JPH04306394A - Stabilizer manufacturing device - Google Patents

Stabilizer manufacturing device

Info

Publication number
JPH04306394A
JPH04306394A JP3006514A JP651491A JPH04306394A JP H04306394 A JPH04306394 A JP H04306394A JP 3006514 A JP3006514 A JP 3006514A JP 651491 A JP651491 A JP 651491A JP H04306394 A JPH04306394 A JP H04306394A
Authority
JP
Japan
Prior art keywords
powder
air
mixed
water
discharge
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
JP3006514A
Other languages
Japanese (ja)
Other versions
JPH07103765B2 (en
Inventor
Toshinobu Araoka
俊宣 荒岡
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.)
Toyo Denki Industrial Co Ltd
Original Assignee
Toyo Denki Industrial 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 Toyo Denki Industrial Co Ltd filed Critical Toyo Denki Industrial Co Ltd
Priority to JP651491A priority Critical patent/JPH07103765B2/en
Publication of JPH04306394A publication Critical patent/JPH04306394A/en
Publication of JPH07103765B2 publication Critical patent/JPH07103765B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/45Mixing liquids with liquids; Emulsifying using flow mixing
    • B01F23/454Mixing liquids with liquids; Emulsifying using flow mixing by injecting a mixture of liquid and gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/53Mixing liquids with solids using driven stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20Jet mixers, i.e. mixers using high-speed fluid streams
    • B01F25/21Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
    • B01F25/211Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers the injectors being surrounded by guiding tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3123Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements
    • B01F25/31232Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements used simultaneously
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3123Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements
    • B01F25/31233Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements used successively
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31242Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31243Eductor or eductor-type venturi, i.e. the main flow being injected through the venturi with high speed in the form of a jet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/60Pump mixers, i.e. mixing within a pump
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/25Mixers with both stirrer and drive unit submerged in the material being mixed

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Abstract

PURPOSE:To prevent the generation of excessive vacuum between places filled with powdered body absorption pipes in discharge ports by supplying a powdered body and air to the insides of the discharge ports by negative pressure caused by discharging water from the discharge ports through the powdered body absorption pipes and air absorption pipes, and mixing the powdered body with discharged water together with air. CONSTITUTION:When water supplied into an impeller casing 13 is injected to the inside of a stirring water tank 10 through injection nozzles 18d, 18e and 18f, negative pressure is generated in a powdered body mixing space in discharge ports 17a, 17b and 17c. The powdered body 22 is injected into a mixing space of the injection nozzles 18d, 18e and 18f by the negative pressure through a powdered body absorption pipe 19d, a collecting cylinder 20, absorption pipes 19a, 19b and 19c and is mixed with the discharged water. At that time, air is mixed into the discharged water flowing into ejector nozzles in the discharge ports 17a, 17b and 17c through air absorption pipes 52a, 52b, 52c and 52d linked with the air. The powdered body 22 is mixed with the discharged water mixed with air bubbles in the mixing space to discharge it into the water tank 10.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、粉粒体を混合攪拌して
作成した混合液、例えば、掘削作業において用いる安定
液 (作泥) を、一気に、大量かつ均一に作泥するこ
とができる安定液製造装置に関する。
[Industrial Application Field] The present invention is capable of uniformly producing a large amount of mixed liquid, such as a stable liquid (sludge preparation) used in excavation work, made by mixing and stirring powder and granules, all at once. This invention relates to a stabilizing liquid manufacturing device.

【0002】0002

【従来の技術】従来、例えば、ボーリング、地中杭、地
下連続壁の下穴等の掘削作業を円滑に行うため、ベント
ナイト等の粉粒体と水とを混合して製造した安定液 (
作泥) を、掘削穴中に注入しながら、掘削作業を行っ
ている。
[Prior Art] Conventionally, in order to smoothly carry out drilling operations such as boring, underground piles, and pilot holes for underground continuous walls, stabilizing liquid (
Excavation work is carried out while injecting mud into the borehole.

【0003】そして、かかる安定液の製造装置として、
本出願人は、先に、特願昭1−19087 号で、以下
に構成を有する安定液製造装置Bを開示した。
[0003] As an apparatus for producing such a stable liquid,
The present applicant previously disclosed in Japanese Patent Application No. 1-19087 a stabilizer liquid manufacturing apparatus B having the following configuration.

【0004】即ち、同装置Bは、図7及び図8に示すよ
うに、撹拌水槽100内に、吸引口101 と複数の吐
出口102 とを具備する水中ポンプ103 を配設し
、これら吐出口102の内、少なくとも一つを攪拌水槽
100 内に開口し、かつ、上記吐出口100 に、一
端を粉粒体供給源104 に接続した粉粒体吸入パイプ
105 の他端を接続し、吐出口102 内に生じる吐
出負圧によってベントナイト等の粉粒体106 を吐出
口102 内へ吸引可能な構成としたことを特徴とする
That is, as shown in FIGS. 7 and 8, the apparatus B includes a submersible pump 103 provided with a suction port 101 and a plurality of discharge ports 102 in a stirring water tank 100. At least one of the pipes 102 is opened into the stirring water tank 100, and the other end of a powder suction pipe 105 whose one end is connected to the powder supply source 104 is connected to the discharge port 100. The discharge port 102 is characterized by a structure in which powder particles 106 such as bentonite can be sucked into the discharge port 102 by the discharge negative pressure generated within the discharge port 102 .

【0005】また、吐出口102 内には、図9に示す
ように、エジェクタノズル107 が配設されており、
同エジェクタノズル107 の前方には、粉粒体混入空
間108 が形成されている。
[0005] Furthermore, as shown in FIG. 9, an ejector nozzle 107 is disposed inside the discharge port 102.
A powder mixture space 108 is formed in front of the ejector nozzle 107 .

【0006】上記した構成により、水中ポンプ103 
の作動とともに、吸引口101 から水を吸引するとと
もに、吐出口102 から水を吐出し、その吐出によっ
て生じる負圧を利用して、即ち、エジェクタ効果によっ
て、粉粒体吸入パイプ105 を通して、吐出口102
 内に形成した粉粒体混入空間108 内に粉状の粉粒
体106 を給送して吐出水に混合し、その後、同混合
液を、吐出口102 から吐出することができる。
With the above configuration, the submersible pump 103
With the operation of , water is sucked from the suction port 101 and water is discharged from the discharge port 102 . Using the negative pressure generated by the discharge, that is, by the ejector effect, the water is drawn through the powder suction pipe 105 , and the water is discharged from the discharge port. 102
Powder-like powder 106 is fed into a powder mixing space 108 formed inside and mixed with the discharge water, and then the mixed liquid can be discharged from the discharge port 102.

【0007】かかる動作において、粉粒体106 は、
吐出水への混合の際に、瞬時に水に混合され、その後、
吐出口102 より吐出され、四方に攪拌されることに
なる。従って、迅速かつ大量に、濃度が均一な安定液を
製造することができる。
[0007] In such an operation, the granular material 106 is
When mixed with discharge water, it is instantly mixed with water, and then
It is discharged from the discharge port 102 and stirred in all directions. Therefore, a stable solution with uniform concentration can be produced quickly and in large quantities.

【0008】なお、図7及び図8において、109 は
送泥用ポンプである。
[0008] In FIGS. 7 and 8, 109 is a mud pump.

【0009】[0009]

【発明が解決しようとする課題】しかし、かかる従来の
安定液製造装置Bは、未だ、以下の解決すべき課題を有
していた。
[Problems to be Solved by the Invention] However, the conventional stabilizer liquid manufacturing apparatus B still has the following problems to be solved.

【0010】即ち、粉粒体吸入パイプ105 内にで粉
粒体106 が詰まった場合、詰まった部分と粉粒体混
入空間108 との間の粉粒体吸入パイプ105 内が
高真空になる。その結果、粉粒体混入空間108内に流
入した吐出水の一部が粉粒体吸入パイプ105 内に逆
流し、粉粒体106 を固化し、粉粒体吸入パイプ10
5 を完全に閉塞させることになる。
That is, when the powder suction pipe 105 is clogged with powder 106, the inside of the powder suction pipe 105 between the clogged part and the powder mixing space 108 becomes a high vacuum. As a result, a part of the discharged water that has flowed into the powder mixture space 108 flows back into the powder suction pipe 105 , solidifies the powder 106 , and solidifies the powder suction pipe 105 .
5 will be completely blocked.

【0011】本発明は、上記課題を解決することができ
る安定液製造装置を提供することを目的とする。
[0011] An object of the present invention is to provide a stabilizing liquid manufacturing apparatus that can solve the above problems.

【0012】0012

【課題を解決するための手段】本発明は、撹拌水槽内に
、吸引口と複数の吐出口とを具備する水中ポンプを配設
し、これら吐出口の内、少なくとも一つを攪拌水槽内に
開口し、かつ、上記吐出口に、一端を粉粒体供給源に接
続した粉粒体吸入パイプの他端、及び一端を大気に開放
した空気吸入パイプの他端をそれぞれ接続し、吐出口内
に生じる吐出負圧によって粉粒体及び空気を吐出口内へ
吸引可能な構成としたことを特徴とする安定液製造装置
に係るものである。
[Means for Solving the Problems] The present invention provides a submersible pump provided with a suction port and a plurality of discharge ports in a stirring water tank, and at least one of these discharge ports is connected to the stirring water tank. The other end of the powder suction pipe is opened and the other end of the powder suction pipe is connected to the powder supply source, and the other end of the air suction pipe whose one end is open to the atmosphere is connected to the discharge port. This invention relates to a stabilizing liquid manufacturing apparatus characterized in that it is configured to be able to suck powder and air into a discharge port by the discharge negative pressure generated.

【0013】なお、粉粒体としては、ベントナイト、セ
メント、砂、ワラ等を用いることができる。
[0013] As the powder, bentonite, cement, sand, straw, etc. can be used.

【0014】[0014]

【実施例】以下、添付図に示す実施例に基づいて、本発
明に係る安定液製造装置Aの構成を具体的に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The structure of the stabilizer manufacturing apparatus A according to the present invention will be specifically explained below based on the embodiments shown in the attached drawings.

【0015】図1及び図2において、10は撹拌水槽で
あり、その内部に水Wを一定高さHまで収容している。
In FIGS. 1 and 2, reference numeral 10 is a stirring water tank in which water W is stored up to a certain height H.

【0016】そして、かかる撹拌水槽10の内部であっ
て、底板11の中央部上には水中ポンプ12を立設状態
に載置している。
A submersible pump 12 is mounted upright on the center of the bottom plate 11 inside the stirring water tank 10.

【0017】水中ポンプ12は、図1に示すように、内
部にインペラ13a を回動自在に囲繞するインペラケ
ーシング13と、同インペラケーシング13に連設し、
内部にインペラ13a と連結し同インペラ13a を
回動するためのモータ14a を内蔵するモータケーシ
ング14とからなる。
As shown in FIG. 1, the submersible pump 12 includes an impeller casing 13 which rotatably surrounds an impeller 13a therein, and an impeller casing 13 connected to the impeller casing 13.
It consists of a motor casing 14 that is connected to an impeller 13a and has a built-in motor 14a for rotating the impeller 13a.

【0018】なお、15は水中ポンプ12を載置支持す
る支持台である。
Note that 15 is a support base on which the submersible pump 12 is placed and supported.

【0019】上記構成において、インペラケーシング1
3は、図1及び図2に示すように、その前部中央部に吸
引口16を設けるとともに、その外周縁に、複数 (本
実施例では3個) の吐出口17a,17b,17c 
を設けている。
In the above configuration, the impeller casing 1
3, as shown in FIGS. 1 and 2, has a suction port 16 in the center of its front part, and a plurality of (three in this embodiment) discharge ports 17a, 17b, 17c on its outer periphery.
has been established.

【0020】そして、図3に示すように、各吐出口17
a,17b,17c の内部には、エジェクタノズル5
0が配設され、同エジェクタノズル50の前方には、粉
粒体混入空間51が形成されている。
As shown in FIG. 3, each discharge port 17
a, 17b, 17c, there is an ejector nozzle 5 inside.
In front of the ejector nozzle 50, a powder mixture space 51 is formed.

【0021】また、吐出口17a,17b,17c に
は、吐出開口18a,18b,18c を水中ポンプ1
2から離隔した位置にもたらすためにラッパ状の噴出ノ
ズル18d,18e,18f が取付けられている。
Further, the discharge ports 17a, 17b, 17c have discharge openings 18a, 18b, 18c connected to the submersible pump 1.
Trumpet-shaped jet nozzles 18d, 18e, and 18f are attached to provide the jets at positions separated from the jets 2.

【0022】かかる構成を有する吐出口17a,17b
,17c は、粉粒体と、空気と、水との混合液を、攪
拌水槽10内に吐出するため用いられる。なお、吐出口
17a,17b,17c の吐出方向は、インペラケー
シング13の外周縁の接線方向に伸延しており、混合液
の吐出や送給を円滑なものとしている。
[0022] Discharge ports 17a and 17b having such a configuration
, 17c are used to discharge a liquid mixture of powder, air, and water into the stirring water tank 10. Note that the discharge directions of the discharge ports 17a, 17b, and 17c extend in the tangential direction of the outer peripheral edge of the impeller casing 13, so that the mixed liquid can be smoothly discharged and fed.

【0023】即ち、図1、図2及び図3に示すように、
吐出口17a,17b,17c の基端には、上記した
粉粒体混入空間51に連通する複数の下部粉粒体吸入パ
イプ19a,19b,19c の下端が連通連結されて
おり、同下部粉粒体吸入パイプ19a,19b,19c
 の上端は、集合筒20の周壁に連通連結されている。
That is, as shown in FIGS. 1, 2 and 3,
The base ends of the discharge ports 17a, 17b, 17c are connected to the lower ends of a plurality of lower powder suction pipes 19a, 19b, 19c, which communicate with the powder mixture space 51 described above. Body suction pipes 19a, 19b, 19c
The upper end of is connected to the peripheral wall of the collecting cylinder 20 in communication.

【0024】一方、集合筒20の上面には、一端を攪拌
水槽10の外部に設けた粉粒体供給源としての粉粒体収
納袋21内のベントナイト等の粉粒体22にフィルタ2
3を介して挿入した上部粉粒体吸入パイプ19d の他
端が連通連結されている。
On the other hand, on the upper surface of the collection cylinder 20, a filter 2 is attached to a powder 22 such as bentonite in a powder storage bag 21, which serves as a powder supply source and has one end provided outside the stirring water tank 10.
The other end of the upper powder suction pipe 19d inserted through the pipe 3 is connected for communication.

【0025】また、上部粉粒体吸入パイプ19d の中
途には開閉バルブ19e が設けられており、同バルブ
19e を開閉することによって、施工現場における施
工条件に適合した形態で粉粒体22を供給・停止するこ
とができる。
Further, an on-off valve 19e is provided in the middle of the upper powder suction pipe 19d, and by opening and closing the valve 19e, the powder 22 is supplied in a form that suits the construction conditions at the construction site.・Can be stopped.

【0026】さらに、図1、図2及び図3に示すように
、吐出口17a,17b,17c の基端には、上記し
たエジェクタノズル50の内部空間に連通する複数の空
気吸入パイプ52a,52b,52c の下端が連通連
結されており、同下部空気吸入パイプ52a,52b,
52c の上端は上部空気吸入パイプ52d に連通連
結されており、同上部空気吸入パイプ52d は攪拌水
槽10の上方に伸延して、その上端を大気に開放してい
る。
Furthermore, as shown in FIGS. 1, 2 and 3, a plurality of air suction pipes 52a, 52b are connected to the base ends of the discharge ports 17a, 17b, 17c, and communicate with the internal space of the ejector nozzle 50. , 52c are connected in communication with each other, and the lower air suction pipes 52a, 52b,
The upper end of 52c is connected to an upper air suction pipe 52d, which extends above the stirring water tank 10 and opens its upper end to the atmosphere.

【0027】また、図1及び図2に示すように、攪拌水
槽10の一隅部には、下部に吸引口を具備する送泥用ポ
ンプ40が配設されており、同送泥用ポンプ40の上部
に設けた吐出口41には、屈曲自在な送泥ホース42の
一端が接続されており、同送泥ホース42の他端は、所
望の掘削穴に挿入されている。
Further, as shown in FIGS. 1 and 2, a mud feeding pump 40 having a suction port at the bottom is disposed in one corner of the stirring water tank 10. One end of a flexible mud feeding hose 42 is connected to the discharge port 41 provided at the top, and the other end of the mud feeding hose 42 is inserted into a desired excavation hole.

【0028】また、図1に示すように、送泥ホース42
の上部には、開閉バルブ43が設けられている。
Furthermore, as shown in FIG.
An on-off valve 43 is provided at the top of the .

【0029】次に、上記構成を有する安定液製造装置A
の使用手順について、図1及び図2を参照して説明する
Next, stabilizer manufacturing apparatus A having the above configuration
The usage procedure will be explained with reference to FIGS. 1 and 2.

【0030】まず、上部粉粒体吸入パイプ19d の中
途に設けた開閉バルブ19e を開状態にするとともに
、送泥ホース42に設けた開閉バルブ43を閉状態にし
て、水中ポンプ12と送泥ポンプ40とを駆動する。
First, the on-off valve 19e provided in the middle of the upper powder suction pipe 19d is opened, and the on-off valve 43 provided on the mud feeding hose 42 is closed, thereby shutting down the submersible pump 12 and the mud feeding pump. 40.

【0031】同駆動によって、インペラケーシング13
内のインペラ13a が回転し、同回転によって、吸引
口16から水がインペラケーシング13内に吸引される
[0031] Due to the same drive, the impeller casing 13
The inner impeller 13a rotates, and water is sucked into the impeller casing 13 from the suction port 16 by this rotation.

【0032】インペラケーシング13内に流入した水は
、同ケーシング13から吐出口17a,17b,17c
 及び噴出ノズル18d,18e,18f を通して攪
拌水槽10内に吐出ないし噴出されることになる。
The water that has flowed into the impeller casing 13 is discharged from the impeller casing 13 through the discharge ports 17a, 17b, 17c.
The water is then discharged or spouted into the stirring water tank 10 through the jet nozzles 18d, 18e, and 18f.

【0033】また、上記吐出動作において、吐出口17
a,17b,17c 内の粉粒体混入空間51内には負
圧が発生することになる。
Furthermore, in the above-mentioned discharge operation, the discharge port 17
Negative pressure will be generated in the powder mixture space 51 inside a, 17b, and 17c.

【0034】この負圧によって、即ち、エジェクタ効果
によって、粉粒体収納袋21内の粉状の粉粒体22が、
上部及び下部粉粒体吸引パイプ19d →集合筒20→
19a,19b,19c を通して、各吐出口18d,
18e,18f の粉粒体混入空間51内に噴出され、
吐出口18d,18e,18f 内を流れる吐出水に混
合され、混合液を生成する。
Due to this negative pressure, that is, due to the ejector effect, the powder 22 in the powder storage bag 21 is
Upper and lower powder suction pipes 19d →Collecting tube 20→
19a, 19b, 19c, each discharge port 18d,
18e, 18f are ejected into the powder mixture space 51,
It is mixed with the discharged water flowing through the discharge ports 18d, 18e, and 18f to produce a mixed liquid.

【0035】ところで、本実施例では、この負圧によっ
て、大気と連通する空気吸入パイプ52a,52b,5
2c,52d を通して、空気もエジェクタノズル50
内を流れる吐出水中に混入するとになる。従って、気泡
混じりの吐出水が、各吐出口18d,18e,18f 
の粉粒体混入空間51内に流入し、この気泡混じりの吐
出水に粉粒体22が混入し、その後、攪拌水槽10内に
吐出されることになる。
By the way, in this embodiment, this negative pressure causes the air suction pipes 52a, 52b, 5, which communicate with the atmosphere, to
2c, 52d, air is also ejected through the ejector nozzle 50.
If it gets mixed in with the discharge water flowing through the interior, it will become a problem. Therefore, the discharged water mixed with air bubbles is
The powder 22 flows into the powder mixing space 51, and the powder 22 is mixed into this discharged water mixed with air bubbles, and is then discharged into the stirring water tank 10.

【0036】このように、噴出ノズル18d,18e,
18f を通して攪拌水槽10内に吐出ないし噴出され
る吐出水は、粉粒体22のみならず空気を混入している
ので、粉粒体22によって粉粒体吸引パイプ19d 内
が詰まった場合であっても、粉粒体混入空間51と、粉
粒体吸引パイプ19d の詰まった個所間に過度の真空
が発生するのを防止でき、粉粒体混入空間51から粉粒
体吸引パイプ19d 内に吐出水が逆流し、同粉粒体2
2を完全に固化するのを確実に防止することができる。
In this way, the jet nozzles 18d, 18e,
The discharged water discharged or spouted into the stirring water tank 10 through 18f contains not only the powder 22 but also air, so if the powder suction pipe 19d is clogged by the powder 22, Also, it is possible to prevent excessive vacuum from being generated between the particulate material mixing space 51 and the part where the powder material suction pipe 19d is clogged, and water discharged from the powder material mixing space 51 into the powder material suction pipe 19d. flows back, and the same powder 2
2 can be reliably prevented from solidifying completely.

【0037】その後、混合液は、噴出ノズル18d,1
8e,18f から強力に攪拌水槽10に噴出されるこ
とになる。
[0037] Thereafter, the mixed liquid is ejected through the jet nozzles 18d, 1
8e and 18f are powerfully ejected into the stirring water tank 10.

【0038】かかる動作において、粉粒体22は、吐出
水Wへの混合の際に、瞬時に水Wに混合され、攪拌水槽
10内で、四方に攪拌されることになる。
In this operation, the powder 22 is instantaneously mixed with the water W when mixed with the discharged water W, and is stirred in all directions within the stirring water tank 10.

【0039】従って、迅速かつ大量に、濃度が均一な安
定液を製造することができる。
[0039] Therefore, a stable solution having a uniform concentration can be produced quickly and in large quantities.

【0040】さらに、本実施例において、吐出口18a
,18b,18c から吐出された混合液は、空気を混
入しているため、攪拌水槽10内において、強力な攪拌
流を形成することができ、上記した安定液の濃度の均一
化をさらに促進することができる。
Furthermore, in this embodiment, the discharge port 18a
, 18b, 18c contains air, so that a strong stirring flow can be formed in the stirring water tank 10, which further promotes uniformity of the concentration of the above-mentioned stabilizing liquid. be able to.

【0041】その後、送泥ホース42に設けた開閉バル
ブ43を開状態にすると、上記した要領で製造した安定
液は、送泥ポンプ40の吐出口41から送泥ホース42
を通して、所望の掘削穴等へ迅速かつ確実に供給される
ことになる。
Thereafter, when the on-off valve 43 provided on the slurry feed hose 42 is opened, the stabilized liquid produced in the manner described above flows from the discharge port 41 of the mud feed pump 40 to the slurry feed hose 42.
Through this, it is quickly and reliably supplied to the desired excavation hole, etc.

【0042】しかも、かかる送泥作用に並行して、上記
した粉粒体混合・攪拌作用も継続して行われているので
、安定液の濃度を均一に保持しながら、送泥作用を連続
的に行うことができ、掘削作業の能率を向上することが
できる。
Moreover, in parallel with this mud feeding action, the above-mentioned powder and granule mixing and stirring actions are continuously carried out, so the mud feeding action can be carried out continuously while maintaining a uniform concentration of the stabilizing liquid. This can improve the efficiency of excavation work.

【0043】なお、上記実施例において、水中ポンプ1
2は、インペラ13a のみを具備したものとして示し
ているが、インペラ13a を取付けているモータ14
a の出力軸を下方に延出して、同延出部に攪拌羽根を
取付けることもできる。
[0043] In the above embodiment, the submersible pump 1
2 is shown as having only the impeller 13a, but the motor 14 to which the impeller 13a is attached
It is also possible to extend the output shaft of a downwardly and attach a stirring blade to the extended part.

【0044】この場合は、粉粒体22と水との混和をさ
らに促進することができ、粉粒体22の粒子をさらに微
細にできるとともに、安定液をさらに均一化することが
できる。
In this case, the mixing of the powder 22 and water can be further promoted, the particles of the powder 22 can be further made finer, and the stabilizing liquid can be made more uniform.

【0045】次に、図4及び図5を参照して、本発明に
かかる安定液製造装置Aの他の実施例について説明する
Next, another embodiment of the stabilizer production apparatus A according to the present invention will be described with reference to FIGS. 4 and 5.

【0046】本実施例は、実質的に、水中ポンプ12に
攪拌機能のみならず、送泥機能も持たせた構成に特徴を
有する。なお、上記した図1及び図2に示す安定液清掃
装置Aと同一構成の個所は、同一符合によって示す。
This embodiment is essentially characterized by a configuration in which the submersible pump 12 has not only a stirring function but also a mud feeding function. Note that parts having the same configuration as the stabilizer cleaning device A shown in FIGS. 1 and 2 described above are indicated by the same reference numerals.

【0047】本実施例において、図3及び図4に示すよ
うに、インペラケーシング13の吐出口17c は、そ
の先端を上方に屈曲しており、同上方屈曲端には、送泥
パイプ24の下端を接続しており、同送泥パイプ24の
上端には、屈曲自在な送泥ホース25の一端が接続され
ており、同送泥ホース25の他端は、所望の掘削穴に挿
入されている。
In this embodiment, as shown in FIGS. 3 and 4, the tip of the discharge port 17c of the impeller casing 13 is bent upward, and the lower end of the mud feeding pipe 24 is located at the upward bent end. One end of a flexible mud feeding hose 25 is connected to the upper end of the mud feeding pipe 24, and the other end of the mud feeding hose 25 is inserted into a desired excavation hole. .

【0048】また、図1に示すように、送泥パイプ24
の上部には、開閉バルブ26が設けられている。
Furthermore, as shown in FIG. 1, the mud feeding pipe 24
An on-off valve 26 is provided at the top of the holder.

【0049】上記構成によっても、前述した実施例と同
様に、強力に粉粒体と空気の混合・攪拌作用を行うこと
によって濃度の均一な安定液を製造することができ、し
かも、かかる送泥作用に並行して、上記した粉粒体混合
・攪拌作用も継続して行われているので、安定液の濃度
を均一に保持しながら、送泥作用を連続的に行うことが
でき、掘削作業の能率を向上することができる。
[0049] With the above structure as well, it is possible to produce a stable liquid with a uniform concentration by strongly mixing and agitating the powder and air, as in the above-mentioned embodiments, and furthermore, it is possible to produce a stable liquid with a uniform concentration. In parallel with this action, the above-mentioned mixing and stirring of the powder and granules continues, so the mud feeding action can be carried out continuously while maintaining a uniform concentration of the stabilizing liquid, which improves the excavation work. efficiency can be improved.

【0050】さらに、本実施例では、粉粒体22の投入
・作泥・攪拌・送泥を単一の水中ポンプ12を用いて行
うことができ、安定液製造装置Aを安価に製作すること
ができる。
Furthermore, in this embodiment, the charging of the granular material 22, the preparation of mud, the stirring, and the transport of mud can be performed using a single submersible pump 12, and the stable liquid manufacturing apparatus A can be manufactured at low cost. Can be done.

【0051】次に、図6を参照して、上記した実施例の
変容例について説明する。
Next, a modification of the above embodiment will be described with reference to FIG.

【0052】本変容例は、粉粒体供給源を、掘削穴中に
存在する安定液とするとともに、同安定液を、旧掘削穴
から新掘削穴へ送給可能とした構成に特徴を有する。
[0052] This modified example is characterized by a configuration in which the powder supply source is a stabilizing liquid existing in the drilled hole, and the stable liquid can be fed from the old drilled hole to the new drilled hole. .

【0053】即ち、図6において、30,31 はそれ
ぞれ新旧掘削穴であり、旧掘削穴31内にはコンクリー
トの基礎33が打設されており、その上部には、安定液
22が浮き上がっている。
That is, in FIG. 6, 30 and 31 are new and old excavated holes, respectively. A concrete foundation 33 has been placed in the old excavated hole 31, and the stabilizing liquid 22 is floating above it. .

【0054】一方、新掘削穴30内には未だ基礎打ちは
なされていない。
On the other hand, the foundation has not yet been poured into the newly excavated hole 30.

【0055】そして、本実施例にかかる安定液製造装置
Aは、その上部粉粒体吸入パイプ19c の一端を旧掘
削穴31内の粉粒体22内に挿入するとともに、送泥ホ
ース25の一端を新掘削穴30内に挿入している。
The stabilizer liquid manufacturing apparatus A according to this embodiment inserts one end of the upper particulate matter suction pipe 19c into the particulate matter 22 in the old excavation hole 31, and also inserts one end of the mud feeding hose 25. is inserted into the newly drilled hole 30.

【0056】かかる構成によって、前述した実施例と同
様に、水中ポンプ12によって生じた負圧を利用して旧
掘削穴31から安定液22と空気とを吸引して攪拌水槽
10内で水と効率よくかつ均一に混合攪拌して安定液を
製造し、同安定液を連続して新掘削穴30に送給するこ
とができる。
With this configuration, similarly to the embodiment described above, the negative pressure generated by the submersible pump 12 is used to suck the stabilizing liquid 22 and air from the old excavation hole 31, and the water and air are efficiently mixed in the stirring water tank 10. A stable liquid can be produced by mixing and stirring well and uniformly, and the stable liquid can be continuously fed to the newly drilled hole 30.

【0057】そして、かかる安定液を、新掘削穴30の
内面に充満することによって、掘削壁の崩壊を確実に防
止することができる。
By filling the inner surface of the newly excavated hole 30 with this stabilizing liquid, collapse of the excavated wall can be reliably prevented.

【0058】なお、第3図において、32はコンクリー
ト投入装置を示す。
[0058] In Fig. 3, numeral 32 indicates a concrete charging device.

【0059】以上、図1〜図5に示す実施例をおいて、
ベントナイトを水への混入物として用いたが、本発明に
かかる安定液製造装置は、水に混和することによって泥
漿物を生成可能な他の原料、例えば、フライアッシュ、
セメント、セメント混和剤、、砂、ワラ等にも適用でき
るものである。即ち、本発明において、粉粒体とは、ベ
ントナイトの他、上記セメント等の原料も含むものであ
る。
[0059] In the embodiments shown in FIGS. 1 to 5,
Although bentonite is used as a contaminant in water, the stable liquid production device according to the present invention can also contain other raw materials that can produce a slurry by mixing with water, such as fly ash,
It can also be applied to cement, cement admixtures, sand, straw, etc. That is, in the present invention, the granular material includes not only bentonite but also raw materials such as the above-mentioned cement.

【0060】[0060]

【発明の効果】上記した構成により、本発明は、以下の
効果を奏する。
[Effects of the Invention] With the above-described configuration, the present invention has the following effects.

【0061】■本発明では、水中ポンプの作動とともに
、吸引口から水を吸引するとともに、吐出口から水を吐
出し、その吐出によって生じる負圧を利用して、即ち、
エジェクタ効果によって、粉粒体吸入パイプ及び空気吸
入パイプを通して、吐出口内に、粉状の粉粒体及び空気
を給送して、粉粒体を空気とともに吐出水に混合し、そ
の後、同混合液を、吐出口から吐出することができる。 かかる動作において、粉粒体は、吐出水への混合の際に
、瞬時に水に溶解され、その後、吐出口より吐出され、
四方に攪拌されることになる。
[0061] In the present invention, when the submersible pump operates, water is sucked from the suction port and water is discharged from the discharge port, and the negative pressure generated by the discharge is used to:
By the ejector effect, the powder and air are fed into the discharge port through the powder and air suction pipes, and the powder and the air are mixed into the discharged water, and then the mixed liquid is mixed with the air. can be discharged from the discharge port. In such an operation, the granular material is instantly dissolved in the water when mixed with the discharge water, and then discharged from the discharge port,
It will be stirred in all directions.

【0062】従って、迅速かつ大量に、濃度が均一な安
定液を製造することができる。
[0062] Therefore, a stable solution with uniform concentration can be produced quickly and in large quantities.

【0063】■また、吐出口から吐出された混合液は、
空気を混入しているため、粉粒体によって粉粒体吸引パ
イプ内が詰まった場合であっても、吐出口内部と粉粒体
吸引パイプの詰まった個所間に過度の真空が発生するの
を防止でき、粉粒体混入空間から粉粒体吸引パイプ内に
吐出水が逆流し、同粉粒体が完全に固化するのを確実に
防止することができる。
■Also, the mixed liquid discharged from the discharge port is
Because air is mixed in, even if the powder suction pipe becomes clogged with powder, it prevents excessive vacuum from being generated between the inside of the discharge port and the clogged part of the powder suction pipe. This can reliably prevent discharged water from flowing back into the powder suction pipe from the powder mixing space and completely solidifying the powder.

【0064】■さらに吐出口から吐出された混合液は、
空気を混入しているため、攪拌水槽内において、強力な
攪拌流を形成することができ、上記した安定液の濃度の
均一化をさらに促進することができる。
[0064] Furthermore, the mixed liquid discharged from the discharge port is
Since air is mixed in, a strong stirring flow can be formed in the stirring water tank, and the uniformity of the concentration of the above-mentioned stabilizing liquid can be further promoted.

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

【図1】本発明に係る安定液製造装置の一実施例の断面
正面図である。
FIG. 1 is a cross-sectional front view of an embodiment of a stabilizer manufacturing apparatus according to the present invention.

【図2】同平面図である。FIG. 2 is a plan view of the same.

【図3】同要部断面側面図である。FIG. 3 is a cross-sectional side view of the same main part.

【図4】他の実施例の断面正面図である。FIG. 4 is a cross-sectional front view of another embodiment.

【図5】同平面図である。FIG. 5 is a plan view of the same.

【図6】同変容例の断面正面図である。FIG. 6 is a cross-sectional front view of the modified example.

【図7】従来の安定液製造装置の断面正面図である。FIG. 7 is a cross-sectional front view of a conventional stabilizing liquid manufacturing apparatus.

【図8】同平面図である。FIG. 8 is a plan view of the same.

【図9】同要部断面側面図である。FIG. 9 is a cross-sectional side view of the same main part.

【符号の説明】[Explanation of symbols]

A  安定液製造装置 10  攪拌水槽 12  水中ポンプ 16  吸引口 17a,17b,17c 吐出口 18a,18b,18c 噴出ノズル 22  粉粒体 A Stabilizing liquid manufacturing equipment 10 Stirring water tank 12 Submersible pump 16 Suction port 17a, 17b, 17c discharge port 18a, 18b, 18c jet nozzle 22 Powder material

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  撹拌水槽内に、吸引口と複数の吐出口
とを具備する水中ポンプを配設し、これら吐出口の内、
少なくとも一つの吐出口を攪拌水槽内に開口し、かつ、
上記吐出口に、一端を粉粒体供給源に接続した粉粒体吸
入パイプの他端、及び一端を大気に開放した空気吸入パ
イプの他端をそれぞれ接続し、吐出口内に生じる吐出負
圧によって粉粒体及び空気を吐出口内へ吸引可能な構成
としたことを特徴とする安定液製造装置。
Claim 1: A submersible pump having a suction port and a plurality of discharge ports is disposed in a stirring water tank, and among these discharge ports,
at least one outlet is opened in the stirring water tank, and
The other end of a powder suction pipe whose one end is connected to a powder supply source, and the other end of an air suction pipe whose one end is open to the atmosphere are connected to the above discharge port, and the discharge negative pressure generated within the discharge port is A stable liquid manufacturing device characterized by having a structure capable of sucking powder and air into a discharge port.
JP651491A 1991-01-23 1991-01-23 Stabilizer manufacturing equipment Expired - Fee Related JPH07103765B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP651491A JPH07103765B2 (en) 1991-01-23 1991-01-23 Stabilizer manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP651491A JPH07103765B2 (en) 1991-01-23 1991-01-23 Stabilizer manufacturing equipment

Publications (2)

Publication Number Publication Date
JPH04306394A true JPH04306394A (en) 1992-10-29
JPH07103765B2 JPH07103765B2 (en) 1995-11-08

Family

ID=11640522

Family Applications (1)

Application Number Title Priority Date Filing Date
JP651491A Expired - Fee Related JPH07103765B2 (en) 1991-01-23 1991-01-23 Stabilizer manufacturing equipment

Country Status (1)

Country Link
JP (1) JPH07103765B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0645177A1 (en) * 1993-09-29 1995-03-29 Heinrich Frings GmbH & Co. KG Device for introducing gas in a liquid

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111890557B (en) * 2020-07-29 2022-02-18 单县中联混凝土有限公司 Husky grey mixer for building

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0645177A1 (en) * 1993-09-29 1995-03-29 Heinrich Frings GmbH & Co. KG Device for introducing gas in a liquid

Also Published As

Publication number Publication date
JPH07103765B2 (en) 1995-11-08

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