JPH0412000A - System for transporting dehydrated sludge under pressure through pipeline - Google Patents

System for transporting dehydrated sludge under pressure through pipeline

Info

Publication number
JPH0412000A
JPH0412000A JP11175990A JP11175990A JPH0412000A JP H0412000 A JPH0412000 A JP H0412000A JP 11175990 A JP11175990 A JP 11175990A JP 11175990 A JP11175990 A JP 11175990A JP H0412000 A JPH0412000 A JP H0412000A
Authority
JP
Japan
Prior art keywords
main pipe
sludge
incinerator
pipe
dehydrated sludge
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
Application number
JP11175990A
Other languages
Japanese (ja)
Inventor
Kiyoshi Kuioka
杭岡 潔
Kunio Takeya
武谷 国男
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.)
Ube Corp
Original Assignee
Ube Industries 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP11175990A priority Critical patent/JPH0412000A/en
Publication of JPH0412000A publication Critical patent/JPH0412000A/en
Pending legal-status Critical Current

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  • Air Transport Of Granular Materials (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To smoothly transport dehydrated sludge to an incinerator, etc., by providing a sludge transporting main pipe for collecting plural drain pipes and connecting the pipes at the initial and intermediate points, a header connected to the plural sludge transporting main pipes and extending to the incinerator, etc. CONSTITUTION:A specified time schedule is assigned to operate a controller 300, a solenoid valve 310 corresponding to the operation is opened, and compressed air is blown in from the corresponding ejector 140. A pressurizing device 100 for the dehydrator of the corresponding group is simultaneously opened, and dehydrated sludge is sent to a sludge collecting main pipe 130 through a check valve 110 and a discharge and feed pipe 120. The dehydrated sludge in the main pipe 130 forms a concd. plug flow by the compressed air continuously blown in from the ejector 140, smoothly flows downward in the header and is transported to an incinerator through a header 160.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、例えば、下水処理場などにおいて脱水機から
生成する脱水汚泥を遠隔地の焼却炉等へ運搬する管路圧
送システムに関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a pipe pumping system for transporting dehydrated sludge produced from a dehydrator in a sewage treatment plant or the like to a remote incinerator or the like.

[従来の技術] 従来、下水処理場では、10〜数10個の各々の脱水機
で脱水された下水汚泥(脱水汚泥)は次工程の焼却炉等
で焼却されるが、その際工場立地の関係から必ずしも脱
水機と焼却炉とが近接しておらず、脱水機とはかなり離
れた遠隔地に焼却炉が設備され、この間の輸送は一般的
にはベルトコンベヤを組合わせて使用されていた。
[Conventional technology] Conventionally, in sewage treatment plants, the sewage sludge (dehydrated sludge) dehydrated by 10 to several dozen dehydrators is incinerated in the next process, such as an incinerator. Due to this, the dehydrator and incinerator were not necessarily located close to each other, and the incinerator was installed in a remote location quite far away from the dehydrator, and transport between them was generally carried out using a combination of belt conveyors. .

第3図はこの1例を示すベルトコンベヤ配置系統図であ
り、この従来例では、脱水機LA。
FIG. 3 is a belt conveyor layout system diagram showing one example of this, and in this conventional example, the dewatering machine LA.

IB、IC,IDの脱水汚泥をベルトコンベヤ20によ
りシュートlOへ集結し、同様に2A。
The dehydrated sludge from IB, IC, and ID is collected on the chute IO by the belt conveyor 20, and similarly, the sludge is transferred to the chute 2A.

2B、2C,2Dの脱水機群、3A〜3Dの脱水機群、
4A〜4Dの脱水機群の汚泥もシュート10へ連結され
、これらシュート10.10を連結するベルトコンベヤ
30で集合した後、ベルトコンベヤ30の終端でベルト
コンベヤ40およびベルトコンベヤ50へ連結して遠隔
地の焼却炉60へ脱水汚泥を輸送していた。
2B, 2C, 2D dehydrator groups, 3A to 3D dehydrator groups,
The sludge from the dehydrator groups 4A to 4D is also connected to the chute 10, collected on the belt conveyor 30 that connects these chutes 10 and 10, and then connected to the belt conveyor 40 and belt conveyor 50 at the end of the belt conveyor 30 to be transported remotely. Dehydrated sludge was being transported to incinerator 60 on the ground.

[発明が解決しようとする課題] しかしながら、脱水汚泥をベルトコンベヤを使用して輸
送する場合には、たとえばベルトコンベヤにカバーを設
けても臭気は外部に漏れ、処理場内はもとより処理場周
辺の住宅地の生活環境を破壊するばかりでなく、処理場
内は汚染し、周囲を清潔に保持するために多大の労力と
費用を発生させていた等の問題があった。
[Problems to be Solved by the Invention] However, when dehydrated sludge is transported using a belt conveyor, for example, even if a cover is provided on the belt conveyor, the odor leaks to the outside, causing not only the inside of the treatment plant but also the residences around the treatment plant. There were problems such as not only destroying the local living environment, but also contaminating the inside of the treatment plant and incurring a great deal of labor and expense to keep the surrounding area clean.

また、複数の脱水機から出る脱水汚泥を効率良く、より
少ないベルトコンベヤで目的地まで輸送するために、例
えば、第3図に示す実施例のようなベルトコンベヤの配
列を採用すると、連続運転をする場合、ベルトコンベヤ
30はベルトコンベヤ20の輸送能力の4倍(脱水機能
力の8倍)とし、ベルトコンベヤ40およびベルトコン
ベヤ50の最大輸送能力はベルトコンベヤ3002倍(
脱水機能力の16倍)としなければならず、ベルトコン
ベヤの設備費は過大となる。一方、脱水機の運転はある
程度間欠運転できることを考慮し、ベルトコンベヤも間
欠運転を採用して輸送能力の小さなベルトコンベヤを採
用しようとすると、各脱水機の吐出量に対してベルトコ
ンベヤの運転停止をその輸送能力以内で制御することは
非常に複雑で困難であり実現性が乏しかった。
In addition, in order to efficiently transport dehydrated sludge from multiple dehydrators to the destination using fewer belt conveyors, for example, if a belt conveyor arrangement such as the embodiment shown in Fig. 3 is adopted, continuous operation can be achieved. In this case, the belt conveyor 30 is 4 times the transport capacity of the belt conveyor 20 (8 times the dewatering function), and the maximum transport capacity of the belt conveyor 40 and the belt conveyor 50 is 3002 times the belt conveyor (8 times the dehydration function).
16 times the dewatering function), and the equipment cost for the belt conveyor becomes excessive. On the other hand, considering that the dewatering machine can be operated intermittently to some extent, if we try to adopt intermittent operation of the belt conveyor and use a belt conveyor with a small transport capacity, the operation of the belt conveyor will stop for the discharge amount of each dehydrator. It has been extremely complex and difficult to control the transport capacity within its transport capacity, and has little practicality.

[課題を解決するための手段〕 以上の課題を同時に解決するために、本発明の装置にお
いては、 複数個の脱水機で得られた脱水汚泥を集合して該脱水機
から離れた次工程の焼却炉等へ運搬する移送手段であっ
て、該脱水機の吐出側に加圧装置および排送管を備え、
複数の該排送管を集合して始点および中間点において連
結する送泥母管を設けるとともに、複数の該送泥母管と
連結され、かつ、該焼却炉等へ延在する集合母管を配設
し、前記送泥母管の始点の直後に送泥母管内に圧縮エア
を送入するエジェクタを設け、かつ、前記送泥母管の中
間点の直前に逆止弁を設け、該各エジェクタに圧縮エア
を供給する電磁開閉弁および該itga開閉弁の連通遮
断を制御する制御装置を備えた脱水汚泥の管路圧送シス
テムを構成したものである。
[Means for Solving the Problems] In order to simultaneously solve the above problems, the apparatus of the present invention collects dehydrated sludge obtained from a plurality of dehydrators and transfers it to the next process separated from the dehydrators. A transfer means for transporting to an incinerator or the like, comprising a pressurizing device and a discharge pipe on the discharge side of the dehydrator,
A slurry main pipe is provided that collects a plurality of the discharge pipes and connects them at a starting point and an intermediate point, and a collecting main pipe that is connected to the plurality of mud transport pipes and extends to the incinerator, etc. an ejector for feeding compressed air into the slurry main pipe immediately after the starting point of the slurry main pipe, and a check valve immediately before the intermediate point of the slurry main pipe; This is a dehydrated sludge pipe pumping system that is equipped with an electromagnetic on-off valve that supplies compressed air to an ejector and a control device that controls communication and cutoff of the itga on-off valve.

[作用] 本発明の管路圧送システムでは、脱水機で脱水された脱
水汚泥は加圧装置で加圧されて排送管を経由して集泥母
管へ移送され、エジェクタを介して吹込まれる圧縮エア
によって集泥母管内をプラグフロー(栓流)となって流
れ、集合母管を通過し最終の目的地の焼却炉等へ円滑に
輸送される。
[Function] In the pipe pressure feeding system of the present invention, the dehydrated sludge dehydrated by the dehydrator is pressurized by the pressurizing device, transferred to the sludge collection main pipe via the discharge pipe, and blown through the ejector. The compressed air flows through the collecting main pipe as a plug flow, passes through the collecting main pipe, and is smoothly transported to the final destination, such as an incinerator.

この間、各群の脱水機のうち、運転するものと運転しな
いものを時間的にプログラム化された運転指令に基づい
て各エジェクタに圧縮エアを供給する圧気配管に設けら
れた電磁開閉器を制御装置からの電気信号によって開閉
操作する。
During this time, a control device controls the electromagnetic switches installed in the pressure piping that supplies compressed air to each ejector based on the time-programmed operation commands to determine which dehydrators in each group are to be operated and which ones are not to be operated. Opening and closing operations are performed by electrical signals from the

[実施例] 以下、図に示す実施例を用いて本発明の詳細な説明する
[Example] Hereinafter, the present invention will be described in detail using examples shown in the drawings.

第1図は本発明に係る管路圧送システムの配置系統図で
ある。第2図はエジェクタ用の電磁開閉弁の開閉制御の
タイムスケジュールを示す運転指令図である。
FIG. 1 is a layout diagram of a pipe pressure feeding system according to the present invention. FIG. 2 is an operation command diagram showing a time schedule for controlling the opening and closing of the electromagnetic on-off valve for the ejector.

第1図において、LA、IB、IC,IDは1群の脱水
機を示し、同様に2A〜2D、3A〜3D、4A〜4D
は各々の群れの脱水機である。
In Fig. 1, LA, IB, IC, and ID indicate one group of dehydrators, and similarly 2A to 2D, 3A to 3D, 4A to 4D.
is the dehydrator of each flock.

100は加圧装置で、たとえば遠心ポンプや往復動(レ
シプロ)ポンプなどの圧送ポンプやスクイズポンプなど
を使用する。120は排送管で、排送管の途中には逆止
弁110を設ける。1群の排送管120は1点に集結し
、これに連結して集泥母管130が設けられ、集泥母管
130の始点の直後には圧縮空気供給設備(たとえばコ
ンプレッサ)200から電磁開閉弁310を経由して圧
縮エアを集泥母管130へ供給するためのエジェクタ1
40が輸送方向斜めに傾斜して設けられる。
Reference numeral 100 denotes a pressurizing device, which uses, for example, a pressure pump such as a centrifugal pump or a reciprocating pump, or a squeeze pump. 120 is a discharge pipe, and a check valve 110 is provided in the middle of the discharge pipe. One group of discharge pipes 120 converge at one point, and a mud collecting main pipe 130 is provided connected to this, and immediately after the starting point of the mud collecting main pipe 130, an electromagnetic air is supplied from compressed air supply equipment (for example, a compressor) 200. Ejector 1 for supplying compressed air to mud collection main pipe 130 via on-off valve 310
40 is provided obliquely in the transportation direction.

また集泥母管130の中間には適宜他の群の排送管12
0が集結され、合流点の直前に逆止弁150、合流点の
直後にエジェクタ140が設けられる。このように配設
された複数の集泥母管130はさらに合流し、以後集合
母管160として焼却炉60へ連結される。この合流点
直前の集泥母管130にも逆止弁150が設けられる。
In addition, in the middle of the mud collection main pipe 130, there are other groups of discharge pipes 12 as appropriate.
A check valve 150 is provided immediately before the merging point, and an ejector 140 is provided immediately after the merging point. The plurality of mud collecting main pipes 130 arranged in this manner are further merged together, and thereafter connected to the incinerator 60 as a collecting main pipe 160. A check valve 150 is also provided in the mud collecting main pipe 130 immediately before this confluence point.

なお、300は電磁開閉弁310の開閉を制御する制御
装置である。
Note that 300 is a control device that controls opening and closing of the electromagnetic on-off valve 310.

このようにして、第1図の実施例では4個(1群)X4
群=16個の脱水機を2本の集泥母管130と1本の集
合母管140とからなる管路によって連結された本発明
の管路輸送システムの作動について説明する。
In this way, in the embodiment shown in FIG.
The operation of the pipeline transportation system of the present invention in which a group of 16 dehydrators are connected by a pipeline consisting of two mud collecting main pipes 130 and one collecting main pipe 140 will be described.

まず、複数の群に分類された脱水機100、すなわち1
群(IA、IB、IC,ID)、2群。
First, the dehydrators 100 classified into a plurality of groups, that is, 1
Group (IA, IB, IC, ID), Group 2.

3群、4群のうち、たとえば、第2図に示すように1群
と3群を同時に運転休止し、それとは反対に2群と4群
とを上記1群および3群とは反対に休止運転するような
タイムスケジュールを指定して制御装置300を操作し
、そのときに運転に対応する電磁開閉弁310を開状態
にして対応するエジェクタ140から圧縮エアを吹込む
。同時に、運転に対応する群の脱水機の加圧装置100
を運転状態にすると、脱水汚泥は逆止弁110を経由し
て排送管120を押圧されて流れ、集泥母管130へ到
る。集泥母管130に入った脱水汚泥はエジェクタ14
0より連続して吹込まれる圧縮空気によって高濃度状態
のプラグフロー(栓流)を形成して集泥母管中を円滑に
下流へ向けて流れ、その後集合母管140を経由して焼
却炉へ運搬される。
Of the 3rd and 4th groups, for example, as shown in Fig. 2, the 1st and 3rd groups are stopped at the same time, and on the contrary, the 2nd and 4th groups are stopped in the opposite manner to the 1st and 3rd groups. The control device 300 is operated by specifying a time schedule for the operation, and at that time, the electromagnetic on-off valve 310 corresponding to the operation is opened and compressed air is blown from the corresponding ejector 140. At the same time, the pressurizing device 100 of the group of dehydrators corresponding to the operation
When the sludge is put into operation, the dehydrated sludge is forced to flow through the discharge pipe 120 via the check valve 110 and reaches the sludge collecting main pipe 130. The dehydrated sludge that has entered the sludge collection main pipe 130 is transferred to the ejector 14
The compressed air that is continuously blown in from zero forms a highly concentrated plug flow that smoothly flows downstream through the collecting main pipe 140 and then to the incinerator via the collecting main pipe 140. transported to.

このようにして一定時間経過して、所定の運転時間(た
とえば時刻t1〜t2間の時間)が終ると、開状態の電
磁弁310は閉となり、それに代って今まで閉状態の電
磁弁310は開状態となり、今まで休止していた群、た
とえば2群と4群が作動し、1群と3群の脱水機の加圧
装置100とエジェクタ140の作動は休止する間に2
群ならびに4群の脱水機の脱水汚泥が前述と同様に目的
地へ移送される。2群および4群が運転されている間2
群および4群のエジェクタ140からの圧縮エアは中間
点の直前に配設された逆止弁150によって逆流が防止
される。また、集合母管160の直前の、集泥母管13
0終端に設けた逆止弁150は集泥母管130の下流へ
流れる圧縮エアおよびそれに随伴する脱水汚泥が他の集
泥母管130へ逆流しないためのものである。
After a certain period of time has elapsed in this manner, and a predetermined operating time (for example, the time between times t1 and t2) ends, the solenoid valve 310 that has been in the open state is closed, and instead of the solenoid valve 310 that has been in the closed state until now. is in the open state, groups that have been inactive, for example, groups 2 and 4, are activated, and the pressurizing devices 100 and ejectors 140 of the dehydrators of groups 1 and 3 are stopped while they are inactive.
The dewatered sludge from the dehydrators of the group and the group 4 is transferred to the destination in the same manner as described above. 2 while the 2nd and 4th groups are running
Compressed air from the group and fourth group ejectors 140 is prevented from flowing back by a check valve 150 disposed just before the intermediate point. In addition, the mud collecting main pipe 13 immediately before the collecting main pipe 160
The check valve 150 provided at the 0 end is to prevent the compressed air flowing downstream of the sludge collecting main pipe 130 and the accompanying dewatered sludge from flowing back into the other sludge collecting main pipe 130.

以上説明したように、本実施例のように交互に間欠運転
を繰返すタイムスケジュールによった輸送計画に基づい
て輸送することにより、集泥母管130の輸送能力は排
送管120の輸送能力の4倍強で十分であり、従来のベ
ルトコンベヤ連続運転の場合のように脱水機の能力の8
倍とする必要はないので設備費は大幅に下がる。
As explained above, by transporting based on a transport plan based on a time schedule that alternately repeats intermittent operation as in this embodiment, the transport capacity of the mud collecting main pipe 130 is equal to or greater than that of the discharge pipe 120. A little more than 4 times the capacity is sufficient, and 8 times the capacity of the dewatering machine is
Since there is no need to double the amount, equipment costs are significantly reduced.

[発明の効果] 以上述べたように、本発明の管路圧送システムによれば
、脱水汚泥を高濃度で圧送できるばかりでなく、悪臭を
発生させることもなく機器設置個所を汚染することもな
く、極めて良好な作業環境を保持できるばかりでな(、
間欠運転の完全自動化を通じて能率良(輸送できるうえ
、従来のベルトコンベヤシステムに比べて設備費が大幅
に低減できる。
[Effects of the Invention] As described above, according to the pipe pressure feeding system of the present invention, not only can dehydrated sludge be pumped at a high concentration, but also it does not generate bad odor or contaminate the equipment installation location. , not only can we maintain an extremely good working environment (,
Fully automated intermittent operation allows efficient transportation, and equipment costs are significantly lower than traditional belt conveyor systems.

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

第1図〜第2図は本発明の実施例に係り、第1図は管路
圧送システムの配置系統図、第2図はエジェクタ用の電
磁開閉弁の開閉制御タイムスケジュールを示す運転指令
図、第3図は従来のベルトコンベヤ配置系統図である。 IA、IB、IC,LD・・・脱水機、2A、2B、2
C,2D・・・脱水機、3A、3B、3C,3D・・・
脱水機、4A、4B、4C,4,D・・・脱水機、10
・・・シュート、 20.30,40,50.・・・ベルトコンベヤ、60
・・・焼却炉、   100・・・加圧装置、110・
・・逆止弁、   120・・・排送管、130・・・
集泥母管、  140・・・エジェクタ、150・・・
逆止弁、   160・・集合母管、200・・・圧縮
エア供給設備、 300・・・制御装置、 310・・電磁開閉弁。 第2図
1 and 2 relate to an embodiment of the present invention, in which FIG. 1 is a layout diagram of a pipe pressure feeding system, FIG. 2 is an operation command diagram showing an opening/closing control time schedule of an electromagnetic on-off valve for an ejector, FIG. 3 is a conventional belt conveyor layout system diagram. IA, IB, IC, LD...Dehydrator, 2A, 2B, 2
C, 2D... dehydrator, 3A, 3B, 3C, 3D...
Dehydrator, 4A, 4B, 4C, 4, D...Dehydrator, 10
...Shoot, 20.30,40,50. ...belt conveyor, 60
... Incinerator, 100 ... Pressure device, 110.
...Check valve, 120...Discharge pipe, 130...
Sludge collecting main pipe, 140... Ejector, 150...
Check valve, 160...Collecting main pipe, 200...Compressed air supply equipment, 300...Control device, 310...Solenoid opening/closing valve. Figure 2

Claims (1)

【特許請求の範囲】[Claims] (1)複数個の脱水機で得られた脱水汚泥を集合して該
脱水機から離れた次工程の焼却炉等へ運搬する移送手段
であって、 該脱水機の吐出側に加圧装置および排送管を備え、 複数の該排送管を集合して始点および中間点において連
結する送泥母管を設けるとともに、複数の該送泥母管と
連結され、かつ、該焼却炉等へ延在する集合母管を配設
し、 前記送泥母管の始点の直後に送泥母管内に圧縮エアを送
入するエジェクタを設け、かつ、前記送泥母管の中間点
の直前に逆止弁を設け、 該各エジェクタに圧縮エアを供給する電磁開閉弁および
該電磁開閉弁の連通遮断を制御する制御装置を備えた 脱水汚泥の管路圧送システム。
(1) A transfer means for collecting dehydrated sludge obtained from a plurality of dehydrators and transporting it to the next process, such as an incinerator, separated from the dehydrators, which includes a pressurizing device and a pressure device on the discharge side of the dehydrators. A slurry transport pipe is provided, which is equipped with a discharge pipe, and connects a plurality of the discharge pipes together at a starting point and an intermediate point, and is connected to the plurality of mud transport pipes and extends to the incinerator, etc. An ejector for feeding compressed air into the slurry main pipe is installed immediately after the starting point of the slurry main pipe, and a back check is provided immediately before the intermediate point of the slurry main pipe. A dehydrated sludge pipe pressure feeding system comprising a valve, an electromagnetic on-off valve that supplies compressed air to each ejector, and a control device that controls communication and cutoff of the electromagnetic on-off valve.
JP11175990A 1990-05-01 1990-05-01 System for transporting dehydrated sludge under pressure through pipeline Pending JPH0412000A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11175990A JPH0412000A (en) 1990-05-01 1990-05-01 System for transporting dehydrated sludge under pressure through pipeline

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11175990A JPH0412000A (en) 1990-05-01 1990-05-01 System for transporting dehydrated sludge under pressure through pipeline

Publications (1)

Publication Number Publication Date
JPH0412000A true JPH0412000A (en) 1992-01-16

Family

ID=14569472

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11175990A Pending JPH0412000A (en) 1990-05-01 1990-05-01 System for transporting dehydrated sludge under pressure through pipeline

Country Status (1)

Country Link
JP (1) JPH0412000A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6251877B1 (en) * 1998-03-24 2001-06-26 Pacific Corporation Composition for external application containing a β-1,6-branched-β-1,3-glucan

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6251877B1 (en) * 1998-03-24 2001-06-26 Pacific Corporation Composition for external application containing a β-1,6-branched-β-1,3-glucan

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