JPH06218397A - Method and device for drying and firing sludge - Google Patents
Method and device for drying and firing sludgeInfo
- Publication number
- JPH06218397A JPH06218397A JP5029593A JP2959393A JPH06218397A JP H06218397 A JPH06218397 A JP H06218397A JP 5029593 A JP5029593 A JP 5029593A JP 2959393 A JP2959393 A JP 2959393A JP H06218397 A JPH06218397 A JP H06218397A
- Authority
- JP
- Japan
- Prior art keywords
- cake
- sludge
- oil tank
- oil
- drying
- 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
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は紙パルプ工場、食品製造
工場などの各種製造工場やホテル、給食施設、レストラ
ン等の厨房関係施設および下水、し尿処理場等より出さ
れた排水を凝集沈殿、浮上分離、生物学的な処理等の各
種処理をして汚泥(スラッジ)を得た後、さらに該汚泥
を脱水機により脱水して得られたケーキを主対象とした
汚泥の乾燥、焼却方法及びその装置に関する。[Field of Industrial Application] The present invention coagulates and sediments wastewater discharged from various manufacturing factories such as a pulp and paper factory, a food manufacturing factory and kitchen-related facilities such as hotels, lunch facilities and restaurants, and sewage and night soil treatment plants. Floating separation, biological treatment, and other various treatments to obtain sludge (sludge), and then dehydration of the sludge with a dehydrator, and a method for drying and incinerating sludge mainly for cakes obtained Regarding the device.
【0002】[0002]
【従来の技術】従来のこの種の有機汚泥処理方法とし
て、可燃性の油を水の沸騰点以上の温度に加温し、該油
中にスラッジ状の有機汚泥を投入して脱水固化した後、
固化汚泥を、付着した可燃性の油と共に燃焼させる方法
がある(特開昭50−139574号公報参照)。2. Description of the Related Art As a conventional method for treating organic sludge of this type, a flammable oil is heated to a temperature higher than the boiling point of water, and sludge-like organic sludge is added to the oil for dehydration and solidification. ,
There is a method of burning the solidified sludge together with the attached flammable oil (see Japanese Patent Application Laid-Open No. 50-139574).
【0003】[0003]
【発明が解決しようとする課題】しかし上記従来の有機
汚泥処理方法は、スラッジ状の有機汚泥をさらに脱水機
により脱水することなく直接、含有水分の多い該スラッ
ジ状の有機汚泥を油中に投入して乾燥させるために、乾
燥効率が悪く、実用的でなかった。また、スラッジ(汚
泥)を脱水機により脱水して得たケーキを乾燥すること
なく直接、焼却炉に投入して焼却した場合、ケーキ中の
含有水分が多すぎて燃料を多量に消費し、燃焼効率が悪
い。However, in the above-mentioned conventional organic sludge treatment method, the sludge-shaped organic sludge having a high water content is directly added to oil without further dehydration of the sludge-shaped organic sludge by a dehydrator. Therefore, it was not practical because the drying efficiency was poor. Also, if the cake obtained by dehydrating sludge (sludge) with a dehydrator is directly put into an incinerator without being dried, the water content in the cake is too high, and a large amount of fuel is consumed. ineffective.
【0004】一般に、脱水機の型式としては種々のもの
があるが、ベルトプレスやフィルタープレスを使用して
得たケーキの厚みは5〜20mmと厚い。従って、この
ような厚みのケーキを加温した油槽中に投入したとして
も、ケーキの中心部分がよく乾燥せず、乾燥に時間がか
かり乾燥効率が悪い。また、遠心脱水機やスクリュープ
レスを使用して得た丸くて大きいダンゴ状のケーキを油
槽に投入してもこれまた中側が乾燥しないという難点が
ある。さらに、脱水機で脱水されたケーキをケーキ貯留
槽に保管した場合、ケーキは貯留槽内でその自重により
圧密されて大きな塊となりやはり乾燥しにくいという欠
点があった。Generally, there are various types of dehydrators, but the thickness of a cake obtained by using a belt press or a filter press is as thick as 5 to 20 mm. Therefore, even if a cake having such a thickness is put into a heated oil tank, the central portion of the cake does not dry well, and it takes a long time to dry and the drying efficiency is poor. Further, even if a round and large dango-shaped cake obtained by using a centrifugal dehydrator or a screw press is put into an oil tank, the inside of the cake does not dry. Further, when the cake dehydrated by the dehydrator is stored in the cake storage tank, the cake is compacted by its own weight in the storage tank to form a large lump, which is also difficult to dry.
【0005】本発明は上記の点に鑑みてなされたもの
で、その目的とするところはケーキを薄片状に形成して
どの箇所も均一で短時間に効率よく乾燥し、かつ乾燥後
のケーキを少ない燃料で効率よく焼却できるようにした
汚泥の乾燥、焼却方法及びその装置を提供することにあ
る。また、脱水機より得られたケーキが厚みの厚いケー
キであったりあるいは大きなダンゴ状の塊であった場合
やまたは貯留槽内でケーキがその自重により圧密されて
大きな塊となっている場合でも、ケーキの塊をほぐし、
ケーキを平均に送り出すようにしながら所望する薄片状
に簡易な構造にて容易に得られるようにするとともにケ
ーキを油槽中で移動させて熱的接触を強制的に行い迅速
かつ連続的な乾燥を可能ならしめた汚泥の乾燥、焼却装
置を提供することにある。The present invention has been made in view of the above points, and an object of the present invention is to form a cake into a flaky form, to uniformly and efficiently dry any part in a short time, and to provide a cake after drying. It is an object of the present invention to provide a method and an apparatus for drying and incinerating sludge that can be efficiently incinerated with less fuel. Also, even if the cake obtained from the dehydrator is a thick cake or a large dango-shaped mass, or even if the cake is compacted by its own weight into a large mass in the storage tank, Loosen the cake mass,
Allows the cake to be sent out to the average while easily obtaining the desired flaky shape with a simple structure, and moves the cake in an oil tank to force thermal contact for quick and continuous drying. It is to provide a drying and incineration device for the sludge that has been soaked.
【0006】[0006]
【課題を解決するための手段】本発明に係る汚泥の乾燥
方法は、汚泥を脱水して得たケーキを水分蒸発可能な薄
片状に形成し、次いで該薄片状のケーキを加温された油
槽中で搬送しながら乾燥するようにしたものである。ま
た本発明に係る汚泥の乾燥装置は、汚泥を脱水してケー
キとする脱水機と、該ケーキを所定の厚みの薄片状に形
成するケーキ厚み成形機と、油中で薄片状のケーキを搬
送させるスクレーパーを備えた油槽とからなるものであ
る。さらに本発明に係る汚泥の乾燥、焼却方法は、汚泥
を脱水して含有水分90%以下のケーキを得た後、該ケ
ーキを水分蒸発可能な薄片状に形成し、次いで該薄片状
のケーキを加温された油槽中で搬送しながら乾燥し、該
乾燥したケーキを焼却するようにしたものである。ま
た、本発明に係る汚泥の乾燥、焼却装置は、汚泥を脱水
してケーキとする脱水機と、該ケーキを所定の厚みの薄
片状に形成するケーキ厚み成形機と、油中で薄片状のケ
ーキを搬送させるスクレーパーを備えた油槽と、該油槽
で乾燥したケーキを焼却する焼却炉とからなるものであ
る。The method for drying sludge according to the present invention is a method in which a cake obtained by dehydrating sludge is formed into flakes capable of evaporating water, and then the flaky cake is heated in an oil tank. It is designed to be dried while being transported inside. Further, the sludge drying device according to the present invention includes a dehydrator that dehydrates sludge into a cake, a cake thickness molding machine that forms the cake into a flaky shape having a predetermined thickness, and conveys a flaky cake in oil. And an oil tank equipped with a scraper. Further, the method for drying and incinerating sludge according to the present invention is to dehydrate the sludge to obtain a cake having a water content of 90% or less, then form the cake into a water-evaporable flaky cake, and then form the flaky cake. The dried cake is dried while being conveyed in a heated oil tank, and the dried cake is incinerated. Further, the sludge drying and incineration apparatus according to the present invention, a dehydrator for dehydrating sludge into a cake, a cake thickness forming machine for forming the cake into a flaky shape having a predetermined thickness, and a flaky shape in oil. It comprises an oil tank equipped with a scraper for conveying the cake, and an incinerator for incinerating the cake dried in the oil tank.
【0007】さらに、本発明に係る汚泥の乾燥、焼却装
置は、汚泥を脱水してケーキとする脱水機と、該脱水機
で得られたケーキを貯留するケーキ貯留槽と、該貯留槽
のケーキをホッパーに移送するケーキ移送ポンプと、前
記ホッパー内のケーキの塊をほぐし、ケーキを平均に送
り出すならし羽根を内蔵したケーキ厚み成形機と、該成
形機で得られた薄片状のケーキを油中で搬送させるスク
レーパーを備えた油槽と、該油槽で乾燥したケーキを焼
却する焼却炉とからなるものである。さらにまた、ケー
キ厚み成形機は一対の内方向に回転するロールまたは押
出し用口金を備えている。Further, the sludge drying and incinerating apparatus according to the present invention comprises a dehydrator for dehydrating sludge into a cake, a cake storage tank for storing the cake obtained by the dehydrator, and a cake for the storage tank. To a hopper, and a cake thickness molding machine with a built-in leveling vane that loosens the cake mass in the hopper and sends the cake to the average, and a flaky cake obtained by the molding machine as an oil. It is composed of an oil tank equipped with a scraper to be conveyed inside, and an incinerator for incinerating the cake dried in the oil tank. Furthermore, the cake thickness molding machine is equipped with a pair of inwardly rotating rolls or extrusion die.
【0008】[0008]
【実施例】以下、本発明の実施例を図面に基いて説明す
る。図1は本発明の一実施例を示す汚泥の乾燥、焼却装
置の概略説明図である。1は汚泥脱水機、処理汚泥に応
じて加圧脱水、真空脱水、遠心脱水、ロール脱水あるい
はこれらの組合せのいずれの手段によってもよい。2は
汚泥脱水機1で得られたケーキKを次のケーキ貯留槽3
に移送するコンベアである。ケーキ貯留槽3を設けるこ
ととしたのは後述する油槽7との距離が離れていたり、
油槽7の周囲に十分な脱水機1等の設置スペースがない
場合等に一時的な貯留場所として好適である。またケー
キ貯留槽3を設置した場合は、ケーキKの貯留が可能と
なるため操業時間の調整が可能となる。しかし、ケーキ
貯留槽3を設けることなく汚泥脱水機1で得られたケー
キKを直接、後述するケーキ厚み成形機5のホッパー5
aに投入するようにしてもよい。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic explanatory view of a sludge drying and incinerating apparatus showing an embodiment of the present invention. 1 may be a sludge dewatering machine, or any of pressure dewatering, vacuum dewatering, centrifugal dewatering, roll dewatering, or a combination thereof depending on the treated sludge. 2 is the cake K obtained from the sludge dewatering machine 1 in the next cake storage tank 3
It is a conveyor to be transferred to. The cake storage tank 3 is provided because the distance to the oil tank 7 described later is long,
It is suitable as a temporary storage place when there is not enough space for installing the dehydrator 1 or the like around the oil tank 7. Further, when the cake storage tank 3 is installed, the cake K can be stored, so that the operation time can be adjusted. However, the cake K obtained by the sludge dewatering machine 1 is directly provided without providing the cake storage tank 3, and the hopper 5 of the cake thickness molding machine 5 described later is used.
You may make it throw into a.
【0009】4はケーキ貯留槽3内のケーキKをホッパ
ー5aに移送するケーキ移送ポンプで、パイプラインに
より行なう。5はホッパー5aに内蔵したならし羽根
で、ホッパー5a内のケーキKの塊をほぐし、該ケーキ
Kを平均に送り出すためのものである。ホッパー5aを
備えたケーキ厚み成形機5は該ホッパー5aの下部に一
対の内方向に回転するロール5bを備え、一対のロール
5b間の隙間を脱水されたケーキの含有水分率や性状等
に応じて適宜調整可能な構造とすることによって最適厚
みの薄片状に成形されるようになっている。例えば該ロ
ール5bから押出された薄片状のケーキKの厚みは0.
5mmから数mmに成形すると油槽での乾燥が効率よく
行なうことができる。さらに、ケーキKの排出スピード
を調整できるようにロール5bの回転速度を変更できる
ようにしている。本発明でいう薄片状とは、薄片に限ら
ず、シート状、短冊状、リボン状又はうどん状等の細帯
状等の各種形状が含まれ、要は油槽での乾燥がケーキの
内部まで均一に短時間に行なわれる形状であればよい。Reference numeral 4 is a cake transfer pump for transferring the cake K in the cake storage tank 3 to the hopper 5a, which is carried out by a pipeline. Reference numeral 5 denotes a leveling blade incorporated in the hopper 5a, which serves to loosen the cake K in the hopper 5a and send the cake K to the average. The cake thickness molding machine 5 equipped with a hopper 5a is equipped with a pair of inwardly rotating rolls 5b at the bottom of the hopper 5a, and the gap between the pair of rolls 5b is adjusted according to the moisture content and properties of the dehydrated cake. By adopting a structure that can be adjusted as appropriate, a thin piece having an optimum thickness is formed. For example, the thickness of the flaky cake K extruded from the roll 5b is 0.
Molding from 5 mm to several mm enables efficient drying in an oil tank. Further, the rotation speed of the roll 5b can be changed so that the discharge speed of the cake K can be adjusted. The thin piece shape in the present invention is not limited to a thin piece, and includes various shapes such as a sheet shape, a strip shape, a ribbon shape, or a strip shape such as a udon shape, and the point is that the drying in an oil tank is even to the inside of the cake. Any shape can be used as long as it is performed in a short time.
【0010】ケーキ厚み成形機5は図1では一対の内方
向に回転するロール5bを用いて行なうようにしたが必
ずしもこれに限定されるものではなく、図2に示すよう
に口金方式によりケーキKを薄片状に押出すようにして
もよい。すなわち、ケーキ移送ポンプ4により密閉され
たホッパー5a内に移送されたケーキKは該ホッパー5
aの下部に設けた口金5cから押出すようにしてもよ
い。この口金5cは最適厚みのケーキKが排出されるよ
うに交換または厚み調整可能となっている。また本例で
はホッパー5aを密閉型としケーキKをポンプにより圧
送するようにした場合について説明したが、この他に、
シリンダー方式(図示せず)等によりケーキKを薄片状
に押出すようにしてもよい。In FIG. 1, the cake thickness molding machine 5 is configured to use a pair of inwardly rotating rolls 5b, but the invention is not limited to this, and as shown in FIG. May be extruded in the form of flakes. That is, the cake K transferred into the hopper 5a sealed by the cake transfer pump 4 is
You may make it extrude from the base 5c provided in the lower part of a. The base 5c can be replaced or the thickness can be adjusted so that the cake K having the optimum thickness is discharged. In this example, the case where the hopper 5a is a closed type and the cake K is pumped is described.
The cake K may be extruded into a thin piece by a cylinder method (not shown) or the like.
【0011】ケーキ厚み成形機5の下方には側面船形ま
たは平面長方形等をした油槽7を設置する。油槽7の長
手方向外側両端にはエンドレスのチェーン9を駆動させ
るスプロケット8を設ける。エンドレスのチェーン9に
は所定間隔をおいて油槽7内の長手方向に沿って入口か
ら出口に向けて移動するスクレーパー10を取付け、油
槽7内に投入された薄片状のケーキKを該スクレーパー
10で順次、かき寄せながら出口側に移動させる。スク
レーパー10は油槽7内の油をなるべく移送中に波立て
ないようにするために油を通過させる孔(図示せず)を
多数穿設するか、またはスクレーパー10自体を金網状
に形成する。さらに該スクレーパー10はケーキKの浸
漬時間を変更できるようにチェーン9に噛み合うスプロ
ケット8の回転を変更して該スクレーパー10の移動す
る速度の調節ができるようにしている。Below the cake thickness forming machine 5, an oil tank 7 having a side surface ship shape or a plane rectangular shape is installed. Sprockets 8 for driving an endless chain 9 are provided at both outer ends in the longitudinal direction of the oil tank 7. Attached to the endless chain 9 is a scraper 10 that moves from the inlet to the outlet along the longitudinal direction in the oil tank 7 at a predetermined interval, and the flaky cake K charged in the oil tank 7 is attached by the scraper 10. Move to the exit side while scraping them one by one. The scraper 10 is provided with a large number of holes (not shown) through which the oil passes, in order to prevent the oil in the oil tank 7 from undulating during transfer, or the scraper 10 itself is formed in a wire mesh shape. Further, in the scraper 10, the rotation of the sprocket 8 meshing with the chain 9 is changed so that the immersion time of the cake K can be changed so that the moving speed of the scraper 10 can be adjusted.
【0012】また油槽7内に充填する油はコストの低減
化を図るために使用済みの食用油等の廃油が使用され
る。油槽7内の油は薄片状のケーキK中に含有する水分
が蒸発し得るような温度にガスバーナー、灯油の燃焼そ
の他の加熱手段により加温部6により加熱し、通常11
0℃から200℃位の温度に加熱するのがよい。油槽7
の上方には消火液スプレーノズル11を複数箇所に設置
し、油槽7中の油が自然発火した場合等の非常時に備え
て自動消火できる設備を備えている。油槽7内に投入さ
れた薄片状のケーキKは、加温された油の中をスクレー
パー10で順次、かき寄せられながら出口側に移動する
過程でケーキK中の水分が該加温された油によって蒸発
し乾燥する。すなわち、ケーキKを静止状態で加温され
た油に接触させるのではなく、該ケーキKを油中で移動
させて強制的に熱的接触を図るようにしているために、
より迅速に乾燥させることができる乾燥後のケーキK中
の水分は5%以下となり、乾燥効率がよい。薄片状のケ
ーキKは油槽7を通過後、スクレーパー10により順
次、搬送され、該スクレーパー10の周囲及び孔を通し
て油切りがある程度されて案内板11を介してフライ貯
槽12に貯留される。As the oil filled in the oil tank 7, waste oil such as used cooking oil is used in order to reduce the cost. The oil in the oil tank 7 is heated by the heating section 6 by a gas burner, kerosene combustion or other heating means to a temperature at which the water contained in the flaky cake K can be evaporated.
It is preferable to heat to a temperature of about 0 ° C to 200 ° C. Oil tank 7
A fire extinguishing liquid spray nozzle 11 is installed at a plurality of locations above the, and equipment for automatic extinguishing is provided in case of emergency such as when the oil in the oil tank 7 spontaneously ignites. The flaky cake K charged into the oil tank 7 is heated by the scraper 10 in the heated oil in order, and the water in the cake K is moved by the heated oil in the process of moving to the outlet side while being scraped. Evaporate and dry. That is, since the cake K is not brought into contact with the heated oil in a stationary state, the cake K is moved in the oil to forcibly make thermal contact.
The water content in the cake K after drying, which can be dried more quickly, is 5% or less, and the drying efficiency is good. After passing through the oil tank 7, the flaky cake K is successively conveyed by the scraper 10 and is drained to some extent through the periphery and holes of the scraper 10 and stored in the fry storage tank 12 via the guide plate 11.
【0013】フライ貯槽12に貯留された乾燥後のケー
キLはスクリューコンベア13で搬送されて焼却炉14
に投入される。焼却炉14に投入された乾燥後のケーキ
Lは該ケーキ自体に油を含んでおり、これが補助燃料と
なり、焼却炉14内の燃焼熱と相挨って一層効果的に燃
焼させることができ、水分が極めて少なく迅速に燃焼で
きる上に燃費効率がよい。The dried cake L stored in the fry storage tank 12 is conveyed by the screw conveyor 13 to the incinerator 14.
Be thrown into. The cake L after drying, which has been put into the incinerator 14, contains oil in the cake itself, and this serves as an auxiliary fuel, which can be combusted more effectively due to the combustion heat in the incinerator 14 and the dust. It has extremely low water content, can burn quickly, and has good fuel efficiency.
【0014】実施例1 汚泥脱水機1により脱水した含有水分85%のケーキK
をホッパー5aに投入し、ケーキ厚み成形機5のロール
5bの間隙を2mmに設定し、該ケーキ厚み成形機5の
ロール5bから押出された薄片状のケーキKを油槽7中
の温度180℃の油に浸漬し、スクレーパー10でケー
キKを油中で移動させながら3分間、乾燥した後のケー
キLの含有水分は5%であった。 実施例2 汚泥脱水機1により脱水した含有水分85%のケーキK
をホッパー5aに投入し、ケーキ厚み成形機5のロール
5bの間隙を1mmに設定し、該ケーキ厚み成形機5の
ロール5bから押出された薄片状のケーキKを油槽7中
の温度180℃の油に浸漬し、スクレーパー10でケー
キKを油中で移動させながら2分間、乾燥した後のケー
キLの含有水分は1%であった。Example 1 Cake K having a water content of 85% dehydrated by a sludge dewatering machine 1
Is charged into the hopper 5a, the gap between the rolls 5b of the cake thickness molding machine 5 is set to 2 mm, and the flaky cake K extruded from the rolls 5b of the cake thickness molding machine 5 is heated at a temperature of 180 ° C. in the oil tank 7. The water content of the cake L after being immersed in oil and dried by the scraper 10 for 3 minutes while moving the cake K in the oil was 5%. Example 2 Cake K having a water content of 85% dehydrated by the sludge dehydrator 1
Is charged into the hopper 5a, the gap between the rolls 5b of the cake thickness molding machine 5 is set to 1 mm, and the flaky cake K extruded from the rolls 5b of the cake thickness molding machine 5 is heated at a temperature of 180 ° C. in the oil tank 7. The water content of the cake L after being immersed in oil and dried for 2 minutes while moving the cake K in the oil with the scraper 10 was 1%.
【0015】比較例1 汚泥脱水機1により脱水した含有水分85%の厚み5m
mのケーキKをそのまま直接、油槽7中の温度180℃
の油に乾燥し、スクレーパー10でケーキKを油中で移
動させながら5分間、浸漬した後のケーキLの含有水分
は40%であり、ケーキの表面は乾燥するが中側は乾爆
しなかった。このため、焼却炉での焼却は焼却不良とな
った。Comparative Example 1 Dewatered by the sludge dewatering machine 1 and having a water content of 85% and a thickness of 5 m
m cake K directly as it is, the temperature in the oil tank 7 is 180 ° C.
The water content of Cake L is 40% after dipping for 5 minutes while moving Cake K in oil with scraper 10 while moving it in oil, and the surface of the cake is dry, but the inner side is not dry explosion. It was For this reason, incineration in an incinerator was incomplete.
【0016】[0016]
【発明の効果】本発明は上記の説明から判るように、汚
泥を脱水して得たケーキを水分蒸発可能な薄片状に形成
し、次いで該薄片状のケーキを加温された油槽中で搬送
しながら乾燥することとしたので、ケーキを薄い薄片状
に形成することとケーキを加温された油中で移動させて
強制的に熱的接触を図ることとが相俟ってケーキのどの
箇所も均一で短時間に効率よく乾燥させることができ
る。また、上記乾燥後のケーキは該ケーキ自体に油を含
んでおり、これが補助燃料となり、焼却炉内の燃焼熱と
相挨って一層効果的に燃焼させることができ、水分が極
めて少なく迅速に燃焼できる上に燃費効率がよく、廃棄
物の大幅な減量化ができる。さらに、脱水機より得られ
たケーキが厚みの厚いケーキであったり、あるいは大き
なダンゴ状の塊であった場合やまたは貯留槽内でケーキ
がその自重により圧密されて大きな塊となっている場合
でも、ケーキの塊をほぐし、ケーキを平均に送り出すよ
うにしながら所望する薄片状に簡易な構造にて容易に得
られる。As can be seen from the above description, the present invention forms a cake obtained by dehydrating sludge into a water-evaporable flaky cake, and then transports the flaky cake in a heated oil tank. However, since it was decided to dry it, it was not possible to form the cake into thin flakes and to move the cake in heated oil to forcibly make thermal contact. It is even and can be efficiently dried in a short time. In addition, the cake after drying contains oil in the cake itself, which serves as an auxiliary fuel, and can be burned more effectively in combination with the heat of combustion in the incinerator, resulting in a very small amount of water and quickness. In addition to being able to burn, it has good fuel efficiency and can significantly reduce waste. Furthermore, even if the cake obtained from the dehydrator is a thick cake, or a large dango-shaped cake, or even if the cake is compacted by its own weight into a large cake in the storage tank. The cake can be easily obtained in a desired flaky shape with a simple structure while loosening the cake mass and feeding the cake evenly.
【0017】さらにまた、本発明に係る汚泥の乾燥、焼
却装置は汚泥を脱水してケーキとする脱水機と、該ケー
キを所定の厚みの薄片状に形成するケーキ厚み成形機
と、油中で薄片状のケーキを搬送させるスクレーパーを
備えた油槽と、該油槽で乾燥したケーキを焼却する焼却
炉とからなる一連のシステムとして、自動運転が可能と
なる。また、ケーキ厚み成形機は、一対の内方向に回転
するロールまたは押出し用口金にてケーキを所望する薄
片状に簡単な構造にて容易に形成することができる。さ
らに、ケーキ厚み成形機のホッパー内にならし羽根を備
えているので、ホッパー内のケーキがダンゴ状にかたま
っていようともこの塊をほぐすことが でき、かつケー
キを厚み成形箇所側に平均に送り出すことができる。Furthermore, the sludge drying and incineration apparatus according to the present invention comprises a dehydrator for dehydrating sludge into a cake, a cake thickness forming machine for forming the cake into a flaky shape having a predetermined thickness, and an in-oil medium. Automatic operation is possible as a series of systems consisting of an oil tank equipped with a scraper for conveying flaky cakes and an incinerator for incinerating cakes dried in the oil tank. Further, the cake thickness molding machine can easily form the cake into a desired flaky shape with a simple structure using a pair of inwardly rotating rolls or an extrusion die. Furthermore, since the hopper of the cake thickness molding machine is equipped with leveling blades, this cake can be loosened even if the cake in the hopper is clumped like a dango, and the cake is sent to the thickness molding location side on average. be able to.
【図1】本発明の一実施例を示す汚泥の乾燥、焼却装置
の概略説明図である。FIG. 1 is a schematic explanatory view of a sludge drying and incineration apparatus showing an embodiment of the present invention.
【図2】ケ−キ厚み成形機の他の実施例を示す概略説明
図である。FIG. 2 is a schematic explanatory view showing another embodiment of the cake thickness molding machine.
1 汚泥脱水機 3 ケ−キ貯留槽 4 ケ−キ移送ポンプ 5 ケ−キ厚み成形機 5a ホッパ− 5b ロ−ル 5c 口金 7 油槽 10 スクレ−パ− 14 焼却炉 K ケ−キ L 乾燥ケ−キ 1 Sludge Dewatering Machine 3 Key Storage Tank 4 Key Transfer Pump 5 Key Thickness Forming Machine 5a Hopper 5b Roll 5c Clasp 7 Oil Tank 10 Scraper 14 Incinerator K Key L Dry Case Ki
───────────────────────────────────────────────────── フロントページの続き (72)発明者 今 尾 邦 明 東京都中央区日本橋二丁目三番十八号 中 和機工株式会社内 (72)発明者 湯 山 大 和 東京都中央区日本橋二丁目三番十八号 中 和機工株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kuniaki Imao 2-3-8 Nihonbashi, Chuo-ku, Tokyo Nakawa Kiko Co., Ltd. (72) Inventor Daiwa Yuyama 2-chome, Nihonbashi, Chuo-ku, Tokyo No. 3-18 Chuwa Kiko Co., Ltd.
Claims (6)
能な薄片状の厚みに形成し、次いで該薄片状のケーキを
加温された油槽中で搬送しながら乾燥することを特徴と
する汚泥の乾燥方法。1. A cake obtained by dehydrating sludge is formed into a flaky thickness capable of evaporating water, and then the flaky cake is dried while being transported in a heated oil tank. Sludge drying method.
該ケーキを所定の厚みの薄片状に形成するケーキ厚み成
形機と、油中で薄片状のケーキを搬送させるスクレーパ
ーを備えた油槽とからなることを特徴とする汚泥の乾燥
装置。2. A dehydrator for dehydrating sludge into a cake,
A sludge drying device comprising a cake thickness forming machine for forming the cake into a flaky shape having a predetermined thickness and an oil tank provided with a scraper for transporting the flaky cake in oil.
ーキを得た後、該ケーキを水分蒸発可能な薄片状に形成
し、次いで該薄片状のケーキを加温された油槽中で搬送
しながら乾燥し、該乾燥したケーキを焼却することを特
徴とする汚泥の乾燥、焼却方法。3. The sludge is dehydrated to obtain a cake having a water content of 90% or less, the cake is formed into a water-evaporable flaky piece, and the flaky cake is then conveyed in a heated oil tank. A method for drying and incinerating sludge, which comprises drying while incinerating the dried cake.
該ケーキを所定の厚みの薄片状に形成するケーキ厚み成
形機と、油中で薄片状のケーキを搬送させるスクレーパ
ーを備えた油槽と、該油槽で乾燥したケーキを焼却する
焼却炉とからなることを特徴とする汚泥の乾燥、焼却装
置。4. A dehydrator for dehydrating sludge into a cake,
A cake thickness forming machine for forming the cake into a flake shape having a predetermined thickness, an oil tank equipped with a scraper for conveying the flake cake in oil, and an incinerator for incinerating the cake dried in the oil tank. A sludge drying and incinerating device.
該脱水機で得られたケーキを貯留するケーキ貯留槽と、
該貯留槽のケーキをホッパーに移送するケーキ移送ポン
プと、前記ホッパー内のケーキの塊をほぐし、ケーキを
平均に送り出すならし羽根を内蔵したケーキ厚み成形機
と、該成形機で得られた薄片状のケーキを油中で搬送さ
せるスクレーパーを備えた油槽と、該油槽で乾燥したケ
ーキを焼却する焼却炉とからなることを特徴とする汚泥
の乾燥、焼却装置。5. A dehydrator for dehydrating sludge into a cake,
A cake storage tank for storing the cake obtained by the dehydrator,
A cake transfer pump for transferring the cake in the storage tank to a hopper, a cake thickness molding machine having a built-in leveling blade for loosening the cake lump in the hopper and sending the cake evenly, and a thin piece obtained by the molding machine. An apparatus for drying and incinerating sludge, comprising an oil tank equipped with a scraper for transporting a cake in the form of oil, and an incinerator for incinerating the cake dried in the oil tank.
機は一対の内方向に回転するロールまたは押出し用口金
を備えていることを特徴とする請求項2、4または5記
載の汚泥の乾燥、焼却装置。6. The sludge forming machine according to claim 2, 4 or 5, wherein the cake thickness molding machine according to claim 2, 4 or 5 is provided with a pair of inwardly rotating rolls or an extrusion die. Drying and incineration equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5029593A JPH06218397A (en) | 1993-01-27 | 1993-01-27 | Method and device for drying and firing sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5029593A JPH06218397A (en) | 1993-01-27 | 1993-01-27 | Method and device for drying and firing sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06218397A true JPH06218397A (en) | 1994-08-09 |
Family
ID=12280377
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5029593A Pending JPH06218397A (en) | 1993-01-27 | 1993-01-27 | Method and device for drying and firing sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06218397A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3018734U (en) * | 1995-05-29 | 1995-11-28 | フレックス株式会社 | Cow manure dryer |
WO2001030708A1 (en) * | 1999-10-29 | 2001-05-03 | Asahi Engineering Corporation | Clarification treatment apparatus and method for clarification treatment |
KR100395119B1 (en) * | 2000-12-29 | 2003-08-21 | 한국에너지기술연구원 | An apparatus for feeding and drying sewage sludge |
JP2009539587A (en) * | 2006-06-14 | 2009-11-19 | レ テクノロジーズ エルコテック インコーポレイテッド | Process and apparatus for treating a substance and / or increasing its dryness |
JP2010023024A (en) * | 2008-07-18 | 2010-02-04 | Hanbat National Univ Industry-Academic Cooperation Foundation | Vaporizing and drying device of organic sludge immersed in oil |
CN102701559A (en) * | 2012-05-24 | 2012-10-03 | 天津科技大学 | Method and device for comprehensively treating sludge generated by sewage treatment plant and kitchen waste oil |
WO2017077251A1 (en) | 2015-11-05 | 2017-05-11 | Cleef System | Facility and method for drying a pasty product |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4943873A (en) * | 1972-09-02 | 1974-04-25 | ||
JPS5767777A (en) * | 1980-10-13 | 1982-04-24 | Kurita Water Ind Ltd | Dryer for sludge or the like |
JPH0427497A (en) * | 1990-05-22 | 1992-01-30 | Kitajima Hirotane | Treatment of organic industrial waste |
-
1993
- 1993-01-27 JP JP5029593A patent/JPH06218397A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4943873A (en) * | 1972-09-02 | 1974-04-25 | ||
JPS5767777A (en) * | 1980-10-13 | 1982-04-24 | Kurita Water Ind Ltd | Dryer for sludge or the like |
JPH0427497A (en) * | 1990-05-22 | 1992-01-30 | Kitajima Hirotane | Treatment of organic industrial waste |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3018734U (en) * | 1995-05-29 | 1995-11-28 | フレックス株式会社 | Cow manure dryer |
WO2001030708A1 (en) * | 1999-10-29 | 2001-05-03 | Asahi Engineering Corporation | Clarification treatment apparatus and method for clarification treatment |
KR100395119B1 (en) * | 2000-12-29 | 2003-08-21 | 한국에너지기술연구원 | An apparatus for feeding and drying sewage sludge |
JP2009539587A (en) * | 2006-06-14 | 2009-11-19 | レ テクノロジーズ エルコテック インコーポレイテッド | Process and apparatus for treating a substance and / or increasing its dryness |
US8454814B2 (en) | 2006-06-14 | 2013-06-04 | GL&V Canada | Processes and apparatuses for treating and/or increasing dryness of a substance |
JP2010023024A (en) * | 2008-07-18 | 2010-02-04 | Hanbat National Univ Industry-Academic Cooperation Foundation | Vaporizing and drying device of organic sludge immersed in oil |
CN102701559A (en) * | 2012-05-24 | 2012-10-03 | 天津科技大学 | Method and device for comprehensively treating sludge generated by sewage treatment plant and kitchen waste oil |
WO2017077251A1 (en) | 2015-11-05 | 2017-05-11 | Cleef System | Facility and method for drying a pasty product |
FR3043453A1 (en) * | 2015-11-05 | 2017-05-12 | Cleef System | INSTALLATION AND METHOD FOR DRYING A PRODUCT IN A PASTY CONDITION |
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