JPH11300397A - Sludge drying device - Google Patents

Sludge drying device

Info

Publication number
JPH11300397A
JPH11300397A JP10106277A JP10627798A JPH11300397A JP H11300397 A JPH11300397 A JP H11300397A JP 10106277 A JP10106277 A JP 10106277A JP 10627798 A JP10627798 A JP 10627798A JP H11300397 A JPH11300397 A JP H11300397A
Authority
JP
Japan
Prior art keywords
sludge
moisture content
centrifugal thin
heat transfer
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.)
Withdrawn
Application number
JP10106277A
Other languages
Japanese (ja)
Inventor
Hiroichi Yamamoto
本 博 一 山
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP10106277A priority Critical patent/JPH11300397A/en
Publication of JPH11300397A publication Critical patent/JPH11300397A/en
Withdrawn legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a sludge drying device by which sludge is efficiently dried in a centrifugal thin-film drier. SOLUTION: This sludge drying device is provided with a centrifugal thin-film drier 1 having a heat-transfer drum 1a for drying the sludge and a sludge feed pipeline 2 for supplying the sludge into a heat-transfer drum 1a. The heating device 3 consisting of a piping 3a of the material resistant to induction heating and an electromagnetic induction heater 4 set outside the piping 3a is furnished to the sludge feed pipeline 2. The sludge in the pipeline 2 is heated by a heating device 3 to prevent the lowering of viscosity of the sludge, and the sludge is extended on the inner face of the drum 1a into film and surely dried.

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、下水汚泥等の汚泥
を処理する汚泥乾燥装置に係り、とりわけ効率良く汚泥
を乾燥させることができる汚泥乾燥装置に関する。
The present invention relates to a sludge drying apparatus for treating sludge such as sewage sludge, and more particularly to a sludge drying apparatus capable of efficiently drying sludge.

【0002】[0002]

【従来の技術】従来、下水汚泥等の汚泥処理において、
汚泥を乾燥するために伝熱胴を有する遠心薄膜乾燥機が
用いられている。この遠心薄膜乾燥機では、汚泥供給配
管によって供給された汚泥が伝熱胴内で薄膜状に引延ば
されて乾燥する。
2. Description of the Related Art Conventionally, in the treatment of sludge such as sewage sludge,
A centrifugal thin film dryer having a heat transfer drum is used to dry sludge. In this centrifugal thin film dryer, the sludge supplied by the sludge supply pipe is stretched into a thin film in the heat transfer drum and dried.

【0003】このとき、供給汚泥の含水率が低いと汚泥
の粘性が高まるため、汚泥が遠心薄膜乾燥機の伝熱胴内
に流入したとき、伝熱胴内で汚泥が薄膜状になりにくく
なり、汚泥層が厚くなって乾燥効率が低下する。あるい
は遠心薄膜乾燥機への汚泥供給に脈動が生じ、遠心薄膜
乾燥機の伝熱胴によって乾燥された汚泥の含水率にムラ
が生じやすくなる。また供給汚泥の粘性が極端に高まる
と、汚泥供給配管内に詰まりが生じる恐れもあり、詰ま
りを解消するためには洗浄などの保守が必要となる。
[0003] At this time, if the water content of the supplied sludge is low, the viscosity of the sludge increases, so that when the sludge flows into the heat transfer cylinder of the centrifugal thin film dryer, the sludge hardly becomes a thin film in the heat transfer cylinder. As a result, the sludge layer becomes thicker and the drying efficiency decreases. Alternatively, pulsation occurs in the sludge supply to the centrifugal thin film dryer, and the moisture content of the sludge dried by the heat transfer drum of the centrifugal thin film dryer tends to be uneven. If the viscosity of the supplied sludge becomes extremely high, clogging may occur in the sludge supply pipe, and maintenance such as washing is required to eliminate the clogging.

【0004】[0004]

【発明が解決しようとする課題】上述のように、遠心薄
膜乾燥機の汚泥乾燥効率を向上するには、供給される汚
泥の含水率が低下しないようにしなければならない。ま
た、供給される汚泥の含水率が低下した場合でも、遠心
薄膜乾燥機によって乾燥された汚泥の含水率を低い値に
安定的に維持しなければならない。
As described above, in order to improve the sludge drying efficiency of the centrifugal thin film dryer, it is necessary to prevent the water content of the supplied sludge from decreasing. Further, even when the water content of the supplied sludge decreases, the water content of the sludge dried by the centrifugal thin film dryer must be stably maintained at a low value.

【0005】本発明はこのような点を考慮してなされた
ものであり、効率良く汚泥を乾燥することができる汚泥
乾燥装置を提供することを目的とする。
[0005] The present invention has been made in view of such a point, and an object of the present invention is to provide a sludge drying apparatus capable of efficiently drying sludge.

【0006】[0006]

【課題を解決するための手段】本発明は、内部に汚泥が
投入され、この汚泥を乾燥させて乾燥汚泥を生成する伝
熱胴を有する遠心薄膜乾燥機と、伝熱胴内へ汚泥を供給
する汚泥供給配管と、汚泥供給配管に設けられ、汚泥を
加熱する加熱装置とを備えたことを特徴とする汚泥乾燥
装置である。
SUMMARY OF THE INVENTION According to the present invention, there is provided a centrifugal thin-film dryer having a heat transfer drum for introducing sludge into the inside thereof and drying the sludge to produce dry sludge, and supplying the sludge into the heat transfer drum. And a heating device provided on the sludge supply pipe to heat the sludge.

【0007】本発明によれば、加熱装置によって汚泥供
給配管内の汚泥を加熱することにより、遠心薄膜乾燥機
の伝熱胴内に供給される汚泥の粘性低下を防ぐことがで
きる。
According to the present invention, by heating the sludge in the sludge supply pipe by the heating device, it is possible to prevent the viscosity of the sludge supplied into the heat transfer drum of the centrifugal thin film dryer from decreasing.

【0008】[0008]

【発明の実施の形態】以下、図面を参照して本発明によ
る汚泥乾燥装置の実施の形態について説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, an embodiment of a sludge drying apparatus according to the present invention will be described with reference to the drawings.

【0009】図1は本発明による汚泥乾燥装置の第1の
実施の形態を示す系統構成図である。
FIG. 1 is a system configuration diagram showing a first embodiment of a sludge drying apparatus according to the present invention.

【0010】図1に示すように汚泥乾燥装置は、投入さ
れた汚泥を引延ばして乾燥させる伝熱胴1aを有する遠
心薄膜乾燥機1と、伝熱胴1a内に汚泥を供給する汚泥
供給配管2と、汚泥供給配管2に設けられ汚泥を加熱す
る加熱装置3とを備えている。
As shown in FIG. 1, the sludge drying apparatus includes a centrifugal thin film dryer 1 having a heat transfer drum 1a for extending and drying sludge supplied thereto, and a sludge supply pipe for supplying sludge into the heat transfer drum 1a. 2 and a heating device 3 provided in the sludge supply pipe 2 for heating the sludge.

【0011】このうち加熱装置3は汚泥供給配管2に介
在された耐誘導加熱材管路3aと、この耐誘導加熱材管
路3a外方に配置された電磁誘導加熱装置4とを有して
いる。
The heating device 3 includes an induction heating material pipe 3a interposed in the sludge supply pipe 2, and an electromagnetic induction heating device 4 disposed outside the induction heating material pipe 3a. I have.

【0012】また汚泥供給配管2には汚泥供給ポンプ5
が接続されている。さらに遠心薄膜乾燥機1の伝熱胴1
aの外方には、伝熱胴1aを加熱する加熱蒸気か流入す
る加熱蒸気入口6と加熱蒸気出口7とが設けられてい
る。また遠心薄膜乾燥機1の伝熱胴1aは内部にブレー
ド(図示せず)を有し、このブレードが数百rpmで回
転することにより、供給された汚泥を薄膜状に引延ばし
て乾燥処理する。また遠心薄膜乾燥機1の伝熱胴1a内
では汚泥の乾燥中に臭気ガスが発生し、この臭気ガスは
抽気ブロア9により抽気ガス管8を通り脱臭装置10に
運ばれ脱臭処理される。
A sludge supply pump 5 is connected to the sludge supply pipe 2.
Is connected. Further, the heat transfer drum 1 of the centrifugal thin film dryer 1
Outside of a, a heating steam inlet 6 and a heating steam outlet 7 into which heating steam for heating the heat transfer drum 1a flows are provided. The heat transfer drum 1a of the centrifugal thin-film dryer 1 has a blade (not shown) inside, and the blade rotates at several hundred rpm to spread the supplied sludge into a thin film and perform a drying process. . In the heat transfer drum 1a of the centrifugal thin-film dryer 1, odor gas is generated during drying of the sludge, and the odor gas is carried by the bleed gas blower 9 through the bleed gas pipe 8 to the deodorizer 10, where it is subjected to deodorization.

【0013】次にこのような構成からなる本実施の形態
の作用について説明する。まず汚泥供給ポンプ5により
汚泥が圧送され、汚泥供給配管2を経由して遠心薄膜乾
燥機1の伝熱胴1a内に投入される。伝熱胴1a内にお
いて汚泥は伝熱胴1a内面に引延ばされ、加熱蒸気入口
6から流入する蒸気により加熱されて乾燥される。この
場合、蒸気は加熱蒸気入口6から流入して伝熱胴1aの
外面を加熱し、その後加熱蒸気出口7から流出する。
Next, the operation of the embodiment having the above-described configuration will be described. First, sludge is pressure-fed by a sludge supply pump 5 and is fed into the heat transfer drum 1a of the centrifugal thin film dryer 1 via the sludge supply pipe 2. In the heat transfer drum 1a, the sludge is spread on the inner surface of the heat transfer drum 1a, and is heated and dried by the steam flowing from the heating steam inlet 6. In this case, the steam flows in from the heating steam inlet 6 to heat the outer surface of the heat transfer drum 1a, and then flows out from the heating steam outlet 7.

【0014】この間、汚泥は汚泥供給配管2に設置され
た耐誘導加熱材管路3内を通過する。このとき、電磁誘
導加熱装置4により耐誘導加熱材管路3内の汚泥が加熱
され、汚泥の粘性が低下する。このため汚泥は汚泥供給
配管2内を容易に通過できるようになる。特に冬季な
ど、外気温が低下している際には、このような汚泥の加
熱が有効となる。また、加熱された汚泥を遠心薄膜乾燥
機1の伝熱胴1a内に投入することにより、伝熱胴1a
内での乾燥処理も、より効率的に行なわれ、安定した低
含水率の汚泥を得ることができる。
During this time, the sludge passes through the induction heating material pipe 3 installed in the sludge supply pipe 2. At this time, the sludge in the induction heating material pipe 3 is heated by the electromagnetic induction heating device 4, and the viscosity of the sludge decreases. Thus, the sludge can easily pass through the sludge supply pipe 2. In particular, when the outside air temperature is falling, such as in winter, such heating of the sludge is effective. Also, by feeding the heated sludge into the heat transfer cylinder 1a of the centrifugal thin film dryer 1, the heat transfer cylinder 1a
The drying process in the inside is also performed more efficiently, and it is possible to obtain a sludge having a stable low moisture content.

【0015】ここで、例えば汚泥供給配管2の外側を加
熱蒸気などの別の熱源を利用して加熱した場合、熱は汚
泥供給配管2外周部を加熱することになり、汚泥そのも
のを十分加熱できない場合も考えられる。これに対して
本発明によれば、電磁誘導加熱装置4を用いて、耐誘導
加熱材管路3を通過する汚泥を外部および内部から均等
に加熱することができ、汚泥の粘性低下を防ぐことがで
きる。このため汚泥の流動性を高めて、汚泥を伝熱胴1
a内面に薄膜状に確実に延ばすことができ、伝熱胴1a
内での乾燥効果をより高めることができる。また、汚泥
供給配管2内での汚泥の粘性低下を防ぐことができるの
で、汚泥供給配管2内での汚泥の脈動や閉塞の発生を防
止することができ、より安定した運転を行なうことがで
きる。
Here, for example, if the outside of the sludge supply pipe 2 is heated using another heat source such as heating steam, the heat will heat the outer periphery of the sludge supply pipe 2 and the sludge itself cannot be sufficiently heated. It is possible. On the other hand, according to the present invention, the sludge passing through the induction heating material pipe 3 can be uniformly heated from the outside and the inside by using the electromagnetic induction heating device 4 to prevent the viscosity of the sludge from decreasing. Can be. Therefore, the fluidity of the sludge is increased, and the sludge is transferred to the heat transfer cylinder 1.
a can be reliably extended in the form of a thin film on the inner surface.
The drying effect in the inside can be further enhanced. Further, since the sludge viscosity in the sludge supply pipe 2 can be prevented from lowering, sludge pulsation and blockage in the sludge supply pipe 2 can be prevented, and more stable operation can be performed. .

【0016】次に図2により本発明による汚泥乾燥装置
の第2の実施の形態について説明する。図2において、
図1に示す第1の実施の形態と同一部分には同一符号を
付して詳細な説明は省略する。
Next, a second embodiment of the sludge drying apparatus according to the present invention will be described with reference to FIG. In FIG.
The same parts as those in the first embodiment shown in FIG. 1 are denoted by the same reference numerals, and detailed description is omitted.

【0017】図2に示すように汚泥供給ポンプ5の上流
側に投入汚泥貯留槽12が設けられており、この汚泥貯
留槽12上に遠心薄膜乾燥機1へ投入される汚泥の含水
率を検出する投入汚泥含水率検出器(第1含水率計)1
1が設けられている。
As shown in FIG. 2, an input sludge storage tank 12 is provided on the upstream side of the sludge supply pump 5, and the water content of the sludge supplied to the centrifugal thin film dryer 1 is detected on the sludge storage tank 12. Input sludge moisture content detector (first moisture content meter) 1
1 is provided.

【0018】また遠心薄膜乾燥機1の下方に、遠心薄膜
乾燥機1によって乾燥された汚泥を排出する排出コンベ
ア14が設けられ、この排出コンベア14上に乾燥汚泥
の含水率を検出する乾燥汚泥含水率検出器(第2含水率
計)13が設けられている。さらに投入汚泥含水率検出
器11および乾燥汚泥含水率検出器13からの信号は電
源調整装置15に送られ、この電源調整装置15によっ
て電源誘導加熱装置4の出力が調整されるようになって
いる。
A discharge conveyor 14 for discharging sludge dried by the centrifugal thin film dryer 1 is provided below the centrifugal thin film dryer 1. On this discharge conveyor 14, a dry sludge hydrate for detecting the moisture content of the dry sludge is provided. A rate detector (second moisture content meter) 13 is provided. Further, signals from the input sludge moisture content detector 11 and the dried sludge moisture content detector 13 are sent to a power supply adjusting device 15, and the output of the power supply induction heating device 4 is adjusted by the power supply adjusting device 15. .

【0019】図2において、電源調整装置15へは、投
入汚泥含水率検出器11と乾燥汚泥含水率検出器13か
らの測定信号が入力される。電源調整装置15では、投
入汚泥含水率検出器11により検出された投入汚泥の含
水率が下がった場合、あるいは、乾燥汚泥含水率検出器
13により検出された乾燥汚泥の含水率が上昇した場
合、電磁誘導加熱装置4の電源をONとする。さらに投
入汚泥含水率検出器11と乾燥汚泥含水率検出器13か
らの測定信号に基づいて、投入汚泥の含水率が大きく下
がったり、乾燥汚泥の含水率が大きく上昇した場合は、
電源調整装置15により電磁誘導加熱装置4への供給電
力を増加させ、このことにより耐誘導加熱材管路3を通
過する汚泥を強力に加熱する。
In FIG. 2, measurement signals from the input sludge moisture content detector 11 and the dry sludge moisture content detector 13 are input to the power supply adjusting device 15. In the power supply adjusting device 15, when the water content of the input sludge detected by the input sludge water content detector 11 decreases, or when the water content of the dry sludge detected by the dry sludge water content detector 13 increases, The power supply of the electromagnetic induction heating device 4 is turned on. Furthermore, based on the measurement signals from the input sludge moisture content detector 11 and the dry sludge moisture content detector 13, when the moisture content of the input sludge greatly decreases or the moisture content of the dry sludge greatly increases,
The power supplied to the electromagnetic induction heating device 4 is increased by the power supply adjustment device 15, thereby strongly heating the sludge passing through the anti-induction heating material pipe 3.

【0020】このようにして、投入汚泥の含水率が上昇
して粘性が高まった場合、あるいは遠心薄膜乾燥機1か
らの乾燥汚泥の含水率が上昇した場合に、これらの状態
を修正するとともに、汚泥供給配管2内における汚泥の
脈動や閉塞の発生を防止し、安定した低含水率の乾燥汚
泥を得ることができる。
In this way, when the water content of the input sludge increases and the viscosity increases, or when the water content of the dry sludge from the centrifugal thin film dryer 1 increases, these conditions are corrected, Pulsation and blockage of the sludge in the sludge supply pipe 2 can be prevented, and stable dry sludge with a low water content can be obtained.

【0021】なお、上記各実施の形態に示す汚泥乾燥装
置は、下水汚泥の乾燥分野に限らず、汚泥の乾燥全般に
適用できることは勿論である。
The sludge drying apparatus shown in each of the above embodiments can be applied not only to the sewage sludge drying field but also to sludge drying in general.

【0022】[0022]

【発明の効果】以上説明したように、本発明によれば、
汚泥供給配管を通って遠心薄膜乾燥機に投入される汚泥
を加熱することにより、汚泥の粘性低下を防止でき、か
つ遠心薄膜乾燥機内での乾燥効果をより高めることがで
きる。また汚泥供給配管内における汚泥の脈動や閉塞の
発生を防止し、安定した運転を行なうことができる。
As described above, according to the present invention,
By heating the sludge fed into the centrifugal thin-film dryer through the sludge supply pipe, it is possible to prevent the viscosity of the sludge from lowering and to further enhance the drying effect in the centrifugal thin-film dryer. Further, pulsation and blockage of sludge in the sludge supply pipe can be prevented, and stable operation can be performed.

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

【図1】本発明による汚泥乾燥装置の第1の実施の形態
を示す構成図。
FIG. 1 is a configuration diagram showing a first embodiment of a sludge drying device according to the present invention.

【図2】本発明による汚泥乾燥装置の第2の実施の形態
を示す構成図。
FIG. 2 is a configuration diagram showing a second embodiment of the sludge drying device according to the present invention.

【符号の説明】[Explanation of symbols]

1 遠心薄膜乾燥機 1a 伝熱胴 2 汚泥供給配管 3 耐誘導加熱材管路 4 電磁誘導加熱装置 5 汚泥供給ポンプ 11 投入汚泥含水率検出器 13 乾燥汚泥含水率検出器 15 電源調整装置 DESCRIPTION OF SYMBOLS 1 Centrifugal thin film dryer 1a Heat transfer cylinder 2 Sludge supply piping 3 Induction heating material pipe 4 Electromagnetic induction heating device 5 Sludge supply pump 11 Input sludge moisture content detector 13 Dry sludge moisture content detector 15 Power supply adjustment device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】内部に汚泥が投入され、この汚泥を乾燥さ
せて乾燥汚泥を生成する伝熱胴を有する遠心薄膜乾燥機
と、 伝熱胴内へ汚泥を供給する汚泥供給配管と、 汚泥供給配管に設けられ、汚泥を加熱する加熱装置とを
備えたことを特徴とする汚泥乾燥装置。
1. A centrifugal thin-film dryer having a heat transfer drum for generating sludge by drying sludge therein, a sludge supply pipe for supplying sludge into the heat transfer drum, and a sludge supply. A sludge drying device comprising: a heating device provided in a pipe for heating sludge.
【請求項2】遠心薄膜乾燥機へ供給される汚泥の含水率
を測定する第1含水率計と、 遠心薄膜乾燥機によって乾燥された乾燥汚泥の含水率を
測定する第2含水率計とを更に備え、 これら第1含水率計と第2含水率計からの信号に基づい
て、加熱装置の出力を調整する調整装置を設けたことを
特徴とする請求項1記載の汚泥乾燥装置。
2. A first moisture content meter for measuring the moisture content of sludge supplied to a centrifugal thin film dryer, and a second moisture content meter for measuring the moisture content of dried sludge dried by the centrifugal thin film dryer. The sludge drying device according to claim 1, further comprising an adjusting device for adjusting an output of the heating device based on signals from the first moisture content meter and the second moisture content meter.
JP10106277A 1998-04-16 1998-04-16 Sludge drying device Withdrawn JPH11300397A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10106277A JPH11300397A (en) 1998-04-16 1998-04-16 Sludge drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10106277A JPH11300397A (en) 1998-04-16 1998-04-16 Sludge drying device

Publications (1)

Publication Number Publication Date
JPH11300397A true JPH11300397A (en) 1999-11-02

Family

ID=14429596

Family Applications (1)

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JP10106277A Withdrawn JPH11300397A (en) 1998-04-16 1998-04-16 Sludge drying device

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110357378A (en) * 2019-06-26 2019-10-22 上海煜工环保科技有限公司 A kind of organic solid waste carbonization method of disposal of energy-efficient electromagnetic induction heating and device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110357378A (en) * 2019-06-26 2019-10-22 上海煜工环保科技有限公司 A kind of organic solid waste carbonization method of disposal of energy-efficient electromagnetic induction heating and device

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