JPH02200994A - Stabilizer manufacturing device - Google Patents

Stabilizer manufacturing device

Info

Publication number
JPH02200994A
JPH02200994A JP1019087A JP1908789A JPH02200994A JP H02200994 A JPH02200994 A JP H02200994A JP 1019087 A JP1019087 A JP 1019087A JP 1908789 A JP1908789 A JP 1908789A JP H02200994 A JPH02200994 A JP H02200994A
Authority
JP
Japan
Prior art keywords
bentonite
discharge
discharge ports
water tank
pump
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
JP1019087A
Other languages
Japanese (ja)
Other versions
JP2531774B2 (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 JP1019087A priority Critical patent/JP2531774B2/en
Priority to EP90401844A priority patent/EP0502218A1/en
Priority to CA002019975A priority patent/CA2019975C/en
Publication of JPH02200994A publication Critical patent/JPH02200994A/en
Application granted granted Critical
Publication of JP2531774B2 publication Critical patent/JP2531774B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • B01F23/50Mixing 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
    • 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
    • B01F25/60Pump 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

Abstract

PURPOSE:To obtain stabilizer of uniform composition at a low cost and in short time by arranging a submergible pump equipped with a suction port and a plurality of discharge ports in an agitated water tank and constituting a titled device so as to allow it to suck bentonite or the like into the discharge ports by the discharge negative pressure generated in the discharge ports. CONSTITUTION:A submergible pump 12 is erectly placed on the center of the bottom plate 11 of an agitated water tank 10. In the next step, a suction port 16 is provided at the front center section of an impeller casing 13, and a plurality of discharge ports 17a, 17b and 17c (three pieces in the example) are also provided on the peripheral edge of the suction port 16. The submergible pump 12 and a mud sending pump 40 are driven to suck water into the impeller casing 13. Then, the water flowed into the impeller casing 13 is discharged or spouts into the agitated water tank 10 through the discharge ports 17a, 17b and 17c and exhaust nozzles 18d, 18e and 18f. At this moment during discharging work, negative pressure is generated in discharge openings 18a, 18b and 18c.

Description

【発明の詳細な説明】 (イ)産業上の利用分野 本発明は、掘削作業において用いる安定液(作泥)を、
−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。
[Detailed description of the invention] (a) Industrial application field The present invention provides a method for stabilizing liquid (sludge) used in excavation work.
- It relates to a stabilizer liquid manufacturing device that can produce sludge uniformly and in large quantities.

(ロ)従来の技術 従来、井戸堀り、抗の下穴等の掘削作業を円滑に行うた
め、ベントナイトと水とを混合して製造した安定液(作
泥)を、掘削大中に注入しながら、掘削作業を行ってい
る。
(b) Conventional technology Traditionally, in order to smoothly perform excavation work such as well drilling and pilot holes for pits, a stabilizing liquid (sludge) made by mixing bentonite and water was injected into the excavation chamber. Meanwhile, excavation work is being carried out.

そして、かかる安定液の製造装置として、第6図及び第
7図に示す安定液製造装置B、Cが知られている。
Stabilizing liquid manufacturing apparatuses B and C shown in FIGS. 6 and 7 are known as such stabilizing liquid manufacturing apparatuses.

まず、第6図に示す安定液製造装置Bについて説明する
と、同製造装置Bは、内部に攪拌用ポンプbと送泥用ポ
ンプCとを設置した調整槽aと、内部にミキサーdと具
備する作泥槽Cとから構成されている。
First, the stable liquid manufacturing apparatus B shown in FIG. 6 will be explained. The manufacturing apparatus B is equipped with an adjustment tank a in which a stirring pump b and a slurry pump C are installed, and a mixer d inside. It consists of a mud tank C.

かかる構成において、まず、作泥槽e中に、ベントナイ
トfと水gとを投入するとともに、ミキサーdで攪拌し
て安定液りを製造する。
In this configuration, first, bentonite f and water g are put into the mud making tank e, and are stirred by the mixer d to produce a stable slurry.

さらに、同安定液りを、調整槽a内に投入して撹拌用ポ
ンプbによって攪拌するとともに、同攪拌によって均一
組成となった安定液りを、送泥用バイブiを通して、図
示しない掘削穴へ送給することができる。
Furthermore, the same stable liquid is put into the adjustment tank a and stirred by the stirring pump b, and the stable liquid whose composition has become uniform due to the stirring is passed through the mud feeding vibrator i and into the excavation hole (not shown). can be sent.

一方、第7図に示す安定液製造装置Cについて説明する
と、同製造装置Cは、内部に上記した攬拌用ポンプbよ
り大型の攪拌・作泥用ポンプjと送泥用ポンプCとを設
置した調整槽aから構成される。
On the other hand, to explain the stable liquid manufacturing device C shown in Fig. 7, the manufacturing device C is equipped with a stirring/sludge pump j larger than the above-mentioned stirring pump b and a mud feeding pump C. It consists of a regulating tank a.

かかる構成において、水gを充満してなる調整槽a内に
ベントナイトfを投入するとともに、攪拌・作泥用ポン
プjによって攪拌・作泥するとともに、同攪拌・作泥に
よって均一組成に製造した安定液りを、送泥用バイブ1
を通して、図示しない掘削穴へ送給することができる。
In this configuration, bentonite f is charged into an adjustment tank a filled with water g, and is stirred and mud-formed by a stirring/sludge-forming pump j, and a stable slurry manufactured to have a uniform composition by the stirring/sludge-forming pump j is added. Vibrator 1 for transporting liquid and slurry
It can be fed to an excavation hole (not shown) through the feed hole.

(ハ)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、Cは、未だ、
以下の解決すべき課題を有していた。
(c) Problems to be solved by the invention However, such conventional stabilizer liquid manufacturing apparatuses B and C still have the following problems:
The project had the following issues to be solved.

■第6図に示す安定液製造装置l!Bは、高価なミキサ
ーdを必要とするため、安定液製造装置B自体も高価な
ものとなり、また、いったん、作泥槽eによって作泥し
た後、調整槽aで調整するといった2段階処理であるた
め、均一組成の安定液りを製造するにあたっては、相当
時間を要することになる。
■Stable liquid manufacturing device shown in Figure 6! Since B requires an expensive mixer d, the stabilizer production device B itself is also expensive, and it is a two-step process in which the slurry is made in the slurry tank e and then adjusted in the adjustment tank a. Therefore, it takes a considerable amount of time to produce a stable liquid with a uniform composition.

■一方、第7図に示す安定液製造装置Cは、予め作泥槽
eを用いることなく、直接、米ントナイトrを調整槽a
内に投入し、その後、−個の撹拌・作泥ポンプiのみで
攪拌・作泥するのみであるために、ベントナイトfの溶
解が不完全になり、調整槽aの底部に、多量のベントナ
イ2が残留し、また、安定液り中のベントナイトfの粒
子も大きくなる。
■On the other hand, in the stabilizing liquid manufacturing apparatus C shown in Fig. 7, rice tonite r is directly added to the adjustment tank a without using the mud preparation tank e in advance.
Since the bentonite f is only stirred and mud-formed using - stirring/sludge pumps i, the bentonite f is not completely dissolved, and a large amount of bentonite 2 is deposited at the bottom of the adjustment tank a. remains, and the particles of bentonite f in the stable liquid also become larger.

本発明は、上記問題点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。
SUMMARY OF THE INVENTION An object of the present invention is to provide a stable liquid manufacturing apparatus that can solve the above-mentioned problems.

(ニ)問題点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(
とも一つを撹拌水槽内に開口し、かつ、上記吐出口に、
一端をベントナイト等供給源に接続したベントナイト等
吸入パイプの他端を接続し、吐出口内に生じる吐出負圧
によってベントナイト等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
(D) Means for Solving the Problems The present invention provides a submersible pump having a suction port and a plurality of discharge ports in a stirring water tank.
One of them is opened in the stirring water tank, and the above discharge port is
A device for producing a stable liquid, characterized in that one end of the bentonite suction pipe is connected to a bentonite or the like supply source, and the other end of the bentonite suction pipe is connected to the bentonite or the like suction pipe, so that bentonite or the like can be sucked into the discharge port by the discharge negative pressure generated within the discharge port. This is related.

(ホ)作用及び効果 上記した構成により、本発明は、以下の効果を奏する。(e) Action and effect With the above configuration, the present invention has the following effects.

■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、ベントナイト等吸入パイプを通して、吐出
口内に粉状のベントナイト等を給送して、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。
■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 pass the bentonite etc. through the suction pipe using the ejector effect. Powdered bentonite or the like can be fed into the discharge port and mixed with the discharge water together with air, and then the mixed liquid can be discharged from the discharge port.

かかる動作において、ベントナイト等は、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。
In this operation, bentonite and the like are instantaneously dissolved in the water when mixed with the discharge water, and then are discharged from the discharge port and stirred in all directions.

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。
Therefore, a stable solution with uniform concentration can be produced quickly and in large quantities.

■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、撹拌水槽内において、強力な撹拌流を形成
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, since the mixed liquid discharged from the discharge port contains air, it is possible to form a strong stirring flow in the stirring water tank, further promoting uniformity of the concentration of the above-mentioned stable liquid. Can be done.

(へ)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。
(F) Example Hereinafter, the configuration of the stabilizer manufacturing apparatus A according to the present invention will be specifically explained based on the example shown in the attached drawings.

第1図及び第2図において、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, 10 is a stirring water tank in which water W is stored up to a certain height H.

そして、かかる撹拌水槽10の内部であって、底111
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。
The inside of the stirring water tank 10 has a bottom 111.
A submersible pump 12 is placed upright on the central portion of the tank.

水中ポンプ12は、第1図に示すように、内部にインペ
ラL3a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 that rotatably surrounds an impeller L3a.
and a motor casing 14 that is connected to the impeller casing 13 and has a built-in motor 14a that is connected to the impeller 13a and rotates the impeller 13a.

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.

上記構成において、インペラケーシング13は、第1図
及び第2図に示すように、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 13 has a suction port 16 in the front central part thereof, as shown in FIGS. 1 and 2.
A plurality of (three in this embodiment) discharge ports 17a, 17b, and 17c are provided on the outer periphery of the discharge port.

また、吐出口17a、 17b、 17cには、吐出開
口18a18b、18cを水中ポンプ12から離隔した
位置にもたらすために*l!71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, and 17c are provided with *l! in order to bring the discharge ports 18a, 18b, and 18c to a position separated from the submersible pump 12. 71-shaped jet nozzle 18d
, 18e, and 18f are installed.

そして、以下に説明するように、上記吐出口17a、 
17b、 17cは、ベントナイトと、空気と、水との
混合液を、撹拌水槽IO内に吐出するため用いられる。
As explained below, the discharge port 17a,
17b and 17c are used to discharge a mixed liquid of bentonite, air, and water into the stirring water tank IO.

なお、吐出口17a、 17b、 17cの吐出方向は
、インペラ13a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。
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 13a,
This allows for smooth discharge and feeding of the mixed liquid.

即ち、第1図及び第2図に示すように、吐出口17a、
 17b、 17cの基端には、複数の下部ベントナイ
ト吸入バイブ19a、 19b、 19cの下端が連通
連結されており、同下部ベントナイト吸入バイブ19a
、19b19cの上端は集合筒20に連通連結されてい
る。
That is, as shown in FIGS. 1 and 2, the discharge ports 17a,
The lower ends of a plurality of lower bentonite suction vibes 19a, 19b, 19c are connected to the base ends of the lower bentonite suction vibes 19a, 17b and 17c.
, 19b and 19c are connected to the collecting tube 20 at their upper ends.

そして、集合筒20には、一端を撹拌水槽lOの外部に
設けたベントナイト等供給源としてのベントナイト収納
袋21内のベントナイト22にフィルタ23を介して挿
入した上部ベントナイト吸入バイブ19dの他端が連通
連結されている。
The collecting cylinder 20 is connected to the other end of an upper bentonite suction vibrator 19d inserted through a filter 23 into bentonite 22 in a bentonite storage bag 21 as a supply source of bentonite etc., which is provided at one end outside the stirring water tank IO. connected.

また、上部ベントナイト吸入バイブ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、即ち、ベントナイト22を供給、空気を供給
、またはベントナイト22と空気のいずれも供給しない
形態等を採ることができる。
In addition, an opening/closing valve 19e is provided in the middle of the upper bentonite suction vibe 19d, and by opening and closing the valve 19e, a configuration suitable for the construction conditions at the construction site, that is, supplying bentonite 22, supplying air, Alternatively, a configuration may be adopted in which neither bentonite 22 nor air is supplied.

また、第1図及び第2図に示すように、撹拌水槽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。
In addition, as shown in FIGS. 1 and 2, in one corner of the stirring water tank 10, there is provided a slurry pump 40 having a suction port at the bottom.
One end of a flexible mud feeding hose 42 is connected to a discharge port 41 provided at the top of the mud feeding pump 40, and the other end of the mud feeding hose 42 is connected to a discharge port 41 provided at the top of the mud feeding pump 40. inserted into the drilled hole.

また、第1図に示すように、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。
Further, as shown in FIG. 1, an on-off valve 43 is provided at the upper part of the mud feeding hose 42.

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、第1図及び第2図を参照して説明する。
Next, the procedure for using the stabilizer manufacturing apparatus A having the above configuration will be explained with reference to FIGS. 1 and 2.

まず、上部ベントナイト吸入バイブ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を駆動する。
First, the on-off valve 19e provided in the middle of the upper bentonite suction vibrator 19d is opened, and the on-off valve 43 provided on the mud feeding hose 42 is closed, and the submersible pump 12 and the mud feeding pump 40 are driven.

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。
This drive causes the impeller 13a inside the impeller casing 13 to rotate, and this rotation causes water to be sucked into the impeller casing 13 from the suction port 16.

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17 a + 17 b + 17 
c及び噴出ノズル1.8d、 +8e、 18fを通し
て撹拌水槽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 17 a + 17 b + 17
c and the jet nozzles 1.8d, +8e, and 18f into the stirring water tank 10.

また、上記吐出動作において、吐出開口18a。Further, in the above-mentioned discharge operation, the discharge opening 18a.

18b、18C内には負圧が発生することになる。Negative pressure will be generated within 18b and 18C.

そして、この負圧によって、即ち、エジェクタ効果によ
って、ベントナイト収納袋21内の粉状のベントナイト
22が、上部及び下部ベントナイト吸引バイブ19d 
+集合筒2O−19a、 19b、 19cを通して、
各吐出口17a、 17b、 17c内に空気とともに
噴出され、吐出口17a、 17b、 17c内を流れ
る吐出水に混合され、混合液を生成する。
Then, due to this negative pressure, that is, due to the ejector effect, the powdered bentonite 22 in the bentonite storage bag 21 is transferred to the upper and lower bentonite suction vibes 19d.
+ Through collecting cylinders 2O-19a, 19b, 19c,
It is ejected together with air into each of the discharge ports 17a, 17b, and 17c, and is mixed with the discharged water flowing through the discharge ports 17a, 17b, and 17c, to produce a mixed liquid.

その後、混合液は、噴出ノズル18d、 18g、 1
8fから強力に撹拌水槽10に噴出されることになる。
After that, the mixed liquid is sent to the jet nozzles 18d, 18g, 1
It will be powerfully sprayed into the stirring water tank 10 from 8f.

かかる動作において、ベントナイト22は、吐出水Wへ
の混合の際に、瞬時に水Wに溶解され、その後、吐出口
17a、 17b、 17cを介して噴出ノズル18d
、 IBe、 18!より吐出され、撹拌水槽】O内で
、四方に攪拌されることになる。
In such an operation, the bentonite 22 is instantaneously dissolved in the water W when mixed with the discharge water W, and is then discharged from the jet nozzle 18d through the discharge ports 17a, 17b, and 17c.
, IBe, 18! It is discharged from the tank and stirred in all directions in the stirring water tank.

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。
Therefore, a stable solution with uniform concentration can be produced quickly and in large quantities.

さらに、本実施例において、吐出口17a、 17b。Furthermore, in this embodiment, the discharge ports 17a and 17b.

17cから吐出された混合液は、空気を混入しているた
め、撹拌水槽lO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。
Since the mixed liquid discharged from 17c contains air, it is possible to form a strong stirring flow in the stirring water tank IO, which can further promote uniformity of the concentration of the above-mentioned stabilizing liquid. .

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を通しで、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 mud feeding hose 42 is opened, the stable liquid produced in the above manner is passed through the mud feeding hose 42 from the discharge port 41 of the mud feeding pump 40 to the desired excavation hole, etc. will be supplied quickly and reliably.

しかも、かかる送泥作用に並行して、上記したベントナ
イト混合・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 bentonite mixing and stirring action is continuously performed, so the mud feeding action can be performed continuously while maintaining a uniform concentration of the stabilizing liquid. , can improve the efficiency of excavation work.

なお、上記実施例において、水中ポンプ12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14aの出力軸を下方
に延出して、同延出部にカンタ−を取付けることもでき
る。
In the above embodiment, the submersible pump 12 is shown as having only the impeller 13a, but the output shaft of the motor 14a to which the impeller 13a is attached extends downward, and a canter is provided on the extending part. can also be installed.

この場合は、ベントナイト22と水との混和をさらに促
進することができ、ベントナイト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 bentonite 22 and water can be further promoted, the particles of bentonite 22 can be further made finer, and the stabilizing liquid can be made more uniform.

次に、第3図及び第4図を参照して、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 manufacturing apparatus A according to the present invention will be described with reference to FIGS. 3 and 4.

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
、上記した第1図及び第2図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. Incidentally, parts having the same configuration as the stabilizer liquid cleaning device A shown in FIGS. 1 and 2 described above are indicated by the same reference numerals.

本実施例において、第3図及び第4図に示すように、水
中ポンプI2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、送泥バイブ24の下端を
接続しており、同送泥バイブ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 submersible pump I2 is bent upward, and the lower end of the mud feeding vibrator 24 is attached to the upward bent end. One end of a flexible mud feeding hose 25 is connected to the upper end of the mud feeding vibrator 24, and the other end of the mud feeding hose 25 is inserted into a desired excavation hole.

また、第1図に示すように、送泥バイブ24の上部には
、開閉バルブ26が設けられている。
Further, as shown in FIG. 1, an on-off valve 26 is provided at the upper part of the mud feeding vibe 24.

上記構成によっても、前述した実施例と同様に、強力に
ベントナイト混合・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、上記したベントナイト混合・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。
With the above configuration, it is possible to produce a stable liquid with a uniform concentration by powerfully mixing and stirring bentonite, as in the above-mentioned embodiment. Since the bentonite mixing and stirring action is also performed continuously, the mud feeding action can be performed continuously while maintaining a uniform concentration of the stabilizing liquid, and the efficiency of excavation work can be improved.

さらに、本実施例では、ベントナイト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, charging of bentonite 22, preparation of mud, stirring, and feeding of mud can be performed using a single submersible pump 12, and the stable liquid manufacturing apparatus A can be manufactured at low cost.

次に、第5図を参照して、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.

本変容例は、ベントナイト等供給源を、掘削大中に浮き
上がるベントナイトとするとともに、同ベントナイトを
、重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。
This modified example is characterized by a configuration in which the bentonite etc. supply source is bentonite that floats up during excavation, and the bentonite can be fed from a heavy excavation hole to a new excavation hole.

即ち、第5図において、30.31はそれぞれ新旧掘削
穴であり、重掘削穴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、ベントナイト22が
浮き上がっている。
That is, in FIG. 5, 30 and 31 are the new and old excavation holes, respectively, and there is a concrete foundation 33 in the heavy excavation hole 31.
is poured, and bentonite 22 is floating above it.

一方、新掘削穴30内には未だlle打ちはなされてい
ない。
On the other hand, lle has not yet been drilled into the newly drilled hole 30.

そして、本実施例にかかる安定液製造装置Aは、その上
部ベントナイ)11人バイブ19cの一端を重掘削穴3
1内のベントナイト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 stabilizing liquid manufacturing apparatus A according to this embodiment has an upper bentonite vibrator 19c connected to one end of the vibrator 19c in a heavily excavated hole 3.
At the same time, one end of the mud feeding hose 25 is inserted into the newly excavated hole 30.

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重掘削穴41か
らヘントナイト22を吸引して撹拌水I!lO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, similar to the embodiment described above, the negative pressure generated by the submersible pump 12 is used to suck the hentonite 22 from the heavily excavated hole 41 and stir water I! A stable liquid can be produced by efficiently and uniformly mixing and stirring with water in 1O, and the stable liquid can be continuously fed to the newly drilled hole 30.

そして、かかる安定液を、新掘削穴30の内面に塗布す
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 applying such a stabilizing liquid to the inner surface of the newly excavated hole 30, collapse of the excavated wall can be reliably prevented.

なお、第3図において、32はコンクリート投入装置を
示す。
In addition, in FIG. 3, 32 indicates a concrete charging device.

以上、第1図〜第5図に示す実施例をおいて、ベントナ
イト22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、セメント等にも適用で
きるものである。
As mentioned above, in the embodiments shown in FIGS. 1 to 5, bentonite 22 was used as a contaminant in water, but the device for producing a stable liquid according to the present invention produces a slurry by mixing it with water. It is also applicable to other possible raw materials, such as cement.

即ち、本発明において、ベントナイト等とは、ヘントナ
イト22の他、上記セメント等の原料も含むものである
That is, in the present invention, bentonite and the like include not only hentonite 22 but also raw materials for the above-mentioned cement and the like.

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

第1図は本発明に係る安定液製造装置の一実施例の断面
正面図、第2図は同平面図、第3図及び第4図は他の実
施例の断面正面図と平面図、第5図はその変容例の断面
正面図、第6図及び第7図は従来の安定液製造装置の断
面正面図である。 図中、 A:安定液製造装置 0:撹拌水槽 2:水中ポンプ 6:吸引口 アa 17b、17c  :吐出口 8d、I8s、18f  :噴出ノズル22:ベントナ
イト
FIG. 1 is a cross-sectional front view of one embodiment of the stabilizer production apparatus according to the present invention, FIG. 2 is a plan view thereof, and FIGS. 3 and 4 are a cross-sectional front view and a plan view of other embodiments. FIG. 5 is a cross-sectional front view of a modification thereof, and FIGS. 6 and 7 are cross-sectional front views of a conventional stabilizing liquid manufacturing apparatus. In the figure, A: Stable liquid production device 0: Stirring water tank 2: Submersible pump 6: Suction port a 17b, 17c: Discharge port 8d, I8s, 18f: Spray nozzle 22: Bentonite

Claims (1)

【特許請求の範囲】[Claims] 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
つの吐出口を撹拌水槽内に開口し、かつ、上記吐出口に
、一端をベントナイト等供給源に接続したベントナイト
吸入パイプの他端を接続し、吐出口内に生じる吐出負圧
によってベントナイト等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。
1. A submersible pump having a suction port and a plurality of discharge ports is installed in the stirring water tank, and at least one of these discharge ports is opened into the stirring water tank, and A stable liquid manufacturing device characterized in that one end of the bentonite suction pipe is connected to a supply source of bentonite or the like, and the other end of the bentonite suction pipe is connected to the bentonite suction pipe so that bentonite or the like can be sucked into the discharge port by a discharge negative pressure generated within the discharge port.
JP1019087A 1989-01-27 1989-01-27 Stabilizer manufacturing equipment Expired - Lifetime JP2531774B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP1019087A JP2531774B2 (en) 1989-01-27 1989-01-27 Stabilizer manufacturing equipment
EP90401844A EP0502218A1 (en) 1989-01-27 1990-06-27 Apparatus for producing stabilizing mixture
CA002019975A CA2019975C (en) 1989-01-27 1990-06-27 Apparatus for producing stabilizing mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1019087A JP2531774B2 (en) 1989-01-27 1989-01-27 Stabilizer manufacturing equipment

Publications (2)

Publication Number Publication Date
JPH02200994A true JPH02200994A (en) 1990-08-09
JP2531774B2 JP2531774B2 (en) 1996-09-04

Family

ID=11989674

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1019087A Expired - Lifetime JP2531774B2 (en) 1989-01-27 1989-01-27 Stabilizer manufacturing equipment

Country Status (3)

Country Link
EP (1) EP0502218A1 (en)
JP (1) JP2531774B2 (en)
CA (1) CA2019975C (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9508257D0 (en) * 1995-04-24 1995-06-14 British Nuclear Fuels Plc Removing liquids from tanks

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1139318B (en) * 1959-04-16 1962-11-08 Andreas Weiss Agitator for mixing water or liquid manure with manure
US4645603A (en) * 1977-11-09 1987-02-24 Frankl Gerald P Liquid aeration device and method
GB2095570B (en) * 1981-03-31 1984-10-17 British Nuclear Fuels Ltd An improved apparatus for agitating the contents of storage tanks
DE3321143A1 (en) * 1983-06-10 1984-12-13 Anton 8206 Bruckmühl Humpel Device for treating liquids, in particular liquid manure, preferably situated in containers, and distribution device for this purpose
DE3417039A1 (en) * 1984-02-29 1985-11-14 Kurt Leistner Apparatus for introducing a solid, liquid or gaseous treatment substance/nutrient into water, waste water
DE3407370A1 (en) * 1984-02-29 1985-08-29 Kurt Leistner Apparatus for introducing solid, liquid or gaseous treatment agent/nutrient into water, waste water
DE3621903A1 (en) * 1986-06-30 1988-01-07 Alois Maier Agitator (stirrer)

Also Published As

Publication number Publication date
JP2531774B2 (en) 1996-09-04
CA2019975A1 (en) 1991-12-27
EP0502218A1 (en) 1992-09-09
CA2019975C (en) 1996-07-23

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