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JPH0221879B2 - - Google Patents
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JPH0221879B2 - - Google Patents

Info

Publication number
JPH0221879B2
JPH0221879B2 JP57009264A JP926482A JPH0221879B2 JP H0221879 B2 JPH0221879 B2 JP H0221879B2 JP 57009264 A JP57009264 A JP 57009264A JP 926482 A JP926482 A JP 926482A JP H0221879 B2 JPH0221879 B2 JP H0221879B2
Authority
JP
Japan
Prior art keywords
sludge
heating chamber
heating
dryer
blades
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
JP57009264A
Other languages
Japanese (ja)
Other versions
JPS58124600A (en
Inventor
Kenichi Nagaoka
Yoshuki Yoshinaga
Juji Toyama
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.)
Osaka Gas Co Ltd
Original Assignee
Osaka Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Osaka Gas Co Ltd filed Critical Osaka Gas Co Ltd
Priority to JP57009264A priority Critical patent/JPS58124600A/en
Publication of JPS58124600A publication Critical patent/JPS58124600A/en
Publication of JPH0221879B2 publication Critical patent/JPH0221879B2/ja
Granted legal-status Critical Current

Links

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  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 本発明は、下水汚泥等の水処理汚泥や産業廃棄
物汚泥などの各種汚泥を、横型ドラム状加熱壁に
よつて囲まれた加熱室内に掻上げ用回転羽根を設
けた乾燥機によつて乾燥する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides rotating blades for scraping up various types of sludge such as water treatment sludge such as sewage sludge and industrial waste sludge in a heating chamber surrounded by a horizontal drum-shaped heating wall. The present invention relates to a method of drying using a dryer.

上記方法は、回転羽根の作用によつて、汚泥を
加熱壁に対して周方向広範囲にわたつて接触さ
せ、加熱室の容量の割には大量乾燥処理を行える
ように意図されたものであるが、従来、上記方法
を実施するに、第3図に示すように、単純に、汚
泥を、横型ドラム状加熱室1に供給口2から供給
し、回転羽根5の作用で排出口6に向かつて送り
ながら、ジヤケツト8及び回転羽根5に供給され
るスチームで乾燥しており、次のような欠点があ
つた。つまり、加熱室1に供給される汚泥は、加
熱室1へのポンプ流路12による搬送や加熱室1
での回転羽根5による撹拌に伴うシクソトロピー
現象等により、さらには、加熱室1内での加熱に
より流動しやすくなるために、回転羽根5による
汚泥掻上げが不十分になり、加熱壁7との接触面
積を大にして、乾燥効率を向上しようとする技術
意図が十分達成できないことが多かつた。
The above method is intended to bring the sludge into contact with the heating wall over a wide area in the circumferential direction by the action of the rotating blades, and to be able to perform a large-volume drying process considering the capacity of the heating chamber. Conventionally, to carry out the above method, as shown in FIG. While being fed, the material was dried by the steam supplied to the jacket 8 and the rotary blade 5, resulting in the following drawbacks. In other words, the sludge supplied to the heating chamber 1 is transported by the pump channel 12 to the heating chamber 1 or
Due to the thixotropic phenomenon accompanying the stirring by the rotary blades 5, and furthermore, the heating in the heating chamber 1 causes the sludge to flow more easily, resulting in insufficient scraping of the sludge by the rotary blades 5, which causes the sludge to interfere with the heating wall 7. The technical intention of increasing the drying efficiency by increasing the contact area was often not fully achieved.

本発明の目的は、極めて簡単な手段でもつて、
汚泥が乾燥機に供給する以前から流動しやすいも
のであつたり、あるいは、乾燥中に流動しやすく
なるものであつても、回転羽根による汚泥掻上げ
が十分に行われるようにし、効率の良い乾燥処理
を確実に行えるようにすることにある。
The object of the present invention is to, by extremely simple means,
Even if the sludge is fluid before it is supplied to the dryer, or even if it becomes fluid during drying, the rotating blades should be able to sufficiently scrape up the sludge to ensure efficient drying. The purpose is to ensure that processing can be carried out reliably.

本発明方法の特徴手段は、横型ドラム状加熱壁
によつて囲まれると共に掻上げ用回転羽根を内装
した加熱室から取出したゲル状汚泥の一部を、前
記加熱室に供給する汚泥に、その汚泥の流動状態
が前記回転羽根による汚泥掻上げに適した状態に
なるように混入することにある。
The characteristic means of the method of the present invention is that a part of gel-like sludge taken out from a heating chamber surrounded by a horizontal drum-shaped heating wall and equipped with rotary scraping blades is added to the sludge supplied to the heating chamber. The purpose is to mix the sludge in such a way that the fluid state of the sludge is suitable for sludge scraping by the rotating blades.

上記特徴手段による効果は次の通りである。 The effects of the above characteristic means are as follows.

つまり、単に乾燥処理した汚泥の一部を、加熱
室に供給するに先立つてあるいは加熱室内で乾燥
処理すべき汚泥に混入するだけの極めて簡単な操
作あるいは設備でもつて、加熱室内の汚泥の流動
状態を回転羽根によつて十分に掻上げられるよう
に調節でき、その結果、加熱壁に対して汚泥を十
分大なる面積において接触させて、加熱室の容量
の割に乾燥能力を大にすることを、汚泥の性状に
かかわらず確実に行えるようになつた。
In other words, even with an extremely simple operation or equipment in which a part of the dried sludge is simply mixed into the sludge to be dried before being supplied to the heating chamber or within the heating chamber, the fluidity of the sludge in the heating chamber can be controlled. The sludge can be adjusted to be sufficiently scraped up by the rotating blades, and as a result, the sludge can be brought into contact with the heating wall over a sufficiently large area, increasing the drying capacity in relation to the capacity of the heating chamber. , can now be carried out reliably regardless of the properties of the sludge.

次に、第1図及び第2図により実施例を示す。 Next, an example will be shown with reference to FIGS. 1 and 2.

乾燥機Aに備えられた横型ドラム状加熱室1
に、乾燥処理すべ脱水処理汚泥を供給口2から投
入し、加熱室1内において、電動モータ3及び減
速機4の作用で回転される回転羽根5によつて掻
上げ及び撹拌しながら排出口6に向つて移動させ
ると共に、加熱室1を囲む加熱壁7及び回転羽根
5を介して、加熱壁7を囲むジヤケツト8内で入
口9aから出口10aに向かつて流動されるスチ
ーム等の加熱流体、並びに回転羽根5内で入口9
bから出口10bに向かつて流動されるスチーム
等の加熱流体によつて、加熱室1内の汚泥を乾燥
させ、ゲル状に乾燥した汚泥を排出口6から取出
し、間接加熱方式で連続的に汚泥を乾燥処理す
る。
Horizontal drum-shaped heating chamber 1 provided in dryer A
The dried and dewatered sludge is introduced from the supply port 2, and is scraped up and stirred in the heating chamber 1 by the rotary blades 5 rotated by the action of the electric motor 3 and the speed reducer 4, while being pumped through the discharge port 6. A heating fluid such as steam that is moved toward the heating chamber 1 and flows from the inlet 9a to the outlet 10a within the jacket 8 surrounding the heating wall 7 via the heating wall 7 surrounding the heating chamber 1 and the rotating blade 5; Inlet 9 within rotating blade 5
The sludge in the heating chamber 1 is dried by a heating fluid such as steam flowing from b toward the outlet 10b, and the gel-like dried sludge is taken out from the discharge port 6, and the sludge is continuously heated using an indirect heating method. be dried.

排出口6から取出したゲル状汚泥の一部を、コ
ンベア11a,11bによつて混合装置13に送
つて、加熱室1に供給する汚泥に、適量づつ連続
的あるいは間欠的に混して、加熱室1内の汚泥の
流動状態を、回転羽根5による汚泥掻上げが十分
に行われて、加熱壁7と汚泥の接触面積、換言す
ると加熱室1周方向における接触巾lを十分大に
なるように調節する。
A portion of the gel-like sludge taken out from the discharge port 6 is sent to the mixing device 13 via conveyors 11a and 11b, where it is continuously or intermittently mixed with the sludge supplied to the heating chamber 1, and heated. The flow state of the sludge in the chamber 1 is adjusted so that the sludge is sufficiently scraped up by the rotary blades 5, and the contact area between the heating wall 7 and the sludge, in other words, the contact width l in the circumferential direction of the heating chamber is made sufficiently large. Adjust to

乾燥処理すべき汚泥に対するゲル状汚泥の混入
割合を、可動ホツパー14の位置調節によつて、
前者汚泥の性状や含水率、さらには加熱室1の直
径等の乾燥機A条件などに応じて、乾燥処理効率
が向上するように設定するが、一般的には、平均
水分が60〜65wt%程度になるように混合する。
By adjusting the position of the movable hopper 14, the mixing ratio of gel sludge to the sludge to be dried is adjusted.
The former is set to improve the drying efficiency depending on the properties and moisture content of the sludge, as well as the dryer A conditions such as the diameter of the heating chamber 1, but in general, the average moisture content is 60 to 65 wt%. Mix until evenly mixed.

次に、別の実施例を示す。 Next, another example will be shown.

排出口6から取出したゲル状汚泥を加熱室1内
に、汚泥移送方向適当な位置において連続的ある
いは間歇的に投入することもでき、また、ゲル状
汚泥混入を人為作業によつて行うこともできる。
The gelled sludge taken out from the discharge port 6 can be continuously or intermittently fed into the heating chamber 1 at an appropriate position in the sludge transfer direction, or the gelled sludge can be mixed manually. can.

乾燥機Aの構成を、例えば回転羽根5の形状を
変える等、各種変形が可能である。
Various modifications can be made to the configuration of the dryer A, such as changing the shape of the rotary blades 5, for example.

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

第1図は本発明方法に利用する乾燥機を例示す
る概略縦断面図、第2図は第1図の−線断面
図、第3図は従来方法に利用されていた乾燥機の
概略縦断面図である。 1……加熱室、5……回転羽根、7……加熱
壁、A……乾燥機。
Fig. 1 is a schematic vertical cross-sectional view illustrating a dryer used in the method of the present invention, Fig. 2 is a cross-sectional view taken along the line - - in Fig. 1, and Fig. 3 is a schematic longitudinal cross-sectional view of a dryer used in the conventional method. It is a diagram. 1... Heating chamber, 5... Rotating blade, 7... Heating wall, A... Dryer.

Claims (1)

【特許請求の範囲】[Claims] 1 横型ドラム状加熱壁7によつて囲まれた加熱
室1内に掻上げ用回転羽根5を設けた乾燥機Aに
よつて、汚泥を乾燥する方法であつて、前記加熱
室1から取出したゲル状汚泥の一部を、前記加熱
室1に供給する汚泥に、その汚泥の流動状態が前
記回転羽根5による汚泥掻上げに適した状態にな
るように混入することを特徴とする汚泥乾燥方
法。
1. A method of drying sludge using a dryer A equipped with rotary raking blades 5 in a heating chamber 1 surrounded by a horizontal drum-shaped heating wall 7, in which sludge is removed from the heating chamber 1. A sludge drying method characterized in that a part of gel-like sludge is mixed into the sludge supplied to the heating chamber 1 so that the fluid state of the sludge becomes suitable for sludge scraping by the rotary blades 5. .
JP57009264A 1982-01-21 1982-01-21 Method of drying sludge Granted JPS58124600A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57009264A JPS58124600A (en) 1982-01-21 1982-01-21 Method of drying sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57009264A JPS58124600A (en) 1982-01-21 1982-01-21 Method of drying sludge

Publications (2)

Publication Number Publication Date
JPS58124600A JPS58124600A (en) 1983-07-25
JPH0221879B2 true JPH0221879B2 (en) 1990-05-16

Family

ID=11715571

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57009264A Granted JPS58124600A (en) 1982-01-21 1982-01-21 Method of drying sludge

Country Status (1)

Country Link
JP (1) JPS58124600A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6375478A (en) * 1986-09-18 1988-04-05 青木 福男 Drier
JP4917940B2 (en) * 2007-03-29 2012-04-18 大成建設株式会社 Tunnel construction method
JP6591875B2 (en) * 2015-11-24 2019-10-16 三菱マテリアルテクノ株式会社 Hydrous sludge drying system

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4842447A (en) * 1971-10-04 1973-06-20

Also Published As

Publication number Publication date
JPS58124600A (en) 1983-07-25

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