JPS6012599B2 - Solids collection device - Google Patents
Solids collection deviceInfo
- Publication number
- JPS6012599B2 JPS6012599B2 JP8794980A JP8794980A JPS6012599B2 JP S6012599 B2 JPS6012599 B2 JP S6012599B2 JP 8794980 A JP8794980 A JP 8794980A JP 8794980 A JP8794980 A JP 8794980A JP S6012599 B2 JPS6012599 B2 JP S6012599B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- cyclone
- water
- solids
- fluid
- 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.)
- Expired
Links
Landscapes
- Jet Pumps And Other Pumps (AREA)
- Cyclones (AREA)
Description
【発明の詳細な説明】
本発明は、固形物を含有した流体から固形物を分離補集
する装置、ことに原子力発電所の廃液ホールドアップタ
ンクの底部に沈積するヘドロを排除する装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for separating and collecting solids from a solid-containing fluid, and more particularly to an apparatus for removing sludge deposited at the bottom of a waste liquid hold-up tank in a nuclear power plant.
原子力発電所の廃液ホールドアップタンクに放射能を有
するヘドロが多くたまるとタンクのメインテナンスが困
難となる。このタンク内のヘドロのような固形物を随時
吸引補集する装置を提供せんとするのが本発明の目的で
ある。すなわち本発明は、固形物を含有した流体を吸引
し密閉容器状竪型サイクロンに送るジェットポンプ、本
体下部に設けられた固形物排出口と本体内部の鞠心付近
に開□した流体取出管とを備えた密閉容器状竪型サイク
ロン、前記固形物排出口に着脱可能に連結される補集容
器、及び前記流体取出管から流体を前記ジェットポンプ
にジェットポンプの駆動用流体として送る送給手段を備
えたことを特長とする固形物の瓶集装置にある。When a large amount of radioactive sludge accumulates in waste liquid hold-up tanks at nuclear power plants, tank maintenance becomes difficult. It is an object of the present invention to provide a device for sucking and collecting solid matter such as sludge in this tank at any time. That is, the present invention includes a jet pump that sucks fluid containing solids and sends it to a vertical cyclone in the form of a closed container, a solids discharge port provided at the bottom of the main body, and a fluid take-off pipe opened near the ball center inside the main body. a vertical cyclone in the form of a closed container, a collecting container detachably connected to the solid matter discharge port, and a feeding means for sending fluid from the fluid take-out pipe to the jet pump as a driving fluid for the jet pump. A bottle collection device for solids is characterized by the following features:
本発明装置は可搬式とするのが好適であり、これにより
所要時に任意の場所へもってゆき固形物の捕集が行なえ
る。The device of the present invention is preferably portable, so that it can be taken to any location when required to collect solid matter.
以下本発明を添付図面に例示したその好適な実施例につ
いて詳述する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will now be described in detail with reference to preferred embodiments illustrated in the accompanying drawings.
第1図に示すように本発明装置はサイクロン1、ジェッ
トポンプ2、送水ポンプ3、固形物楢葉容器4を主要構
成部分として成るものである。As shown in FIG. 1, the apparatus of the present invention consists of a cyclone 1, a jet pump 2, a water pump 3, and a solids container 4 as main components.
サイクロン1‘ま竪型の外殻laの上部に接線方向に水
平に関口せしめた流入管leを、また底部に下方に開口
し固形物騒集容器4につながる固形物排出管lcを有す
る。またこのサイクロン1の内部中心軸線上に一端を閉
口し他端はサイクロン上部から側方にのびる液体取出管
16と、サイクロン頂部に閉口する上部排出管ldとが
設けてある。この上部排出管ldは通常のサイクロンで
は設けられておらず、本発明独自のものであり、配管1
4を介し本発明装置の吐出端10につながる。液体吐出
管lbは配管13を介し送水ポンプ3に連結してある。The cyclone 1' has an inflow pipe le which is tangentially and horizontally connected to the top of the vertical outer shell la, and a solids discharge pipe lc which opens downward and connects to the solids collection container 4 at the bottom. Also provided on the internal central axis of the cyclone 1 are a liquid take-out pipe 16 whose one end is closed and whose other end extends laterally from the top of the cyclone, and an upper discharge pipe ld which is closed at the top of the cyclone. This upper discharge pipe ld is not provided in a normal cyclone, and is unique to the present invention.
4 to the discharge end 10 of the device according to the invention. The liquid discharge pipe lb is connected to the water pump 3 via a pipe 13.
この送水ポンプの吐出側は弁6を介し配管1 1からジ
ェットポンプ2の駆動ノズル2aに接続してある。また
この送水ポンプ吐出側は配管16、弁7を介してフィル
夕5に接続してあり、このフィル夕5の出口側は弁8、
配管17を介し配管11に接続してある。ジェットポン
プの吸込口2bは配管15を介し本装置の吸込端に接続
し、吐出口2cは配管12を介し前述のサイクロン1の
流入管に接続してある。The discharge side of this water pump is connected to a drive nozzle 2a of a jet pump 2 from a pipe 11 via a valve 6. Further, the discharge side of this water pump is connected to the filter 5 via piping 16 and valve 7, and the outlet side of this filter 5 is connected to valve 8,
It is connected to the pipe 11 via a pipe 17. The suction port 2b of the jet pump is connected to the suction end of the apparatus via a pipe 15, and the discharge port 2c is connected to the inflow pipe of the cyclone 1 via a pipe 12.
第2図に示すように本発明装置Eはその吸引端9に接続
した吸引管Bの先端の吸引ノズルをt 目的のタンクD
内のヘドロに挿入し、吐出機亀Q‘こ接続した戻り管C
をタンクD内に閉口せしめて使用する。As shown in FIG. 2, the device E of the present invention connects the suction nozzle at the tip of the suction pipe B connected to the suction end 9 to the target tank D.
Return pipe C inserted into the sludge inside and connected to the discharge machine Q'
is used by closing it in tank D.
その作用を次に述べる。Its effect will be described next.
送水ポンプ3で加圧された水は管亀亀を通ってジェット
ポンプ2の駆動ノズル2aに入りジェットポンプを駆動
する。Water pressurized by the water pump 3 passes through the pipe and enters the drive nozzle 2a of the jet pump 2, driving the jet pump.
そこでジェットポンプ吸込口2bに負圧が発生し吸引ノ
ズルAおよび吸引管Bを通ってタンクD内の耽積固形物
が水と−諸に吸込まれる。駆動ノズル2aから噴出され
た水と吸引口20へ吸引された沈積固形物を含むタンク
水とが合流して吐出口2cおよび管!2を通って流入管
竃eからサイクロン2内へ噴出される。Then, a negative pressure is generated at the jet pump suction port 2b, and the accumulated solids in the tank D are sucked into the water and other liquids through the suction nozzle A and the suction pipe B. The water ejected from the drive nozzle 2a and the tank water containing the deposited solids sucked into the suction port 20 merge to form the discharge port 2c and the pipe! 2 and is ejected into the cyclone 2 from the inflow pipe e.
流入管官eは接線方向に閉口しているのでサイクロン内
に旋回流が発生しその遠心力の作用で固形物は外周部に
分離される。Since the inflow pipe e is closed in the tangential direction, a swirling flow is generated within the cyclone, and the solid matter is separated to the outer circumference by the action of the centrifugal force.
固形物は旋回しつつ下方向に落ちていって固体排出管亀
cを通って固形物補集容器4内に入る。The solids fall downward while rotating and enter the solids collecting container 4 through the solids discharge pipe c.
サイクロン亀の胸○部の水(固形物はない)は液体取出
管耳bおよび上部排出管亀dから吐出される。液体取母
管亀bを出た水は送水ポンプ3に吸込まれる。上部取出
管亀dを出た水は戻り管Cを通ってもとのタンクDにも
どる。Water (no solid matter) in the thoracic region of the cyclone turtle is discharged from the liquid outlet tube ear b and the upper discharge tube turtle d. The water coming out of the liquid taker tube turtle b is sucked into the water pump 3. The water that exits the upper outlet pipe d passes through the return pipe C and returns to the original tank D.
本装置は密閉系であるので系外から入ったと同量だけ系
外へ出ていく。Since this device is a closed system, the same amount of water that enters from outside the system comes out.
従ってタンク○から吸引された固形物および水の合計容
積ともどこれる水の容積は自ら等しくなる。このためタ
ンクD内の水位は変化しない。吸引ノズルAの位置を適
当な方法(例えば手動)で移動させタンクDの底面の固
形物を吸込めば上述の如き作用によりタンク水位を変え
ることなく固形物だけを固形物補集容器4内に集められ
る。Therefore, the total volume of solids and water sucked from tank ○ and the volume of water will be equal to each other. Therefore, the water level in tank D does not change. If the position of the suction nozzle A is moved by an appropriate method (for example, manually) and the solid matter on the bottom of the tank D is sucked, only the solid matter can be transferred into the solid matter collection container 4 without changing the tank water level due to the above-mentioned action. Can be collected.
サイクロン亀では分離できないような固形物(例えば非
常に微細な粒子「比重が水に近い粒子など)がある場合
は弁7,8を開いて流れの一部をフィルター5に通しこ
れで捕獲する。If there are solids that cannot be separated by the cyclone turtle (for example, very fine particles with a specific gravity close to that of water), valves 7 and 8 are opened to allow a portion of the flow to pass through the filter 5 and capture it.
本発明による実際の装置の1例の形状の具体的な大きさ
、この具体例装置で扱う後処理物質の性状t濃度〜流量
及び流速等の処理条件「および処理結果を次に示す。The specific size of the shape of one example of the actual device according to the present invention, the properties of the post-processing substance handled in this specific example device, the processing conditions such as concentration to flow rate and flow rate, and the processing results are shown below.
サイクロンの最大内径30物的高さ90仇協、ジヱット
ボンプ2ののど部の内径18.3脚、長さ230燭とし
、送水ポンプ3を錫程28h、流量2.2でノQのもの
とした。The maximum inner diameter of the cyclone was 30, and the physical height was 90. The inner diameter of the throat of jet pump 2 was 18.3, and the length was 230. The water pump 3 was designed with a height of 28 hours and a flow rate of 2.2. .
直径2.8h、高さ公hのタンクDには粒径100沙「
200料も 3脚,5柵の砂が次簿している潜水が撤さ
れても、た。Tank D with a diameter of 2.8h and a height of 100mm has a particle size of 100mm.
The 200 fee also remained even after the 3-leg, 5-bar sand diving was canceled.
これを彼処理物として上述の装置を運転したところ〜
メズルAから吸引管Bを介し配管母 5へ砂の濃度約2
0%の清水が流速1.8hノふ流量4.8虎ノhでジェ
ットポンプ2に吸引され「流速1.4mノsも流量?め
ノhでこのジェットポンプの出口の配管富2からサイク
ロン川こ導入された。サイクロン貴の液体取出管軍bか
らは流速i.4mノs、流量2.2でノhの流れとなっ
て清水のみが送水ポンプ3に達し〜同じく流速1.4m
ノs、流量2.2めノhの流れが送水ポンプ翁からジェ
ットポンプ2の駆動ノズル2aに送られた。When I operated the above-mentioned device using this as a processing material~
The concentration of sand is approximately 2 from muzzle A to piping base 5 via suction pipe B.
0% fresh water is sucked into the jet pump 2 at a flow rate of 1.8 h and a flow rate of 4.8 h, and a cyclone is generated from the pipe 2 at the outlet of this jet pump at a flow rate of 1.4 m.s. Kawako was introduced. From the liquid extraction pipe b of Cyclone Taka, the flow rate was 1.4 m no s, the flow rate was 2.2 h, and only fresh water reached the water pump 3 ~ Also, the flow rate was 1.4 m
A flow with a flow rate of 2.2 mm and a flow rate of 2.2 mm was sent from the water pump to the drive nozzle 2a of the jet pump 2.
一方〜 サイクロン畳の上部排出管3dから配管1 公
「吐出端亀強ち戻り管Cには流速1.敵hノs〜流量4
.8力ノリで「サイクロンで完全に分離された清水のみ
が返送された。以上〜吸込端9から水と固形物が吸込ま
れる場合について説明したがちか物こ、吸引ノズルAま
たは戻り管Cが何らかのトラブルで完全に閉塞した場合
でも「水は3→il→2→12→1→13→3の順で循
環するので送水ポンプは支障なく運転される。On the other hand, from the upper discharge pipe 3d of the cyclone tatami to pipe 1, the flow rate is 1.
.. 8-force nozzle "Only fresh water that was completely separated by the cyclone was returned. Above we have explained the case where water and solids are sucked in from the suction end 9. Even if the pump is completely blocked due to some kind of trouble, the water pump will continue to operate without any problems because the water circulates in the order of 3 → il → 2 → 12 → 1 → 13 → 3.
又、吸引ノズルAから空気のみを吸込んだ場合でもち吸
込まれた空気はサィクロンー内を浮上し上部取出警官d
から排出される。Also, when only air is sucked from suction nozzle A, the sucked air floats up inside the cyclone and is taken out from the top.
is discharged from.
水は3→11→2→12→1→13→3の順で循環する
ので送水ポンプは支障なく運転される。この作用を利用
して「粉塵を含む空気を吸引し粉塵をサイクロンで分離
して4内に楠集することも可能である。Since the water circulates in the order of 3 → 11 → 2 → 12 → 1 → 13 → 3, the water pump can be operated without any problem. Utilizing this effect, it is also possible to suck air containing dust, separate the dust with a cyclone, and collect it in the cyclone.
容器4またはフィル夕5が固形物でいっぱいになれば弁
を閉じて取外し任意の場所へはこんで処分できる。上述
のように本発明によれば装置が密閉系になっているので
吸引した量と同量のものが吐出される。When the container 4 or filter 5 is full of solids, the valve can be closed, removed, and disposed of at any desired location. As described above, according to the present invention, since the device is a closed system, the same amount of suction is discharged.
このためタンクから沈積物を吸引するような場合タンク
水位は変化しない。よって二次廃水を生ぜずタンクの水
位制御不要という効果がある。また吸引物が何であって
も(気体も液体)、さらに吸引管が閉塞しても送水ポン
プは正常に運転される。このため取扱い容易、極端に水
が少なく空気を混入する時でも使用可能という効果があ
る。ざらに吸込口から固形物補集容器まで単純な形状の
通路でつながっているので目詰りが少なく〜大きい固形
物でも吸引可能である。Therefore, when sucking sediment from the tank, the tank water level does not change. Therefore, there is an effect that no secondary wastewater is generated and there is no need to control the water level in the tank. Furthermore, the water pump will operate normally regardless of what is being aspirated (gas or liquid) and even if the suction pipe is blocked. Therefore, it is easy to handle and can be used even when there is extremely little water and air is mixed in. Since the suction port is connected to the solid matter collection container through a simple passageway, there is little clogging and even large solid matter can be sucked.
最後に、固形物は取外し容易な容器亀またはフィル夕5
内に集められるのであとの処分が容易である。Finally, store solids in an easily removable container or filter.
It is easy to dispose of it later because it can be collected inside.
本発明は「原子力発電所のホールドアップタンクのヘド
ロ排除に限らず沈砂池の次砂吸引補集「水路の底の沈殿
物の吸引構築「空中の粉塵の吸引補集にも適用すること
ができる。The present invention can be applied not only to the removal of sludge from hold-up tanks in nuclear power plants, but also to the suction collection of sediment from sedimentation basins, the suction construction of sediment at the bottom of waterways, and the suction collection of airborne dust. .
【図面の簡単な説明】
第1図は本発明装置の好適な1実施例の系統図「第2図
は本発明装置を使用する場合の配置を示す立面図である
。
竃…・・・サイクロン、8a・…・・外殻、lb・・・
…液体取出管トlc……固体排出管t 竃d…・・・上
部排出管も亀e…・・・流入管「 2・…。
・ジェットポンプ、23……駆動ノズル、2b…・・・
吸入口、2c……吐出口「 3・…・・送水ポンプ〜
亀……固形物補集容器〜 5……フィル夕、6,77
8……弁、9……吸込端「 畳0…・・・吐出機ト 貴
竃,12,亀3,母亀8 量5,q6, i71・・
・・・配管。発i図第2図[BRIEF DESCRIPTION OF THE DRAWINGS] Fig. 1 is a system diagram of a preferred embodiment of the device of the present invention, and Fig. 2 is an elevational view showing the arrangement when the device of the present invention is used. Cyclone, 8a... Outer shell, lb...
...Liquid take-out pipe lc...Solid discharge pipe t Stove d...The upper discharge pipe is also connected e...Inflow pipe 2... ・Jet pump, 23...Drive nozzle, 2b...
Suction port, 2c...Discharge port 3...Water pump~
Turtle...solid matter collection container~ 5...filtration, 6,77
8... Valve, 9... Suction end " Tatami 0... Discharge machine, 12, Tortoise 3, Mother turtle 8 Quantity 5, q6, i71...
···Piping. Figure i Figure 2
Claims (1)
ロンに送るジエツトポンプ、本体下部に設けられた固形
物排出口と本体内部の軸心付近に開口した流体取出管及
び流体排出管とを備えた密閉容器状竪型サイクロン、前
記固形物排出口に着脱可能に連結される捕集容器、及び
前記流体取出管から流体を前記ジエツトポンプにジエツ
トポンプの駆動用流体として送る送給手段を備えたこと
を特長とする固形物の捕集装置。Equipped with a jet pump that sucks fluid containing solids and sends it to a vertical cyclone in the form of a closed container, a solids discharge port provided at the bottom of the main body, and a fluid take-out pipe and a fluid discharge pipe that open near the axis inside the main body. A vertical cyclone in the form of a closed container, a collection container detachably connected to the solid matter discharge port, and a feeding means for sending fluid from the fluid take-out pipe to the jet pump as a driving fluid for the jet pump. solid matter collection device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8794980A JPS6012599B2 (en) | 1980-06-30 | 1980-06-30 | Solids collection device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8794980A JPS6012599B2 (en) | 1980-06-30 | 1980-06-30 | Solids collection device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5713398A JPS5713398A (en) | 1982-01-23 |
JPS6012599B2 true JPS6012599B2 (en) | 1985-04-02 |
Family
ID=13929130
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8794980A Expired JPS6012599B2 (en) | 1980-06-30 | 1980-06-30 | Solids collection device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6012599B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60154875A (en) * | 1984-01-26 | 1985-08-14 | Nippon Kokan Kk <Nkk> | Longitudinal seam welding of uoe steel pipe |
SE527012C2 (en) * | 2004-04-19 | 2005-12-06 | Rolls Royce Ab | Method and auxiliary for dismantling / assembling tunnel cluster |
JP4660263B2 (en) * | 2005-04-20 | 2011-03-30 | 株式会社荏原製作所 | Vacuum generator and method for starting the vacuum generator |
JP6415307B2 (en) * | 2014-12-25 | 2018-10-31 | 三和テッキ株式会社 | Decontamination equipment for underground exudate containing radioactive materials |
-
1980
- 1980-06-30 JP JP8794980A patent/JPS6012599B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5713398A (en) | 1982-01-23 |
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