JPH0632405A - Waste transporting method by using pipeline - Google Patents

Waste transporting method by using pipeline

Info

Publication number
JPH0632405A
JPH0632405A JP20858192A JP20858192A JPH0632405A JP H0632405 A JPH0632405 A JP H0632405A JP 20858192 A JP20858192 A JP 20858192A JP 20858192 A JP20858192 A JP 20858192A JP H0632405 A JPH0632405 A JP H0632405A
Authority
JP
Japan
Prior art keywords
pipe
waste water
pipeline
water
waste
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
Application number
JP20858192A
Other languages
Japanese (ja)
Other versions
JP3077072B2 (en
Inventor
Kazutaro Oyabu
和太郎 大薮
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.)
Sanki Engineering Co Ltd
Original Assignee
Sanki Engineering 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 Sanki Engineering Co Ltd filed Critical Sanki Engineering Co Ltd
Priority to JP04208581A priority Critical patent/JP3077072B2/en
Publication of JPH0632405A publication Critical patent/JPH0632405A/en
Application granted granted Critical
Publication of JP3077072B2 publication Critical patent/JP3077072B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Refuse Collection And Transfer (AREA)
  • Air Transport Of Granular Materials (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To forcibly send sedimented solid matter under pressure, without generating any choke, by putting ball-shaped elastic bodies into a double pipeline having an inside pipe comprising many pores and a filtration film. CONSTITUTION:Waste water 50 containing wastes is transported through a pipeline formed of a double pipe, in which a space is made between the inside pipe and the outside pipe, and the inside pipe comprises many pores and a filtration film. In this case, every time a definite quantity of the waste water 50 is pressed in a pipeline from its one end 25, ball-shaped elastic bodies 51 whose diameters are almost the same as the inside diameter of the inside pipe, are forced into the inside pipe so as to transport the waste water 50 as being partitioned by the ball-shaped elastic bodies 51. Gas generated in the process of movement of the waste water 50 is discharged as exhaust gas 17, and permeated water is also discharged as drainage 16. On the other hand, if frictional resistance of the waste water 50 against the inner wall of the pipe increases, pressurized water 15 is injected. Moreover, an ordinary pipe 30 is wound with a heating coil 35 or a cooling coil 36 for promoting fermentation of the waste water 50 or preventing its overheat, if necessary. In this way, the waste water 50 is dewatered and taken out as a solid matter from an exhaust pipe 31, finally.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】一般ゴミや汚水等の廃棄物を焼却
場等の処理施設へ輸送する方法に関する。
[Industrial field of application] The present invention relates to a method of transporting waste such as general waste and sewage to a treatment facility such as an incinerator.

【0002】[0002]

【従来の技術】一般ゴミと呼ばれる廃棄物は材質が不均
等であり水分含有率も不同であるから管路輸送するには
特別な手段が必要である。その一手段として発明者はさ
きに特願昭3−275003において図3及び図4の方
法を提案した。すなわち、図3の2重管を用いて図4の
管路を構成し、ホッパ20に投入した廃棄物と水の混合流
体をスラリ−ポンプ28のプランジャ動作及びこれと同期
した仕切り弁21、24の交番開閉によって排出管31まで圧
送する。図3は2重管の構造で、内側管は多数の小孔を
有する支持壁1、耐圧壁2及びこれらに狭まれた濾過膜
3から構成される。内側管の外側には空隙9を距てて外
側管4があり、該外側管の下面には加圧水15の注入口
5、透過水16の排水口6を備え、上面には透過ガス17の
排気口7が備えられている。なお、濾過膜3と支持壁1
を一体としたセラミック製濾過膜とすることも可能であ
る。
2. Description of the Related Art Since waste materials called general waste are made of uneven materials and have different water contents, a special means is required for transporting them by pipeline. As one of the means, the inventor previously proposed the method of FIGS. 3 and 4 in Japanese Patent Application No. 3-275003. That is, the double pipe of FIG. 3 is used to form the pipe line of FIG. 4, and the mixed fluid of the waste and water put into the hopper 20 is operated by the plunger of the slurry pump 28 and the sluice valves 21, 24 synchronized therewith. It is pressure-fed to the discharge pipe 31 by alternating opening and closing. FIG. 3 shows a double tube structure, and the inner tube is composed of a support wall 1 having a large number of small holes, a pressure resistant wall 2 and a filtration membrane 3 sandwiched between these. An outer tube 4 is provided outside the inner tube with a gap 9 in between, an inlet 5 for pressurized water 15 and a drain 6 for permeated water 16 are provided on the lower surface of the outer tube, and a permeated gas 17 is exhausted on the upper surface. A mouth 7 is provided. The filtration membrane 3 and the support wall 1
It is also possible to make a ceramic filtration membrane that is integrated with the above.

【0003】濾過膜3は高圧側から低圧側へガスや水分
を透過するが、高分子材料やコロイド粒子は透過しな
い。したがって、内側管の内部流体の圧力よりも空隙9
の圧力を低くすることによって流体中の水分やガスを内
側管の小孔を通して透過させ、図1(c)のように空隙
9に貯溜する。この貯溜により空隙内圧力が上昇すると
排水口6から排水して空隙内圧力を低下させるから、管
内流体の含有水分は濾過膜3を通って空隙9へ透過し続
ける。
The filter membrane 3 permeates gas and moisture from the high pressure side to the low pressure side, but does not permeate polymer materials and colloid particles. Therefore, the pressure in the inner tube is higher than the pressure of the fluid in the inner tube.
By lowering the pressure of 1, the water and gas in the fluid are permeated through the small holes of the inner tube and stored in the void 9 as shown in FIG. 1 (c). When the pressure in the void rises due to this storage, the pressure in the void is reduced by draining from the drain port 6, so that the water content of the pipe fluid continues to permeate into the void 9 through the filtration membrane 3.

【0004】また、廃棄物の発酵により発生したガスは
空隙9の上部に集まるが、液面13が一定水準以下になる
と液面検出器12が作動して排気口7から排気する。排気
すると空隙内圧力が低下し過ぎるので排水口6及び排気
口7を閉塞した状態で注水口5から加圧水15を注入し、
空隙内圧力と内側管内圧力との差を常に一定に保つので
ある。
Further, the gas generated by the fermentation of the waste is collected in the upper part of the void 9, but when the liquid level 13 falls below a certain level, the liquid level detector 12 is activated and exhausted from the exhaust port 7. When exhausted, the pressure in the void drops too much, so pressurized water 15 is injected from the water injection port 5 with the drain port 6 and the exhaust port 7 closed.
The difference between the pressure in the void and the pressure in the inner pipe is always kept constant.

【0005】さらに、すべての2重管には下流側フラン
ジ近傍に内側管内流体の圧力を計測する圧力計11が取付
けられており、隣接する上流側2重管の管内圧力よりも
一定値以上に低下したならば管内圧力よりも高い圧力の
加圧水15を管内流体へ注入し、その潤滑作用によって管
壁との摩擦による圧力損失を低滅する。
Further, a pressure gauge 11 for measuring the pressure of the fluid in the inner pipe is attached to each of the double pipes in the vicinity of the downstream side flange so that the pressure in the pipe becomes equal to or more than a certain value than the pressure in the adjacent upstream double pipe. If it decreases, the pressurized water 15 having a pressure higher than the pipe pressure is injected into the pipe fluid, and the lubrication action reduces the pressure loss due to friction with the pipe wall.

【0006】図4の管路にある通常管30には加熱コイル
35または冷却コイル36が設けられ、管内流体の温度を上
昇して発酵を促進し、または発酵により過熱した流体を
冷却する。
A heating coil is provided in the normal pipe 30 in the conduit of FIG.
35 or a cooling coil 36 is provided to raise the temperature of the fluid in the tube to accelerate the fermentation or cool the fluid that has been overheated by the fermentation.

【0007】これによって、不均質な一般ゴミでも管路
に詰まりを生じさせず、かつ騒音や臭気の発生が少な
く、しかも後工程で処理しやすい状態で排出することが
できる、というものである。
As a result, even non-homogeneous general dust can be discharged without causing clogging of the pipeline, generation of noise and odor, and easy handling in the subsequent process.

【0008】[0008]

【発明が解決しようとする課題】水分含有率の低い一般
ゴミにあっては、ポッパ20へ投入する際に水を混入する
ことによって図3及び図4の管路を長距離輸送すること
ができるが、液体成分の多い汚水を輸送すると、管内移
動中に固体成分が沈澱するため管壁との摩擦抵抗の小さ
い液体成分が優先的に移動し、滞留した沈澱固形物が堆
積して遂には管の詰まりを生ずる恐れがある。
For general waste having a low water content, it is possible to transport long distances through the pipelines of FIGS. 3 and 4 by mixing water when throwing it into the popper 20. However, when sewage containing a large amount of liquid components is transported, the solid components precipitate during the movement within the pipe, so the liquid components with low frictional resistance with the pipe wall preferentially move, and the accumulated solid precipitate accumulates, eventually There is a risk of clogging.

【0009】[0009]

【課題を解決するための手段】液体成分の多い汚水を管
路輸送するには沈澱した固体成分を滞留堆積させること
なく強制的に移動させることが必要である。そのための
手段として本発明では、内側管と外側管の間に空隙を設
けかつ内側管に多数の小孔及び濾過膜を形成した2重管
を用いて構成した管路内で廃棄物を含む混合流体を輸送
する方法において、該管路の一端より一定量の混合流体
を圧入するごとにほぼ内側管内径に等しい直径の球状弾
性体を圧入し、該球状弾性体に仕切られた状態で混合流
体を搬送するようにした。
In order to transport wastewater containing a large amount of liquid components by pipe, it is necessary to forcibly move the precipitated solid components without accumulating them. As a means for this, in the present invention, a mixture containing waste is contained in a pipe line formed by using a double pipe in which a gap is provided between the inner pipe and the outer pipe and a large number of small holes and a filtration membrane are formed in the inner pipe. In the method of transporting a fluid, a spherical elastic body having a diameter substantially equal to the inner diameter of the inner pipe is press-fitted every time a fixed amount of the mixed fluid is press-fitted from one end of the pipe, and the mixed fluid is partitioned in the spherical elastic body. To be transported.

【0010】また、廃棄物の発酵を促し又は発酵に伴う
過熱を防ぐため、管路の一部を形成する管体の外周を加
熱し、又は冷却するようにした。
Further, in order to promote the fermentation of the waste or prevent the overheating associated with the fermentation, the outer circumference of the pipe forming a part of the pipe is heated or cooled.

【0011】[0011]

【実施例】以下、添付の図面により本発明の実施例を具
体的に説明する。図1は図4の廃棄物投入用ホッパ20に
代わる汚水及び球状弾性体の投入機構で、スラリ−ポン
プのプランジャ23が作動するシリンダ22には搬送流体を
導入するための管が垂直方向に分岐しているが、該管は
仕切り弁21の上方でさらに2方向に分岐し、一方の管52
からは開閉弁54を経て汚水50が導入され、他方の管から
はホッパ53から球状弾性体51が開閉弁55を経て1ヶずつ
落下投入される。また、シリンダ22には仕切り弁24を介
して吐出管25が接続される。
Embodiments of the present invention will be specifically described below with reference to the accompanying drawings. FIG. 1 is a mechanism for introducing waste water and a spherical elastic body in place of the waste input hopper 20 of FIG. 4, and a pipe for introducing a carrier fluid is vertically branched into a cylinder 22 in which a plunger 23 of a slurry pump operates. However, the pipe branches into two directions above the sluice valve 21, and one pipe 52
Waste water 50 is introduced through the open / close valve 54, and spherical elastic bodies 51 are dropped from the hopper 53 through the open / close valve 55 one by one from the other pipe. A discharge pipe 25 is connected to the cylinder 22 via a sluice valve 24.

【0012】汚水の圧送に際しては、まず、仕切り弁24
を閉じ仕切り弁21を開いた状態でプランジャ23を左へ引
き込むと同時に開閉弁55を開いてホッパ53から球状弾性
体51を1ヶだけシリンダ室へ落下させ、直ちに開閉弁55
を閉じると共に開閉弁54を開き管52から汚水50をシリン
ダ室へ導入する。プランジャ23を最も左へ引き込んだ状
態では図1のように、シリンダ室が汚水で満たされ、プ
ランジャ23に直面して球状弾性体51が1ヶ存在すること
になる。そこで仕切り弁21を閉じ仕切り弁24を開いてプ
ランジャ23を右方へ駆動すれば、シリンダ室の汚水は吐
出管25へ圧送されるのである。なお、球状弾性体は必ず
しもプランジャ動作の1行程ごとに投入するのではな
く、例えば汚水5m3 ごとに1ヶを投入すればよい。
When pumping sewage, first the sluice valve 24
With the sluice valve 21 open and the plunger 23 pulled to the left, the opening / closing valve 55 is opened at the same time, and only one spherical elastic body 51 is dropped from the hopper 53 into the cylinder chamber.
Is closed and the opening / closing valve 54 is opened to introduce the dirty water 50 into the cylinder chamber through the pipe 52. When the plunger 23 is pulled to the leftmost, as shown in FIG. 1, the cylinder chamber is filled with dirty water, and one spherical elastic body 51 exists facing the plunger 23. Therefore, when the partition valve 21 is closed and the partition valve 24 is opened to drive the plunger 23 to the right, the dirty water in the cylinder chamber is pumped to the discharge pipe 25. It should be noted that the spherical elastic body is not necessarily charged every one stroke of the plunger operation, but one may be charged for every 5 m3 of sewage.

【0013】圧送された汚水は、図2において吐出管25
から右へ通常管30や多数の2重管を通って終端の排出管
31へ達するが、その途中の過程について、模式的に示し
た2重管の縦断面図により説明する。球状弾性体は合成
ゴムのように耐圧かつ耐薬品性で弾性のある材質で作ら
れ、かつ管路の内径とほぼ同じ直径を有するので、圧送
される過程では管の内壁に密接しながら移動する。した
がって、汚水は球状弾性体によって区間に仕切られた状
態となって移動し、隣接する区間の汚水と混合すること
がない。汚水中の固体成分は管の下方に沈澱するが、球
状弾性体51は沈澱固形物を滞留させることなく移動させ
るので、常に管内壁を清掃しながら圧送することにな
る。また、汚水が移動する過程で発生したガスは排気17
として排出し、透過した水分は排水16として排出する一
方、管内壁との摩擦抵抗が増して圧力損失が過大になる
と加圧水15を管内壁に注入して圧送を円滑ならしめるの
は図3、図4と同様である。
The sewage sent under pressure is discharged from the discharge pipe 25 in FIG.
To the right through the normal pipe 30 and a number of double pipes and the end discharge pipe
Although it reaches 31, the process in the middle will be described with reference to a schematic vertical sectional view of the double pipe. The spherical elastic body is made of an elastic material such as synthetic rubber that is pressure-resistant, chemical-resistant, and has the same diameter as the inner diameter of the pipeline, so it moves while closely contacting the inner wall of the pipe during the process of being pumped. . Therefore, the sewage does not mix with the sewage in the adjacent section because it moves while being divided into sections by the spherical elastic body. The solid component in the wastewater precipitates below the pipe, but the spherical elastic body 51 moves the precipitated solid without causing it to stay, so that the inner wall of the pipe is constantly pumped. In addition, the gas generated in the process of moving sewage is exhausted.
As shown in FIG. 3 and FIG. The same as 4.

【0014】さらに、通常管30の外周には加熱コイル35
または冷却コイル36が巻かれ、必要に応じて汚水の発酵
を促進するために加熱し、または発酵による過熱を防ぐ
ために冷却する。
Further, a heating coil 35 is provided on the outer circumference of the normal tube 30.
Alternatively, a cooling coil 36 is wound, and is heated to accelerate fermentation of waste water or cooled to prevent overheating due to fermentation, if necessary.

【0015】このように、汚水50は移動と共に水分が除
去され、容積が減少するので球状弾性体51の間隔は次第
に短縮し、最終的には球状弾性体に狭まれて脱水状態と
なった固形分が取り出される。
As described above, the sewage 50 is removed of water as it moves, and the volume thereof is reduced, so that the interval between the spherical elastic bodies 51 is gradually shortened, and finally the solid bodies are narrowed to the spherical elastic bodies and are in a dehydrated state. Minutes are taken out.

【0016】[0016]

【発明の効果】以上のごとく、多数の小孔と濾過膜で形
成した内側管を有する2重管で管路を構成し、一定量の
汚水を投入するごとに、ほぼ内側管内径と等しい直径の
球状弾性体を投入すれば、沈澱固形物の滞留がなく管に
詰まりを生じないので円滑に汚水を搬送することが可能
で、しかも処理の容易な乾燥状態で取り出すことができ
る。
As described above, the pipe line is constituted by a double pipe having an inner pipe formed of a large number of small holes and a filtration membrane, and every time a fixed amount of waste water is introduced, the diameter is almost equal to the inner diameter of the inner pipe. When the spherical elastic body is added, the precipitated solid matter does not stay and the pipe is not clogged, so that the sewage can be transported smoothly and can be taken out in a dry state which is easy to process.

【図面の詳細な説明】[Detailed Description of Drawings]

【図1】本発明に係わる汚水及び球状弾性体の投入機構
の説明図。
FIG. 1 is an explanatory view of a charging mechanism for sewage and a spherical elastic body according to the present invention.

【図2】本発明に係わる球状弾性体の作用を模範的に示
す2重管の縦断面図。
FIG. 2 is a vertical cross-sectional view of a double tube exemplarily showing the action of the spherical elastic body according to the present invention.

【図3】従来方法における2重管の構造を示す図面。FIG. 3 is a view showing a structure of a double pipe in a conventional method.

【図4】従来方法における2重管を用いた管路を示す図
面。
FIG. 4 is a drawing showing a pipe line using a double pipe in a conventional method.

【符号の説明】[Explanation of symbols]

1 支持壁 2 耐圧壁 3 濾過膜 4 外側管 5 加圧水注入口 6 排水口 7 排気口 11 圧力計 12 液面検出器 21 仕切り弁 22 シリンダ 23 プランジャ 24 仕切り弁 35 加熱コイル 36 冷却コイル 50 汚水 51 球状弾性体 54 開閉弁 55 開閉弁 1 Support Wall 2 Pressure-Resistant Wall 3 Filter Membrane 4 Outer Tube 5 Pressurized Water Injection Port 6 Drainage Port 7 Exhaust Port 11 Pressure Gauge 12 Liquid Level Detector 21 Gate Valve 22 Cylinder 23 Plunger 24 Gate Valve 35 Heating Coil 36 Cooling Coil 50 Waste Water 51 Spherical Elastic body 54 Open / close valve 55 Open / close valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 内側管と外側管の間に空隙を設けかつ内
側管に多数の小孔及び濾過膜を形成した2重管を用いて
構成した管路内で廃棄物を含む混合流体を輸送する方法
において、該管路の一端より一定量の混合流体を圧入す
るごとにほぼ内側管内径に等しい直径の球状弾性体を圧
入し、該球状弾性体に仕切られた状態で混合流体を搬送
するようにしたことを特徴とする廃棄物の管路輸送方
法。
1. A mixed fluid containing waste is transported in a pipe line formed by using a double pipe in which a gap is provided between an inner pipe and an outer pipe and a large number of small holes and a filtration membrane are formed in the inner pipe. In this method, a spherical elastic body having a diameter substantially equal to the inner diameter of the inner pipe is press-fitted every time a fixed amount of the mixed fluid is press-fitted from one end of the pipe, and the mixed fluid is conveyed in a state of being partitioned by the spherical elastic body. A pipeline transportation method for waste characterized by the above.
【請求項2】 管路の一部を形成する管体の外周を加熱
し、又は冷却するようにした請求項1記載の廃棄物の管
路輸送方法。
2. The method for transporting waste by pipeline according to claim 1, wherein the outer circumference of the tubular body forming a part of the pipeline is heated or cooled.
JP04208581A 1992-07-14 1992-07-14 Pipeline transportation method for waste Expired - Lifetime JP3077072B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04208581A JP3077072B2 (en) 1992-07-14 1992-07-14 Pipeline transportation method for waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04208581A JP3077072B2 (en) 1992-07-14 1992-07-14 Pipeline transportation method for waste

Publications (2)

Publication Number Publication Date
JPH0632405A true JPH0632405A (en) 1994-02-08
JP3077072B2 JP3077072B2 (en) 2000-08-14

Family

ID=16558558

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04208581A Expired - Lifetime JP3077072B2 (en) 1992-07-14 1992-07-14 Pipeline transportation method for waste

Country Status (1)

Country Link
JP (1) JP3077072B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002347929A (en) * 2001-05-25 2002-12-04 Fujiwara Techno-Art Co Ltd Transfer pipe device and method for solid/liquid mixture
JP2009226236A (en) * 2008-03-19 2009-10-08 Ube Ind Ltd Treatment method of wet sludge
JP2013060307A (en) * 2012-12-19 2013-04-04 Glory Ltd Paper sheet conveying device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5203086B2 (en) * 2007-08-10 2013-06-05 セイコーインスツル株式会社 Power supply voltage drop detection circuit

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002347929A (en) * 2001-05-25 2002-12-04 Fujiwara Techno-Art Co Ltd Transfer pipe device and method for solid/liquid mixture
JP2009226236A (en) * 2008-03-19 2009-10-08 Ube Ind Ltd Treatment method of wet sludge
JP2013060307A (en) * 2012-12-19 2013-04-04 Glory Ltd Paper sheet conveying device

Also Published As

Publication number Publication date
JP3077072B2 (en) 2000-08-14

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