JPH03121292A - Slurry pump - Google Patents

Slurry pump

Info

Publication number
JPH03121292A
JPH03121292A JP25696089A JP25696089A JPH03121292A JP H03121292 A JPH03121292 A JP H03121292A JP 25696089 A JP25696089 A JP 25696089A JP 25696089 A JP25696089 A JP 25696089A JP H03121292 A JPH03121292 A JP H03121292A
Authority
JP
Japan
Prior art keywords
screw
screw conveyer
spiral pump
pump
common
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
JP25696089A
Other languages
Japanese (ja)
Inventor
Kiyoshi Kuioka
杭岡 潔
Ryoichi Yamamoto
良一 山本
Koji Inaba
稲葉 浩司
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 JP25696089A priority Critical patent/JPH03121292A/en
Publication of JPH03121292A publication Critical patent/JPH03121292A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To completely continue long distance transport without diluting sediment of a high concentration with water by directly coupling a spiral pump to a screw conveyer having an intake port on one end and making a rotation axis of the screw conveyer and a rotation axis of the spiral pump in common. CONSTITUTION:A spiral pump 3 is directly coupled to a screw conveyer 2 and a screw 2b of the screw conveyer and an impeller of the spiral pump 3 are rotated at a high speed with a common axis 7. An object to be transported is put into a hopper 10 and led to an intake port 2a of the screw conveyer 2 while it is mixed by an agitator 10a. The object put into the screw conveyer 2 is pressure-fed forward by thrust due to a rotation of the screw 2b to enter the spiral pump 3. A pressure is applied to the object by a centrifugal function of the impeller 3a rotating at a high speed with the rotation axis 7 common to the screw of the screw conveyer in the spiral pump 3, and the object is sequentially supplied to a distribution pipe 8 via a discharge port 3c to be transferred.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、泥状の輸送物、たとえば、沈殿池。[Detailed description of the invention] [Industrial application field] The present invention is directed to transport materials in the form of mud, such as settling ponds.

下水処理場等に堆積した沈殿物などを高濃度のまま吸引
し、輸送する際に使用されるスラリーポンプに関する。
This product relates to slurry pumps that are used to suck up and transport highly concentrated sediments in sewage treatment plants, etc.

[従来の技術] 従来用いられていたスラリーポンプには、渦巻ポンプが
有るが、渦巻ポンプで沈殿物など含水率が低く高濃度の
ものをそのまま吸引するには、吸引力が弱く、沈殿物を
充分に吸引することができないことが多く、その場合に
は止むを得ず水で希釈して濃度を低下させてから吸引し
ていた。
[Conventional technology] Conventionally used slurry pumps include centrifugal pumps, but the suction power is too weak to suck up highly concentrated materials with low water content, such as sediment, and it is difficult to remove the sediment. In many cases, it is not possible to suction sufficiently, and in such cases, it is unavoidable to dilute with water to lower the concentration before suctioning.

また、運良く高濃度のままで吸引できたとしても、短距
離の輸送には支障はないが、長距離輸送は非常に困難で
あり、途中で閉塞したり動力過負荷となって動力装置(
モータ)の焼損トラブルの発生が生じることがあった。
Furthermore, even if you are lucky enough to be able to inhale it at a high concentration, there will be no problem in short-distance transportation, but long-distance transportation will be extremely difficult, and the power equipment may become clogged or overloaded.
Motor) burnout problems could occur.

[発明が解決しようとする課題] 以上のような背景から、高濃度の沈殿物を水で希釈する
ことなく、かつ、長距離輸送を安全に継続して実現でき
るスラリーポンプの出現が望まれていた。
[Problems to be solved by the invention] From the above background, it has been desired to develop a slurry pump that can safely and continuously transport highly concentrated precipitates without diluting them with water. Ta.

[課題を解決するための手段] 本発明においては、以上の課題を解決するために、第1
の発明にあっては、 一端に取込口を有するスクリュコンベヤに渦巻ポンプを
直結し、かつ、該スクリュコンベヤノ回転軸と該渦巻ポ
ンプの回転軸を共通とした。
[Means for Solving the Problems] In the present invention, in order to solve the above problems, the first
In the invention, a volute pump is directly connected to a screw conveyor having an intake port at one end, and the rotation axis of the screw conveyor and the rotation axis of the volute pump are made common.

また、第2の発明においては、 第1の発明のスラリーポンプの吐出口以後に圧縮空気注
入用のノズルを設けた構成とした。
Moreover, in the second invention, a nozzle for compressed air injection is provided after the discharge port of the slurry pump of the first invention.

[作用] 本発明のスラリーポンプは、スクリュコンベヤのスクリ
ュ部を沈殿物中に埋没させ、高濃度のまま強制的に取込
みを行ない、かつ、スクリュの推力によりスクリュコン
ベヤに直結された下流の渦巻ポンプへ押圧するので、渦
巻ポンプへ強力に沈殿物が入り込み、その後、渦巻ポン
プのインペラによって遠心作用で吐出口側へ送り出され
、長距離の輸送が可能となる。また、第2の発明におい
ては、吐出口から排出された沈殿物に、さらに圧縮空気
をノズルより注入されるのでこの空気エネルギを付与さ
れて長比aS送が一層助長される。
[Function] The slurry pump of the present invention immerses the screw part of the screw conveyor in the sediment, forcibly takes in the sediment at a high concentration, and uses the thrust of the screw to connect the downstream volute pump directly to the screw conveyor. Since the precipitate is pressed against the precipitate, the precipitate strongly enters the centrifugal pump, and is then sent out to the discharge port side by centrifugal action by the impeller of the centrifugal pump, enabling long-distance transportation. Furthermore, in the second aspect of the invention, since compressed air is further injected from the nozzle into the sediment discharged from the discharge port, the long ratio aS feeding is further promoted by imparting this air energy.

[実施例] 以下図面に基づいて本発明に係る実施例について詳細に
説明する。
[Examples] Examples according to the present invention will be described in detail below based on the drawings.

第1図および第2図は本発明の実施例を示し、第1図は
全体縦断面図、第2図は全体側面図を示す。
1 and 2 show an embodiment of the present invention, with FIG. 1 showing an overall vertical sectional view and FIG. 2 showing an overall side view.

図において、lはスラリーポンプ、2はスクリュコンベ
ヤ、3は渦巻ポンプ、4はモータ、5はカップリング、
6は中間軸、7は共通の回転軸、8は排送管、9は圧縮
空気の注入ノズル、10はホッパ、20は逆止弁、30
は異物混入防止用のスクリーンである。
In the figure, l is a slurry pump, 2 is a screw conveyor, 3 is a centrifugal pump, 4 is a motor, 5 is a coupling,
6 is an intermediate shaft, 7 is a common rotating shaft, 8 is a discharge pipe, 9 is a compressed air injection nozzle, 10 is a hopper, 20 is a check valve, 30
is a screen to prevent foreign matter from entering.

第1図の実施例では、高濃度の沈殿物等輸送物をホッパ
10に受けて、その後、スラリーポンプ1で下流へ搬送
するものであり、これに対して第2図の実施例では、沈
殿物中へスラリーポンプ1の吸込口部を埋没させて、そ
のまま下流の排送管へ搬送するものである。
In the embodiment shown in FIG. 1, highly concentrated sediment is received in the hopper 10 and then transported downstream by the slurry pump 1. In contrast, in the embodiment shown in FIG. The suction port of the slurry pump 1 is buried in the material, and the material is transported directly to the downstream discharge pipe.

まず、第1図の実施例(第1実施例)について構造と作
動について説明する。
First, the structure and operation of the embodiment shown in FIG. 1 (first embodiment) will be explained.

輸送物はまずホッパlOへ投入され、攪拌機10aで混
練されながら、スクリュコンベヤ2の吸込口2aへ導か
れる。スクリュコンベヤ2内へ入った輸送物はスクリュ
2bの回転による推力により前方へ圧送され、渦巻ポン
プ3内へ入る。渦巻ポンプ3内ではスクリュコンベヤの
スクリュと共通の回転軸7により高速で回転するインペ
ラ3aの遠心作用で輸送物に圧力を付与し、吐出口3C
を経由して輸送物は排送管8へ順次送給され、搬送され
る。
The material to be transported is first put into the hopper IO, and guided to the suction port 2a of the screw conveyor 2 while being kneaded by the stirrer 10a. The transported material entering the screw conveyor 2 is forced forward by the thrust generated by the rotation of the screw 2b and enters the centrifugal pump 3. Inside the centrifugal pump 3, pressure is applied to the transported material by the centrifugal action of the impeller 3a, which rotates at high speed by a rotating shaft 7 common to the screw of the screw conveyor, and the discharge port 3C
The objects to be transported are sequentially fed to the discharge pipe 8 and conveyed.

ここで、第2の発明においては、排送管8に圧縮空気の
注入ノズル9が設けてあり、3〜10kg/cm’Gの
圧縮空気が注入され、輸送物は空気エネルギによりさら
に遠方へ輸送される。なお。
Here, in the second invention, the discharge pipe 8 is provided with a compressed air injection nozzle 9, compressed air of 3 to 10 kg/cm'G is injected, and the transported object is transported further away by air energy. be done. In addition.

スラリーポンプには軸受2Cやモータ方向へ輸送物が漏
洩することを防止するため、シール2dやシール3dが
設けられている。
The slurry pump is provided with a seal 2d and a seal 3d to prevent the transported material from leaking toward the bearing 2C and the motor.

また、第2図の実施例(第2実施例)では、沈殿池や海
底に滞留するヘドロなどを直接採取し搬送するときに使
用され、輸送物はスクリーン30を通過してスクリュコ
ンベヤ2に吸引され、スクリュ(羽根)により垂直に上
昇し、渦巻ポンプで遠心作用を受は排送管8方向へ搬送
される。そして、注入用ノズルで圧縮空気を圧入されて
空気搬送の助力を得て長距離の輸送が実現される。なお
In addition, in the embodiment shown in FIG. 2 (second embodiment), it is used to directly collect and transport sludge accumulated in sedimentation ponds and the seabed, and the transported material passes through a screen 30 and is sucked into the screw conveyor 2. The material is lifted vertically by a screw (vane), and centrifuged by a centrifugal pump and transported in the direction of the discharge pipe 8. Then, compressed air is injected through an injection nozzle, and with the help of air conveyance, long-distance transportation is realized. In addition.

逆止弁20は注入した圧縮空気によりスラリーポンプ1
側へ輸送物が逆流しないためのものであり、第1実施例
にも同様に配設しても良い。
The check valve 20 is operated by the slurry pump 1 by the injected compressed air.
This is to prevent the transported items from flowing backward to the side, and may be similarly provided in the first embodiment.

以上説明したように、本発明ではスクリュコンベヤと渦
巻ポンプとを一体的に直結としたので、高濃度の沈殿物
を安全に長距離輸送できる。また、第2の発明では圧縮
空気を付与するので一層長距離輸送が実現できる。
As explained above, in the present invention, since the screw conveyor and the centrifugal pump are integrally and directly connected, highly concentrated sediment can be safely transported over long distances. Furthermore, in the second invention, since compressed air is applied, even longer distance transportation can be realized.

[発明の効果] 以上述べたように、本発明はスクリュコンベヤに渦巻ポ
ンプを直結し、かつ、スクリュとインペラを共通軸で高
速回転する構成としであるので、高濃度の沈殿物を支障
なく取込み、かつ、強力に吐出し、長距離輸送を継続し
て実施することができる。
[Effects of the Invention] As described above, the present invention has a structure in which a centrifugal pump is directly connected to a screw conveyor, and the screw and impeller rotate at high speed on a common shaft, so that highly concentrated sediment can be taken in without any problem. Moreover, it can be powerfully discharged and can be continuously transported over long distances.

さらに、第2の発明では、スラリーポンプの吐出口後に
圧縮空気注入用のノズルを設けたので、さらに長距離の
輸送が実現できる。
Furthermore, in the second invention, since a nozzle for injecting compressed air is provided after the discharge port of the slurry pump, transportation over a further long distance can be realized.

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

第1図および第2図は本発明の実施例を示し、第1図は
全体縦断面図、第2図は全体側面図である。 1・・・スラリーポンプ、2・・・スクリュコンベヤ、
3・・・渦巻ポンプ、  4・・・モータ、7・・・共
通の回転軸、 8・・・排送管、9・・・圧縮空気注入
用ノズル、 0・・・逆止弁、 0・・・異物混入防止用のスクリーン。
1 and 2 show an embodiment of the present invention, with FIG. 1 being an overall vertical sectional view and FIG. 2 being an overall side view. 1... Slurry pump, 2... Screw conveyor,
3... Volute pump, 4... Motor, 7... Common rotating shaft, 8... Exhaust pipe, 9... Compressed air injection nozzle, 0... Check valve, 0. ...Screen to prevent foreign matter from entering.

Claims (2)

【特許請求の範囲】[Claims] (1)一端に取込口を有するスクリュコンベヤに渦巻ポ
ンプを直結し、かつ、該スクリュコンベヤの回転軸と該
渦巻ポンプの回転軸を共通としたことを特徴とするスラ
リーポンプ。
(1) A slurry pump characterized in that a centrifugal pump is directly connected to a screw conveyor having an intake port at one end, and the rotation axis of the screw conveyor and the centrifugal pump are common.
(2)スラリーポンプの吐出口後に圧縮空気注入用のノ
ズルを設けた請求項1のスラリーポンプ。
(2) The slurry pump according to claim 1, further comprising a nozzle for injecting compressed air after the discharge port of the slurry pump.
JP25696089A 1989-10-03 1989-10-03 Slurry pump Pending JPH03121292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25696089A JPH03121292A (en) 1989-10-03 1989-10-03 Slurry pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25696089A JPH03121292A (en) 1989-10-03 1989-10-03 Slurry pump

Publications (1)

Publication Number Publication Date
JPH03121292A true JPH03121292A (en) 1991-05-23

Family

ID=17299762

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25696089A Pending JPH03121292A (en) 1989-10-03 1989-10-03 Slurry pump

Country Status (1)

Country Link
JP (1) JPH03121292A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003074486A (en) * 2001-09-04 2003-03-12 Toyo Denki Industrial Co Ltd Conveying pump with hopper
DE102006035743A1 (en) * 2006-07-28 2008-01-31 U.T.S. Umwelt-Technik-Süd GmbH Biogas plant feed pump for delivering pumpable biomass e.g. organic solids, has suction duct with inlet opening for biomass to be pumped, where biomass lies above rotor opening provided in operating position of pump in duct direction
CN102032195A (en) * 2010-11-25 2011-04-27 新余市银龙机电科技有限公司 Threaded rod type mortar pump
US20120292245A1 (en) * 2009-07-02 2012-11-22 Nihon Genryo Co., Ltd. Filtration media cleaning apparatus
CN103527493A (en) * 2013-10-30 2014-01-22 陕西省水土保持局 Screw and vertex combined slurry pump

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003074486A (en) * 2001-09-04 2003-03-12 Toyo Denki Industrial Co Ltd Conveying pump with hopper
DE102006035743A1 (en) * 2006-07-28 2008-01-31 U.T.S. Umwelt-Technik-Süd GmbH Biogas plant feed pump for delivering pumpable biomass e.g. organic solids, has suction duct with inlet opening for biomass to be pumped, where biomass lies above rotor opening provided in operating position of pump in duct direction
EP1884665A2 (en) * 2006-07-28 2008-02-06 Apfelböck Ingenieurbüro GmbH Bio gas facility pump for pumping conveyable biomass in a bio gas facility
DE102006035743B4 (en) * 2006-07-28 2010-07-08 Uts Biogastechnik Gmbh Biogas plant feed pump for conveying pumpable biomass in a biogas plant
EP1884665A3 (en) * 2006-07-28 2010-10-06 UTS Biogastechnik GmbH Bio gas facility pump for pumping conveyable biomass in a bio gas facility
US20120292245A1 (en) * 2009-07-02 2012-11-22 Nihon Genryo Co., Ltd. Filtration media cleaning apparatus
US8999155B2 (en) * 2009-07-02 2015-04-07 Nihon Genryo Co., Ltd. Filtration media cleaning apparatus
CN102032195A (en) * 2010-11-25 2011-04-27 新余市银龙机电科技有限公司 Threaded rod type mortar pump
CN103527493A (en) * 2013-10-30 2014-01-22 陕西省水土保持局 Screw and vertex combined slurry pump
CN103527493B (en) * 2013-10-30 2015-10-07 陕西省水土保持局 A kind of spiral and vortex composite mud slurry pump

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