of the present invention is to drop molten sludge melted in a hot-air melting furnace onto the center of the upper surface of a horizontal rotating disk, granulate it into small spheres, and throw it into the air from the periphery of the disk. In a method for granulating molten sludge, which is taken out, cooled, dropped into water, solidified, and recovered.
(a)上記溶融炉の溶融体排出口と上記回転円盤とを該
回転円盤の下方に水面を有する貯水部の水により造粒体
の通過、取出しを許容し、気密に水封した槽内に設け高
温雰囲気を形成する工程、
(b)溶融炉の溶融体排出口より排出された汚泥溶融体
を水平回転円盤の上面中心に直接落下させる工程、
(c)回転円盤上で形成された小球状造粒体を円盤周囲
より半径方向に斜上方に抛出して高温雰囲気内を時間を
掛けて水面に落下させる工程、
(d)水面に落下した造粒体を水中で固化させ水底に集
め、水封部を経て槽外に取出す工程。(a) The melt outlet of the melting furnace and the rotating disk are placed in an airtight water-sealed tank that allows the granules to pass through and be taken out by water in a water storage section with a water surface below the rotating disk. (b) A step in which the sludge melt discharged from the melt outlet of the melting furnace is directly dropped onto the center of the upper surface of the horizontal rotating disk. (c) A small spherical shape formed on the rotating disk. A process in which the granules are ejected diagonally upward in the radial direction from the circumference of the disk and fall to the water surface over time in a high-temperature atmosphere; (d) The granules that have fallen to the water surface are solidified in water and collected at the bottom of the water; The process of taking the water out of the tank through the water seal section.
を有することを特徴とする。It is characterized by having the following.
又、この方法を実施するための本発明の装置は。Also, there is an apparatus of the present invention for carrying out this method.
熱風溶融炉により溶融された汚泥溶融体を水平回転円盤
上面中心に落下させて小球状に造粒し。The sludge melted in the hot air melting furnace is dropped onto the center of the upper surface of a horizontally rotating disk and granulated into small spheres.
該円盤の周囲より空中に抛出して冷却し水中に落下させ
て固化し回収する汚泥溶融体の造粒処理装置において、
上記の熱風溶融炉の汚泥溶融体排出口は上記回転円盤上
面中心の直上に設けられ。In a granulation treatment device for sludge melt that is ejected into the air from the periphery of the disk, cooled, and dropped into water to solidify and recover, the sludge melt discharge port of the hot air melting furnace is located at the center of the top surface of the rotating disk. located directly above.
上記の熱風溶融炉の汚泥溶融体排出口及び上記回転円盤
を内蔵し、該円盤より下位に水面を有する貯水部と、該
貯水部の底部より上方に延び槽外で上記水面より高い位
置に達する造粒体取出管を有する造粒槽。A water storage section that incorporates the sludge melt discharge port of the hot air melting furnace and the above rotating disk and has a water surface below the disk, and extends upward from the bottom of the water storage section and reaches a position higher than the water surface outside the tank. A granulation tank with a granule removal pipe.
上記の造粒体取出管内に設けられ、造粒槽の貯水部底部
より造粒体を搬送する搬送手段。A conveying means is provided in the granule removal pipe and conveys the granules from the bottom of the water storage part of the granulation tank.
上記回転円盤の周囲に設けられ、半径方向に外方へ斜上
方に向う如く傾斜した部分
を有することを特徴とする。It is characterized in that it is provided around the rotating disk and has a portion that is inclined radially outward and obliquely upward.
作−朋
本発明による汚泥溶融体の造粒処理装置は、上記の如く
構成され、この装置を使用して、上記の方法によって造
粒処理が行なわれるので、溶融炉の溶融体排出口から排
出される溶融体及びこれに伴なわれて排出される熱ガス
は、造粒体取出し部が水封され気密に構成された造粒槽
中に排出され。The apparatus for granulating molten sludge according to the present invention is constructed as described above, and the apparatus is used to carry out granulation according to the method described above. The melt produced and the hot gas discharged along with the melt are discharged into a granulation tank whose granulation take-out portion is sealed with water and airtight.
造粒槽内の温度を昇温させ、高温に保持することができ
る。したがって、溶融体排出口より炉内に逆流する気体
は高温であり、炉内熱ガス温度を低下させることは少な
くて済む。The temperature inside the granulation tank can be raised and maintained at a high temperature. Therefore, the gas flowing back into the furnace from the melt outlet has a high temperature, and there is little need to lower the hot gas temperature in the furnace.
溶融体排出口より直接円盤上面中心に落下した汚泥溶融
体は微小な球状体に造粒され、円盤の周囲部より気体中
に抛出される時、円盤周囲の傾斜部によって斜上方に抛
り出され、抛物線を画いて。The sludge melt that falls directly to the center of the upper surface of the disk from the melt outlet is granulated into minute spheres, and when ejected into the gas from the periphery of the disk, it is thrown diagonally upward by the slope around the disk. He was brought out and drew a line.
造粒槽下部の貯水部の水面に落下する。したがって、気
体中の滞留時間が長くなり、又その雰囲気は高温に保持
されているので、造粒体は長時間の間に徐冷され緻密な
高強度の造粒体が得られる。It falls onto the water surface of the water storage section at the bottom of the granulation tank. Therefore, the residence time in the gas becomes longer, and the atmosphere is maintained at a high temperature, so that the granules are slowly cooled over a long period of time, resulting in dense, high-strength granules.
貯水部に落下した造粒体は槽底に集められ、搬送手段に
より、水面より上方迄延設された水封機能を有する取出
し管を搬送されて造粒槽外に取出される。The granules that have fallen into the water storage section are collected at the bottom of the tank, and are taken out of the granulation tank by a transporting means through a take-out pipe that extends above the water surface and has a water-sealing function.
スJ1匠
以下に本発明の方法を実施するための本発明の装置の実
施例を図面に基づいて詳細に説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS Examples of the apparatus of the present invention for carrying out the method of the present invention will be described in detail below based on the drawings.
第1図は、熱風溶融炉より排出される汚泥溶融体を、回
転円盤急速造粒機で微小球状体に造粒し、その造粒体を
着色して着色ビーズを製造する連続溶融・造粒・着色処
理装置に本発明を適用した実施例の全体構成を示す図で
ある。Figure 1 shows continuous melting and granulation in which molten sludge discharged from a hot-air melting furnace is granulated into microspheres using a rotating disk rapid granulator, and the granules are colored to produce colored beads. - It is a diagram showing the overall configuration of an embodiment in which the present invention is applied to a coloring processing device.
この装置は、大別して右側の造粒処理部1と、これから
回収された造粒体を乾燥し、着色する左側の着色処理部
2とより構成される。This apparatus is roughly divided into a granulation processing section 1 on the right side and a coloring processing section 2 on the left side for drying and coloring the granules collected from the granulation processing section 1.
造粒処理部1は、下部に貯水部3を有し、その底部から
貯水部3の水面より高い位置迄延設された造粒体取出し
管4が接続された気密構造の造粒槽5と、その内部に貯
水部3の水面より上方に設けられh水平回転円盤6.造
粒槽の底板を貫通するその軸7を支持する軸支部8.こ
の軸を回転駆動するモータ9、モータ9の駆動力を軸7
に伝達するベルト10より成る急速造粒機11より成る
。The granulation processing section 1 has a water storage section 3 at its lower part, and a granulation tank 5 having an airtight structure to which a granule take-out pipe 4 extending from the bottom to a position higher than the water surface of the water storage section 3 is connected. , provided inside thereof above the water surface of the water storage section 3, h horizontal rotating disk 6. A shaft support 8 for supporting the shaft 7 passing through the bottom plate of the granulation tank. A motor 9 rotates this shaft, and the driving force of the motor 9 is transferred to the shaft 7.
It consists of a rapid granulator 11 consisting of a belt 10 that transmits to the granulator.
回転円盤6の周辺部は半径方向外方に向って上方に傾斜
する傾斜面6aが全周に亘って設けられている。又、回
転円盤の内部には、中心から放射状に複数本の冷却水通
路6bが設けられ、軸7の下端で冷却水ポンプに接続さ
れ、軸7内に軸方向に設けられた冷却水通路7aの上端
に接続されており、円盤の外周部傾斜部の下面に開いて
いる。A peripheral portion of the rotating disk 6 is provided with a sloped surface 6a that slopes upwardly toward the outside in the radial direction over the entire circumference. Also, inside the rotating disk, a plurality of cooling water passages 6b are provided radially from the center, and a cooling water passage 7a is connected to a cooling water pump at the lower end of the shaft 7 and provided in the axial direction within the shaft 7. It is connected to the upper end and opens on the lower surface of the inclined outer peripheral part of the disk.
造粒槽5の頂板の中央部には1例えば、旋回流式部分溶
融炉などの熱風溶融炉12の底部が気密に接続されてお
り、急速造粒機11の回転円盤6の中心の真上に溶融炉
12の溶融体排出口13が位置している。For example, the bottom of a hot air melting furnace 12 such as a swirl flow partial melting furnace is airtightly connected to the center of the top plate of the granulation tank 5, and is directly above the center of the rotating disk 6 of the rapid granulation machine 11. The melt outlet 13 of the melting furnace 12 is located at.
造粒槽5の底板は、全体として図において右端から左端
に向って低くなるように傾斜しており。The bottom plate of the granulation tank 5 is inclined as a whole to become lower from the right end to the left end in the figure.
造粒機の回転円盤6の外周から貯水部3の水中に落下し
た造粒体は左端の最低下に集まる。The granules that have fallen from the outer periphery of the rotating disk 6 of the granulator into the water in the water storage section 3 gather at the bottom of the left end.
この部分に造粒槽外方斜上方に向って造粒体取出し管4
が設けられ、その内部には造粒体搬送手段としてのスク
リューコンベア14が設けられている、造粒体取出し管
4の上側開口下端は、貯水部3の液面より上位にあるの
で、造粒体を取出すことはできるが、造粒槽の気密を保
持することができ、水封機能を達成することができる。A granule take-out pipe 4 is installed in this part toward the outside of the granulation tank and diagonally upward.
The lower end of the upper opening of the granule take-out pipe 4, in which a screw conveyor 14 as a granule conveying means is provided, is located above the liquid level of the water storage section 3, so that the granules are Although the body can be taken out, the granulation tank can be kept airtight and a water-sealing function can be achieved.
次に着色処理部2の構成について説明する。Next, the configuration of the coloring processing section 2 will be explained.
造粒処理部2の造粒体取出し管4より排出された水で濡
れた造粒体を受入れて乾燥するための乾燥室21が造粒
体取出し管の出口の直下に設けられている。乾燥室内に
はコンベア22が設けられ、その下部には溶融炉12の
排ガス導入管23が接続されている。コンベア22の端
部の下部の乾燥室21の底部から造粒体導管24が着色
処理部の主要な装置であるコーティング装置25の上部
にあるホッパ26に延びており、ホッパ26の底部には
、ホッパ内に受入れた乾燥した造粒体をコーティング装
置に定量ずつ供給するフィーダ27が設けられている。A drying chamber 21 for receiving and drying the water-wet granules discharged from the granule take-out pipe 4 of the granulation processing section 2 is provided directly below the outlet of the granule take-out pipe. A conveyor 22 is provided in the drying chamber, and an exhaust gas introduction pipe 23 of the melting furnace 12 is connected to the lower part of the conveyor 22. From the bottom of the drying chamber 21 at the bottom of the end of the conveyor 22, a granule conduit 24 extends to a hopper 26 at the top of a coating device 25, which is the main device of the coloring section. A feeder 27 is provided to feed the dry granules received in the hopper into the coating device in fixed quantities.
コーティング装置25は直立円筒形の着色槽28の底部
に回転円盤29が設けられ、その外周部上方にはフィー
ダ27からの供給管3oと、これと異る位置に着色剤を
噴射するスプレィノズル31とが着色剤供給管32の下
端に取付けて設けられている0回転円盤29の下部の槽
内空間には、溶融炉12の排ガスを導入する排ガス導入
管33が接続されている0着色槽28の側壁の回転円盤
29の上面に下縁が概ね一致する位置には製品取出し用
開口34が設けられ、底面にはドレン等の排出口35が
設けられている。The coating device 25 includes a rotary disk 29 at the bottom of an upright cylindrical coloring tank 28, and above the outer periphery thereof is a supply pipe 3o from a feeder 27 and a spray nozzle 31 for spraying coloring agent at a different position. A zero-coloring tank 28 is connected to an exhaust gas introduction pipe 33 for introducing exhaust gas from the melting furnace 12 into the tank space below the zero-rotation disc 29 which is attached to the lower end of the colorant supply pipe 32. A product removal opening 34 is provided on the side wall at a position where the lower edge approximately coincides with the top surface of the rotating disk 29, and an outlet 35 for a drain or the like is provided on the bottom surface.
乾燥室21及びコーティング装置I25の着色槽28の
頂板には集塵機36に至る排ガス導管が接続され、集塵
された排ガスを排風機37を経て大気に放出する排ガス
管38が設けられている。An exhaust gas pipe leading to a dust collector 36 is connected to the top plate of the drying chamber 21 and the coloring tank 28 of the coating device I25, and an exhaust gas pipe 38 is provided for discharging the collected exhaust gas to the atmosphere through an exhaust fan 37.
以下に、この装置の作用を説明する。The operation of this device will be explained below.
熱風溶融炉12で溶融された汚泥溶融体は、溶融体排出
口13から造粒槽5内の急速造粒機11の回転円盤6の
中心に直接落下し、微小球状に造粒され、造粒体は回転
円盤6の周辺の傾斜部6aにより斜上方に提出され、時
間を掛けて造粒槽下部の貯水部に落下する。造粒槽5は
造粒体取出し管4が水封機能を有し、気密構造を有する
ため、溶融体及びこれに伴われて造粒槽内に排出される
溶融炉熱ガスにより造粒槽内雰囲気は高温に保たれ、造
粒体は長時間掛けて徐冷され一1Ik密な高強度のもの
が得られる1回転円盤6の周辺部6aの水平に対する傾
斜角度は30°〜60°程度とすれば良好な結果が得ら
れる。造粒槽5内の気体は高温に維持されているので、
溶融体排出口13から造粒槽内気体が溶融炉12に逆流
したとしても炉内熱ガスの温度を低下させることは少な
くて済む。The sludge melt melted in the hot air melting furnace 12 falls directly from the melt outlet 13 to the center of the rotating disk 6 of the rapid granulator 11 in the granulation tank 5, and is granulated into microspheres. The particles are pushed obliquely upward by the inclined portion 6a around the rotating disk 6, and fall into the water storage portion at the bottom of the granulation tank over time. Since the granulation tank 5 has a water-sealing function and an airtight structure, the granulation tank 5 is heated by the melt and the melting furnace hot gas discharged into the granulation tank. The atmosphere is kept at a high temperature, and the granules are slowly cooled over a long period of time to obtain a dense, high-strength product. You will get good results if you do this. Since the gas in the granulation tank 5 is maintained at a high temperature,
Even if the gas in the granulation tank flows back into the melting furnace 12 from the melt outlet 13, the temperature of the hot gas in the furnace is not reduced much.
・貯水部3の水に落下した造粒体は、造粒槽底面の傾斜
により最低部に集まり、そこから造粒槽外方に斜上方に
延びる造粒体取出し管4内を搬送手段14により水面上
運搬送された後乾燥室21内に落下する。- The granules that have fallen into the water in the water storage section 3 gather at the lowest part due to the slope of the bottom of the granulation tank, and from there are carried by the conveying means 14 through the granule take-out pipe 4 that extends obliquely upward to the outside of the granulation tank. After being transported on the water surface, it falls into the drying chamber 21.
乾燥室21内に落下した水に濡れた造粒体は、コンベア
22により搬送されつ5、溶融炉排ガス導入管23を経
て導入された溶融炉排ガスの熱により乾槽され、コンベ
ア22の端部で乾燥室21の底部に落下し、導管24を
経てホッパ26に集められる。ホッパ26内の造粒体は
フィーダ27により、所定量ずつコーティング装置25
内の回転円板29上に供給され1回転円板29の回転に
伴い、スプレィノズル31より噴射された着色剤がまん
べんなくコーティングされ1回転円盤29の下部に供給
される溶融炉12の排ガスにより加熱されることにより
乾燥され着色剤は造粒体上に定着され、排出口34より
製品として取出される。The water-wet granules that have fallen into the drying chamber 21 are conveyed by the conveyor 22 and are dried by the heat of the melting furnace exhaust gas introduced through the melting furnace exhaust gas introduction pipe 23. It falls to the bottom of the drying chamber 21 and is collected in a hopper 26 via a conduit 24. The granules in the hopper 26 are transferred to the coating device 25 in predetermined amounts by the feeder 27.
As the one-rotation disk 29 rotates, the colorant sprayed from the spray nozzle 31 is evenly coated and heated by the exhaust gas from the melting furnace 12 that is supplied to the lower part of the one-rotation disk 29. The colorant is dried and fixed on the granules, and is taken out as a product from the outlet 34.
なお着色槽28に導入される排ガスの温度は温度制御用
空気弁40により制御可能となっている。Note that the temperature of the exhaust gas introduced into the coloring tank 28 can be controlled by a temperature control air valve 40.
乾燥室21及びコーティング装置の槽28内で熱を利用
されて温度の低下した排ガスは集塵機36で除塵され、
排気ファン37により排気管38より大気に放出される
。The exhaust gas whose temperature has been lowered by using heat in the drying chamber 21 and the tank 28 of the coating device is removed by a dust collector 36.
The air is discharged into the atmosphere from an exhaust pipe 38 by an exhaust fan 37.
以上の如く、溶融炉の排ガスの有する熱は乾燥室21に
おける濡れた造粒体の乾燥及びコーティング装置25に
おける着色剤の乾燥定着に有効に利用されて排出される
。As described above, the heat contained in the exhaust gas of the melting furnace is effectively utilized for drying the wet granules in the drying chamber 21 and for drying and fixing the colorant in the coating device 25, and is then discharged.
造粒処理部の造粒槽が気密に構成され、溶融炉の溶融体
排出口がその内部で回転円盤直上に開口することによっ
て得られる熱損失の減少と上記の排ガスの熱の有効利用
とが相俟って熱効率が著しく向上する。The granulation tank in the granulation processing section is configured to be airtight, and the molten material discharge port of the melting furnace opens directly above the rotating disk, thereby reducing heat loss and effectively utilizing the heat of the exhaust gas. Together, the thermal efficiency is significantly improved.
又、汚泥溶融体を着色小球状粒状体としたことにより、
これをバインダにより結合して美しい壁材料、鋪道の敷
石等に利用することができ、付加価値を増大させること
ができる。In addition, by making the sludge melt into colored small spherical particles,
This can be combined with a binder and used for beautiful wall materials, paving stones for roads, etc., increasing added value.
羞−員
以上の如く、本発明によれば、汚泥溶融体より、強度の
大きい微小球状造粒体を熱効率良く生産することができ
、汚泥の処分量の減容化、再資源化に効果を得ることが
できる。As described above, according to the present invention, it is possible to produce microspherical granules with higher strength than molten sludge with high thermal efficiency, which is effective in reducing the volume of sludge to be disposed of and recycling. Obtainable.
第1図は本発明を汚泥の連続溶融・造粒・着色処理装置
に適用した実施例の全体構成を示す図式%式%
4・・・・・・造粒体取出し管(水封部)5・・・・・
・造粒槽
6・・・・・・回転円盤
6a・・・・・・傾斜部
11・・・・・・急速造粒機
12・・・・・・熱風溶融炉
13・・・・・・溶融体排出口
14・・・・・・スクリューコンベア(造粒体搬送手段
)21・・・・・・乾燥室
23.33・・・・・・溶融炉排ガス導入管25・・・
・・・コーティング装置
26・・・・・・ホッパ
27・・・・・・フィーダ
28・・・・・・着色槽
29・・・・・・回転円盤
30・・・・・・造粒体供給管
31・・・・・・スプレィノズル
32・・・・・・着色剤供給管
34・・・・・・製品取出し口
36・・・・・・集塵機
38・・・・・・排ガス管Figure 1 is a diagram showing the overall configuration of an embodiment in which the present invention is applied to a sludge continuous melting, granulation, and coloring treatment device.・・・・・・
- Granulation tank 6... Rotating disk 6a... Inclined section 11... Rapid granulator 12... Hot air melting furnace 13... Melt discharge port 14...Screw conveyor (granule conveyance means) 21...Drying chamber 23.33...Melting furnace exhaust gas introduction pipe 25...
... Coating device 26 ... Hopper 27 ... Feeder 28 ... Coloring tank 29 ... Rotating disk 30 ... Granule supply Pipe 31... Spray nozzle 32... Colorant supply pipe 34... Product outlet 36... Dust collector 38... Exhaust gas pipe
Claims (2)
転円盤上面中心に落下させ小球状に造粒し、該円盤の周
囲より空中に抛出して冷却し水中に落下させて固化して
回収する汚泥溶融体の造粒処理方法において、 (a)上記溶融炉の溶融体排出口と上記回転円盤とを該
回転円盤の下方に水面を有す る貯水部の水により造粒体の通過、取出 しを許容し、気密に水封した槽内に設け 高温雰囲気を形成する工程、 (b)溶融炉の溶融体排出口より排出された汚泥溶融体
を水平回転円盤の上面中心に 直接落下させる工程、 (c)回転円盤上で形成された小球状造粒体を円盤周囲
より半径方向に斜上方に抛出 して高温雰囲気内を時間を掛けて水面に 落下させる工程、 (d)水面に落下した造粒体を水中で固化させ水底に集
め、水封部を経て槽外に取出 す工程、 を有することを特徴とする汚泥溶融体の造粒処理方法。(1) Molten sludge melted in a hot air melting furnace is dropped onto the center of the upper surface of a horizontally rotating disk, granulated into small spheres, ejected from the periphery of the disk into the air, cooled, and dropped into water to solidify. In a method for granulating molten sludge to be recovered, (a) the molten material discharge port of the melting furnace and the rotating disk are connected by water in a water storage section having a water surface below the rotating disk to allow the granulated material to pass through and be taken out; (b) A step in which the sludge melt discharged from the melt outlet of the melting furnace is directly dropped onto the center of the upper surface of the horizontal rotating disk. (c) A step in which the small spherical granules formed on a rotating disk are ejected obliquely upward from the circumference of the disk in the radial direction and fall onto the water surface over time in a high-temperature atmosphere; (d) When the particles fall onto the water surface. A method for granulating molten sludge, comprising the steps of solidifying the granules in water, collecting them at the bottom of the water, and taking them out of the tank through a water seal.
転円盤上面中心に落下させて小球状に造粒し、該円盤の
周囲より空中に抛出して冷却し水中に落下させて固化し
回収する汚泥溶融体の造粒処理装置において、 上記の熱風溶融炉の汚泥溶融体排出口は上 記回転円盤上面中心の直上に設けられ、 上記の熱風溶融炉の汚泥溶融体排出口及び 上記回転円盤を内蔵し、該円盤より下位に水面を有する
貯水部と、該貯水部の底部より上方に延び槽外で上記水
面より高い位置に達する造粒体取出管を有する造粒槽、 上記の造粒体取出管内に設けられ、造粒槽 の貯水部底部より造粒体を搬送する搬送手段、上記回転
円盤の周囲に設けられ、半径方向 に外方へ斜上方に向う如く傾斜した部分 を有することを特徴とする汚泥溶融体造粒処理装置。(2) The molten sludge melted in the hot air melting furnace is dropped onto the center of the upper surface of a horizontally rotating disk, granulated into small spheres, ejected from the periphery of the disk into the air, cooled, and dropped into water to solidify. In the granulation treatment apparatus for sludge melt to be recovered, the sludge melt outlet of the hot air melting furnace is provided directly above the center of the upper surface of the rotating disk, and the sludge melt outlet of the hot air melting furnace and the rotating disk are a granulation tank having a built-in water storage part having a water surface below the disk, and a granulation take-out pipe extending upward from the bottom of the water storage part and reaching a position higher than the water surface outside the tank; A conveyance means is provided in the body extraction pipe and conveys the granules from the bottom of the water storage part of the granulation tank, and is provided around the rotating disk and has a portion that slopes outward in the radial direction and obliquely upward. A sludge melt granulation processing device characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8113490A JPH0655271B2 (en) | 1990-03-30 | 1990-03-30 | Method and apparatus for granulating sludge melt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8113490A JPH0655271B2 (en) | 1990-03-30 | 1990-03-30 | Method and apparatus for granulating sludge melt |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03284341A true JPH03284341A (en) | 1991-12-16 |
| JPH0655271B2 JPH0655271B2 (en) | 1994-07-27 |
Family
ID=13737932
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8113490A Expired - Lifetime JPH0655271B2 (en) | 1990-03-30 | 1990-03-30 | Method and apparatus for granulating sludge melt |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0655271B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109364820A (en) * | 2018-11-30 | 2019-02-22 | 北京天极视讯科技发展有限公司 | A method of utilizing biogas residue and biogas liquid slurry-spraying pelletizing |
-
1990
- 1990-03-30 JP JP8113490A patent/JPH0655271B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109364820A (en) * | 2018-11-30 | 2019-02-22 | 北京天极视讯科技发展有限公司 | A method of utilizing biogas residue and biogas liquid slurry-spraying pelletizing |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0655271B2 (en) | 1994-07-27 |
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