JPS59138794A - Circulating pump of high temperature liquid tank - Google Patents
Circulating pump of high temperature liquid tankInfo
- Publication number
- JPS59138794A JPS59138794A JP1130683A JP1130683A JPS59138794A JP S59138794 A JPS59138794 A JP S59138794A JP 1130683 A JP1130683 A JP 1130683A JP 1130683 A JP1130683 A JP 1130683A JP S59138794 A JPS59138794 A JP S59138794A
- Authority
- JP
- Japan
- Prior art keywords
- pump
- tank
- impeller
- suction port
- suction
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D29/00—Details, component parts, or accessories
- F04D29/40—Casings; Connections of working fluid
- F04D29/406—Casings; Connections of working fluid especially adapted for liquid pumps
Abstract
Description
本発明は高温液槽循環ポンプに関する。
化学反応槽寸なわちタンクの反応を効率的に行うために
、内部液の一部を槽外に取り出して再び槽内に灰J循環
流路を設(プて、流路の途中に循環用ポンプを備える構
外型循環装置は広く使用されている。
第1図はかかる槽外型循環装置の基本的な循環系統図で
あり、反応槽Tの外部にポンプPを設(J、循環流路L
1、1.、2を介して接続しである。反応槽の機能、形
状、内部液体の種類、物理的、化学的性状によって各種
の循環経路、ポンプ型式がとらている。
木光明い、高温の液体を大量に循環さけるために、据イ
」、運転、保守に極めて優れた機能を有する槽外型循環
ポンプを提供づるものである。
第2図(、よ従来使用されているタンク循環装置の=(
rを示t l苫’r告図である。タンク1内の最高液位
(1−1・W−1)はタンク内の仕切板で決まり、自由
表面は右しない、タンク内に液が一杯になると、循環ポ
ンプの吸込口2及び吐出し口3を経てポンプ内を液面が
1背しA−バフ1」−ノス゛ル4から溢れる。ポンプ内
の液面は、カバーガス注入管5からン1人された不活性
ガスによって覆われ、軸貫通部(ユメカニカルシール6
によって密封されでいる。
循環ポンプの羽根車7は、吸込D 2より下の位置にあ
って、@継手8を介して電動機9によって回転され、液
を羽根車7の上部から下部に向って流し、加圧循環する
。
このような形式のポンプでは必然的にメカニカルシール
6と羽根車7との間の距離Sが長くなり、安定したポン
プの運転を行うためには軸の強度、軸受構造に充分留意
して製作しな(jれげならない3゜例えば第3図に示す
ように羽根車7の近くに大きな負荷容量を右覆る液中軸
受8をi!え、■つメカニカルシール6の上部に軸受箱
12を設(]る必要がある。然し高温の化学液の中で使
用できる液中軸受8は潤滑剤を使用することができない
1こめに、白液潤滑としなしノーれは′ならないので、
AA )’4、構造に制約があり、人きイヱ負荷容量の
軸受を設「1づることは困難である。従って保守の際の
軸受交換の頻度が多くなる。
このようなことから液中軸受8を使用しない第4図のよ
うな構造が考えられる。即J5軸の強度を増すために成
る程度太くした上で゛、強固な軸受Oa 、9bをメツ
、Jニカルシール6の上に2筒所nQ LJ、羽根車7
は完全にA−バハング≧11式として液中軸受を設4−
Jないものである。口の場合2個の軸受間の距離(スパ
ン)Slは下部軸受から羽根車までの距1llIt(オ
ーバハング)82に見合った1まざを必要とし、軸受装
置はかなり大型のものとなる。その為に駆動用電動機9
の位置が高くイ1す、高温液を扱うポンプとして吸込口
をタンクノズルと接続するだけでポンプ全体を懸架支持
することが困難になる。更にメカニカルシールの交換を
行う場合に人ぎ・な軸受装置を撤去しなければならない
ので作負°6竹が悪い。
したがって本発明の目的は、オーバーハングの長さを短
くでき、かつ大きな軸受装置を設置ノずに好適な作動が
できる高温液槽循環ポンプを提供するにある。
本ざt明によれば、循環ポンプ本体が循環経路の一部を
形成し、タンクから突出した吸込管に循環ポンプの吸込
口を接続して、t 1jjljポンプ全体をタンクに懸
架した立軸槽外型循環ポンプに於いて、タンク内最高液
位よりIIい位置にポンプ内雇^液位を雑持できるよう
に、ポンプ本体にオーバーフコ−ノズルを設The present invention relates to a high temperature liquid tank circulation pump. In order to efficiently carry out reactions in the chemical reaction tank, a part of the internal liquid is taken out of the tank and an ash J circulation channel is installed in the tank. External circulation devices equipped with pumps are widely used. Figure 1 is a basic circulation system diagram of such external circulation devices, in which a pump P is installed outside the reaction tank T (J, circulation flow path L
1, 1. , 2. Various circulation routes and pump types are used depending on the function, shape, type of internal liquid, and physical and chemical properties of the reaction tank. To avoid circulating a large amount of high-temperature liquid, we provide an external circulation pump that has excellent functionality for installation, operation, and maintenance. Figure 2 (, of the conventionally used tank circulation system)
This is a notification map showing r. The highest liquid level (1-1/W-1) in tank 1 is determined by the partition plate inside the tank, and the free surface does not change.When the tank is full of liquid, the suction port 2 and discharge port of the circulation pump 3, the liquid level in the pump increases to 1, and overflows from A-Buff 1''-Nozzle 4. The liquid level inside the pump is covered with an inert gas injected from the cover gas injection pipe 5, and
It is sealed by. The impeller 7 of the circulation pump is located below the suction D 2 and is rotated by an electric motor 9 via a joint 8 to cause the liquid to flow from the top to the bottom of the impeller 7 and circulate under pressure. In this type of pump, the distance S between the mechanical seal 6 and the impeller 7 is inevitably long, and in order to ensure stable pump operation, the strength of the shaft and bearing structure must be carefully considered when manufacturing. For example, as shown in FIG. However, since the submerged bearing 8, which can be used in high-temperature chemical liquids, cannot use lubricant, it must be lubricated with white liquid, and no failure will occur.
AA)'4 Due to structural limitations, it is difficult to design a bearing with a human-friendly load capacity.As a result, the bearing must be replaced more frequently during maintenance. A structure as shown in Fig. 4 that does not use the bearing 8 can be considered.In order to increase the strength of the J5 shaft, make it as thick as possible, and then install two strong bearings Oa and 9b on top of the J-nical seal 6. Tokoro nQ LJ, impeller 7
completely set the submerged bearing as A-bahang ≧11 type 4-
There is no J. In the case of the mouth, the distance (span) Sl between the two bearings requires one stroke corresponding to the distance 1llIt (overhang) 82 from the lower bearing to the impeller, and the bearing device becomes quite large. For that purpose, the driving electric motor 9
If the position of the pump is high, it becomes difficult to suspend and support the entire pump just by connecting the suction port to the tank nozzle as a pump that handles high-temperature liquids. Furthermore, when replacing the mechanical seal, the manual bearing device must be removed, which is a disadvantage. SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a high-temperature liquid tank circulation pump that can shorten the length of the overhang and can operate suitably without installing a large bearing device. According to the book, the circulation pump body forms a part of the circulation path, and the suction port of the circulation pump is connected to the suction pipe protruding from the tank, and the whole pump is suspended outside the vertical tank. In type circulation pumps, an overflow nozzle is installed on the pump body so that the liquid level inside the pump can be maintained at a position higher than the highest liquid level in the tank.
【プ、吸込
L】より高く、且つオーバーフローノズルより低い位置
にポンプ羽根中を位置tbめ、羽根車の吸込口を上向き
に開口し、ポンプ吸込口から羽根車吸込口よりも高い位
置に液を導くよう吸込流路を形成し、液がポンプ羽根車
通って加圧された後、ポンプl!1 il Lノ[1を
通ってタンクに戻る流路が形成されている。
以下第5図および第6図を参照して本発明の詳細な説明
する。
第55図は本発明の一実施例を示し1こ1))j面図で
・ある。10はタンクと接続するポンプ吸込み口、11
は伸縮継子(図示しない)を介してタンクと接続づるポ
ンプ吐出し口である。タンク内部の液は吸込[二110
から内胴13と外11ii114によ−)て形成される
吸込流路15の中を上に向−)て流れ、邪魔板16によ
って軸と直角ノ)向に流れの方向を変え、吸込み案内部
17を通って羽根車−18を不向き流れとなって通過し
、案内翼19を通ってポンプ111出し口11に至るよ
うになっている。オーバー70−ノズル20Iよ邪魔板
16の上部【こ設りられ、自由液面1」・W−Lが設定
される。カバー〇とメカニカルシール22の間に小室2
1を設(プ、メカニカルシール22から漏れた封液は、
軸28と一緒に回転づる水切りLM 23によって振り
飛ばされ、ポンプ内部に浸入することなく小室21のド
レン化24から11+出される。
ポンプ側軸継手25とモータ側軸継手26の間にスベー
リ27を介在さけてメカニカルシールの交換に便ならし
めた(111迄の実施例を第6図に示寸。
ポンプ軸28とモータ軸29を繋ぐ@継手25.2G及
びスベーリ27を剛に組立てることにより、モータ軸2
9どポンプ軸28は一本の剛性軸となり、七−夕に内在
づる油潤滑の負荷容量の大きい軸受で回転軸を剛に支持
することが可能であり、ポンプ側に軸受を設【プる必要
がないので、メカニカルシールの交換作業が極めて簡便
となる。
第5図のような循環ポンプを使用することにより、循環
ポンプの軒昂小型化が可能になり、ポンプ軸のオーバー
ハング長さの短縮によつ−C保守に手数のかかる液中軸
受を省略でき、かつ安定した運転が期待でさる一トに、
メカニカルシール交換の作業が大幅に短縮できる。[P, Suction L] Position the pump blade at a position tb higher than the overflow nozzle and lower than the overflow nozzle, open the impeller suction port upward, and pour the liquid from the pump suction port to a position higher than the impeller suction port. After the liquid passes through the pump impeller and is pressurized, the pump l! A flow path is formed through 1 il L and back to the tank. The present invention will be described in detail below with reference to FIGS. 5 and 6. FIG. 55 shows an embodiment of the present invention and is a 1)) j-side view. 10 is a pump suction port connected to the tank, 11
is a pump outlet connected to a tank via an expansion joint (not shown). The liquid inside the tank is sucked [2110
The flow flows upward through the suction flow path 15 formed by the inner shell 13 and the outer shell 11ii114, and the direction of the flow is changed by the baffle plate 16 in the direction perpendicular to the axis. 17, passes through the impeller 18 as a non-directional flow, passes through the guide vanes 19, and reaches the outlet 11 of the pump 111. Over 70-nozzle 20I is installed above the baffle plate 16, and the free liquid level 1'' W-L is set. Small chamber 2 between cover 〇 and mechanical seal 22
1, the sealing liquid leaking from the mechanical seal 22 is
It is thrown off by the drainer LM 23 that rotates together with the shaft 28, and is taken out from the drain 24 of the small chamber 21 without entering the inside of the pump. A subere 27 is interposed between the pump-side shaft joint 25 and the motor-side shaft joint 26 to facilitate mechanical seal replacement (the dimensions of the embodiment up to 111 are shown in Fig. 6. Pump shaft 28 and motor shaft 29 By rigidly assembling the joint 25.2G and the suberly 27 that connect the
The pump shaft 28 becomes one rigid shaft, and the rotary shaft can be rigidly supported by a bearing with a large load capacity of oil lubrication inherent in Tanabata. Since this is not necessary, replacing the mechanical seal becomes extremely simple. By using a circulation pump like the one shown in Figure 5, it is possible to make the circulation pump more compact, and by shortening the overhang length of the pump shaft, it is possible to omit submerged bearings, which require troublesome maintenance. , and for those who expect stable driving,
Mechanical seal replacement work can be significantly shortened.
第1図は僧外型循環装置の基本的な系統図、第2図は従
来使用されているタンク循環装置の一例を示す構造図、
第3図および第4図はそれぞれ従来装置の例を示す断面
図、第5図は本発明の一実施例を示づ断面図、第6図は
スベーりを使用した応用例を示す断面図である。
10・・・吸込口 11・・・吐出し1113・・・
内胴 14・・・外胴 ′16・・・邪魔板 1
8・・・羽根車 19・・・案内翼 20・・・オ
ーバーフローノズル 22・・・ヌカニカルシール
25.26・・・軸継手
第1図
第2図
第3図 第4図Figure 1 is a basic system diagram of an external circulation system, Figure 2 is a structural diagram showing an example of a conventionally used tank circulation system,
Figures 3 and 4 are sectional views showing an example of a conventional device, Figure 5 is a sectional view showing an embodiment of the present invention, and Figure 6 is a sectional view showing an application example using a subere. be. 10...Suction port 11...Discharge 1113...
Inner shell 14... Outer shell '16... Baffle plate 1
8... Impeller 19... Guide vane 20... Overflow nozzle 22... Nucanical seal
25.26...Shaft coupling Fig. 1 Fig. 2 Fig. 3 Fig. 4
Claims (3)
ンクから突出した吸込み管に循環ポンプの吸込口を接続
して、循環ポンプ全体をタンクに懸架した立輔槽外型循
環ポンプに於いて、タンク内R高液位より高い位置にポ
ンプ内最高液位をf4S持できるように、ポンプ本体に
オーバー°70−ノズルを設り、吸込口より高く、巨っ
オルバーフローノズルより低い位置にポンプ羽根車を位
置けしめ、羽根車の吸込口を上向きに開口し、ポンプ吸
込口/)11ら羽根車吸込口よりも高い位置に液を導く
ように吸込流路を形成し、液がポンプ羽根車を通って加
圧された後、ポンプ吐出し口を通ってタンクに戻る流路
を形成したことを特徴とづる高温液槽循環ポンプ。(1) The circulation pump itself forms part of the circulation path, and the circulation pump's suction port is connected to the suction pipe protruding from the tank, so that the entire circulation pump is suspended in the tank. In order to maintain the maximum liquid level in the pump at a position higher than the R high liquid level in the tank, an over degree 70-nozzle is installed on the pump body, and the position is higher than the suction port and lower than the large over flow nozzle. The pump impeller is positioned at , the suction port of the impeller is opened upward, and a suction flow path is formed so that the liquid is guided from the pump suction port 11 to a position higher than the impeller suction port. A high-temperature liquid tank circulation pump characterized by forming a flow path that returns to a tank through a pump discharge port after being pressurized through a pump impeller.
バーガスを封入し、カバーガスをシールするために封液
を内在するダブルメカニカルシールカー1〜ツツジを備
えた特許請求の範囲第1項記載の高温液槽循環ポンプ。(2) Claim 1, which includes a double mechanical seal car 1 to azalea, which seals a cover gas with a pressure higher than atmospheric pressure at the highest liquid level inside the pump and contains a sealing liquid to seal the cover gas. High temperature liquid tank circulation pump as described.
ータ側軸継手とポンプ側軸継手どの間にスペーサーを介
在せしめた特許請求の範囲第2項に記載の高温液槽循環
ポンプ。(3) High-temperature liquid tank circulation according to claim 2, wherein a spacer is interposed between the motor-side shaft joint and the pump-side shaft joint so that the seal can be easily replaced without an opening for removing the mechanical seal. pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1130683A JPS59138794A (en) | 1983-01-28 | 1983-01-28 | Circulating pump of high temperature liquid tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1130683A JPS59138794A (en) | 1983-01-28 | 1983-01-28 | Circulating pump of high temperature liquid tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59138794A true JPS59138794A (en) | 1984-08-09 |
JPH0319920B2 JPH0319920B2 (en) | 1991-03-18 |
Family
ID=11774316
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1130683A Granted JPS59138794A (en) | 1983-01-28 | 1983-01-28 | Circulating pump of high temperature liquid tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59138794A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6229494U (en) * | 1985-08-07 | 1987-02-23 | ||
WO2002099287A1 (en) | 2001-06-06 | 2002-12-12 | Basf Aktiengesellschaft | Pump for transporting a heat exchange medium for a multi-tube reactor |
JP2010059901A (en) * | 2008-09-05 | 2010-03-18 | Shinko:Kk | Marine vertical shaft centrifugal pump and its component replacing method |
EP2581132A2 (en) | 2011-10-13 | 2013-04-17 | MAN Diesel & Turbo SE | Tube bundle reactor |
DE102011121543A1 (en) | 2011-10-13 | 2013-04-18 | Man Diesel & Turbo Se | Tube bundle reactor useful for catalytic gas-phase reactions, comprises bundle of reaction tubes, heat carrier-annular flow channel, external pump comprising pump housing, main heat exchanger, second heat carrier-annular return channel |
EP3006741A1 (en) | 2014-10-09 | 2016-04-13 | Ebara Corporation | Turbopump with shaft coupling |
-
1983
- 1983-01-28 JP JP1130683A patent/JPS59138794A/en active Granted
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6229494U (en) * | 1985-08-07 | 1987-02-23 | ||
WO2002099287A1 (en) | 2001-06-06 | 2002-12-12 | Basf Aktiengesellschaft | Pump for transporting a heat exchange medium for a multi-tube reactor |
CN1300469C (en) * | 2001-06-06 | 2007-02-14 | 巴斯福股份公司 | Pump for transporting heat exchange medium for multi-tube reactor |
KR100855161B1 (en) | 2001-06-06 | 2008-08-29 | 바스프 에스이 | Pump for transporting a heat exchange medium for a multi-tube reactor |
JP2010059901A (en) * | 2008-09-05 | 2010-03-18 | Shinko:Kk | Marine vertical shaft centrifugal pump and its component replacing method |
EP2581132A2 (en) | 2011-10-13 | 2013-04-17 | MAN Diesel & Turbo SE | Tube bundle reactor |
DE102011121543A1 (en) | 2011-10-13 | 2013-04-18 | Man Diesel & Turbo Se | Tube bundle reactor useful for catalytic gas-phase reactions, comprises bundle of reaction tubes, heat carrier-annular flow channel, external pump comprising pump housing, main heat exchanger, second heat carrier-annular return channel |
DE102011084476A1 (en) | 2011-10-13 | 2013-04-18 | Man Diesel & Turbo Se | Tube reactor |
JP2013086094A (en) * | 2011-10-13 | 2013-05-13 | Man Diesel & Turbo Se | Tube nest reactor |
EP3006741A1 (en) | 2014-10-09 | 2016-04-13 | Ebara Corporation | Turbopump with shaft coupling |
Also Published As
Publication number | Publication date |
---|---|
JPH0319920B2 (en) | 1991-03-18 |
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