JP2005214190A - Impurity crushing device relative to vertical shaft type centrifugal pump - Google Patents
Impurity crushing device relative to vertical shaft type centrifugal pump Download PDFInfo
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- JP2005214190A JP2005214190A JP2004055123A JP2004055123A JP2005214190A JP 2005214190 A JP2005214190 A JP 2005214190A JP 2004055123 A JP2004055123 A JP 2004055123A JP 2004055123 A JP2004055123 A JP 2004055123A JP 2005214190 A JP2005214190 A JP 2005214190A
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- casing
- grit
- pump
- centrifugal pump
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- Crushing And Pulverization Processes (AREA)
Abstract
Description
この発明は、ポンプによって流送する液体に混入する夾雑物を破砕し、目詰り頻度を皆無に近づけ、効率よく流送する破砕装置に関する。 The present invention relates to a crushing apparatus that crushes foreign matters mixed in a liquid fed by a pump, efficiently clogs them, and efficiently feeds them.
従来、一般的に行われている破砕装置は、主として横軸形ポンプを用い、回転するインペラーの主軸を、更にインペラーを貫通する形で前方の吸入管の中心部に延長させて、これにカット羽根と、その内側にグリットを固定させる方式のものが多く、その為に破砕物の通過面積も小さくなってしまうことから、ポンプ入口口径も大きくせざるおえない。破砕後の物性によってはポンプのバキューム力が弱いことからグリッドに目詰まりを生じさせ、送液不可能に陥る。まして高粘性の流体においては、より目詰りが激しくなる。又この時に起るキャビテーションによって振動し、ポンプ本体の破損をも招くことになる。又、仮にこれを竪軸形(水中ポンプ等)としても、下から吸上げて上に吐出させる方式のポンプでは、只単に横を縦にしたにすぎず、前期のような現象が起ることは免れない。 Conventionally, the crushing apparatus generally used mainly uses a horizontal shaft type pump, and the main shaft of the rotating impeller is further extended to the center of the front suction pipe so as to penetrate the impeller and cut into this. There are many blades and a system in which grit is fixed to the inside thereof, and the passage area of the crushed material is also reduced, so the pump inlet diameter must be increased. Depending on the physical properties after crushing, the vacuum force of the pump is weak, causing the grid to be clogged and making it impossible to feed liquid. Furthermore, clogging becomes more severe in highly viscous fluids. Further, the pump body vibrates due to cavitation occurring at this time, and the pump main body is also damaged. Also, even if this is a shaft type (submersible pump, etc.), a pump that sucks up from the bottom and discharges it upwards will simply cause the phenomenon as shown in the previous term to be just vertical. Is inevitable.
この発明は、前記従来の技術の項で述べたようなトラブルを解決し、高粘性の流体中に混入している夾雑物をも破砕・流送し得るコンパクトな装置の提供を目的としている。 An object of the present invention is to provide a compact apparatus capable of solving the troubles described in the section of the prior art and crushing / feeding foreign matter mixed in a highly viscous fluid.
この発明に於いては、前記課題を解決するための手段として、図1に示す竪軸形遠心ポンプを使用することを基本的な前提としている。
このポンプは、図示のように吸入口▲6▼が、胴体▲1▼の上端に位置し、主軸の回転方向に施回しながらインペラー▲5▼の入り口に吸い込まれる方式のものであり、通常の気圧下においては−760mmHgの強力なバキュームを発揮し得る。破砕物の通過面積を大きくした形状のグリット▲8▼と上記バキューム力とが渾然一体となって前期課題は解決される。In the present invention, as a means for solving the above-mentioned problems, the basic premise is to use the shaft type centrifugal pump shown in FIG.
As shown in the figure, this pump has a suction port (6) located at the upper end of the body (1) and is sucked into the inlet of the impeller (5) while being rotated in the rotation direction of the main shaft. A strong vacuum of -760 mmHg can be exhibited under atmospheric pressure. The grit (8) having a shape in which the passage area of the crushed material is increased and the above-described vacuum force are united and the previous problem is solved.
図1に示す実施形態のポンプ本体の強力なバキューム力は、従来のポンプのシール位置とは逆の、吸入側にメカシール▲13▼が装着されていることで得られる完全シールと、胴体▲1▼の中心部で回転する主軸▲2▼の旋回流によって発生する。この旋回流は、カット羽根▲9▼を経てグリット▲8▼の周囲に長方形に配列した切欠き穴▲11▼を通り、インペラー▲5▼の入り口に吸い込まれる。 The strong vacuum force of the pump body of the embodiment shown in FIG. 1 is obtained by the fact that the mechanical seal (13) is mounted on the suction side opposite to the seal position of the conventional pump, and the body (1) It is generated by the swirling flow of the main shaft {circle around (2)} rotating at the center of ▼. This swirling flow passes through the cut blades {9}, passes through the cutout holes {11} arranged in a rectangle around the grit {8}, and is sucked into the entrance of the impeller {5}.
この旋回流は、例えば走り幅跳びの際の<助走>の役目を担い、同じく一定の間隔を停止した状態から飛ぶ場合と比較して、地上を蹴る力が極めて小さくてすむのと同様に、インペラー▲5▼に与える衝撃は小さく、従って耐摩耗度は高まる。 This swirling flow, for example, plays the role of <Running> in the case of long jump, and impellers are similar to the case where the force of kicking the ground is extremely small compared to the case of flying from a state where a certain interval is stopped. The impact given to 5 ▼ is small, and therefore the wear resistance is increased.
以上のように、本発明においては、強力なバキュームと耐摩耗性を持った竪軸形遠心ポンプを基調とし、破砕物通過面積を大きくとった特殊形状のグリットとカット羽根を装着した事により、高粘性液に混入する夾雑物をもコンパクトで効率的に流送する事が可能となった。実験的には粘性係数1000cpの中の夾雑物を破砕流送することに成功しており、その効果は大きいものと思考される。 As described above, in the present invention, the shaft-type centrifugal pump having a strong vacuum and wear resistance is used as a basic tone, and by mounting a specially shaped grit and cut blade having a large crushed material passage area, Contaminants mixed in the highly viscous liquid can be transported in a compact and efficient manner. Experimentally, it has succeeded in crushing and feeding impurities in the viscosity coefficient of 1000 cp, and the effect is considered to be great.
▲1▼ 胴 体
▲2▼ 主 軸
▲3▼ ケーシング
▲4▼ ケーシング円盤
▲5▼ インペラー
▲6▼ 吸入口
▲7▼ 吐出口
▲8▼ グリット本体
▲9▼ カット羽根本体
▲10▼ 軸受箱
▲11▼ グリットの切欠穴
▲12▼ カット羽根
▲13▼ メカニカルシール
▲14▼ プーリー
A 吸引流体進路
B 吐出流体進路(1) Body (2) Main shaft (3) Casing (4) Casing disk (5) Impeller (6) Suction port (7) Discharge port (8) Grit body (9) Cut blade body (10) Bearing box (7) 11 ▼ Grit cutout hole ▲ 12 ▼ Cut blade ▲ 13 ▼ Mechanical seal ▲ 14 ▼ Pulley A Suction fluid path B Discharge fluid path
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JP2004055123A JP2005214190A (en) | 2004-01-30 | 2004-01-30 | Impurity crushing device relative to vertical shaft type centrifugal pump |
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JP2004055123A JP2005214190A (en) | 2004-01-30 | 2004-01-30 | Impurity crushing device relative to vertical shaft type centrifugal pump |
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JP2005214190A true JP2005214190A (en) | 2005-08-11 |
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JP2004055123A Pending JP2005214190A (en) | 2004-01-30 | 2004-01-30 | Impurity crushing device relative to vertical shaft type centrifugal pump |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012233457A (en) * | 2011-05-09 | 2012-11-29 | Teral Inc | Coolant liquid transfer pump |
CN103629161A (en) * | 2013-12-17 | 2014-03-12 | 辽宁长志泵业有限公司 | Second-level cantilever type small flow centrifugal pump |
CN104776046A (en) * | 2014-01-14 | 2015-07-15 | 上海熊猫机械(集团)有限公司 | Pump cutting device having cutting and diversion functions |
CN108533500A (en) * | 2018-03-26 | 2018-09-14 | 石家庄开发区石泵泵业有限公司 | A kind of cutting pump installation for cutting fluid |
-
2004
- 2004-01-30 JP JP2004055123A patent/JP2005214190A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012233457A (en) * | 2011-05-09 | 2012-11-29 | Teral Inc | Coolant liquid transfer pump |
CN103629161A (en) * | 2013-12-17 | 2014-03-12 | 辽宁长志泵业有限公司 | Second-level cantilever type small flow centrifugal pump |
CN104776046A (en) * | 2014-01-14 | 2015-07-15 | 上海熊猫机械(集团)有限公司 | Pump cutting device having cutting and diversion functions |
CN108533500A (en) * | 2018-03-26 | 2018-09-14 | 石家庄开发区石泵泵业有限公司 | A kind of cutting pump installation for cutting fluid |
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