JP2003181254A - Method and apparatus for continuous kneading - Google Patents

Method and apparatus for continuous kneading

Info

Publication number
JP2003181254A
JP2003181254A JP2001380611A JP2001380611A JP2003181254A JP 2003181254 A JP2003181254 A JP 2003181254A JP 2001380611 A JP2001380611 A JP 2001380611A JP 2001380611 A JP2001380611 A JP 2001380611A JP 2003181254 A JP2003181254 A JP 2003181254A
Authority
JP
Japan
Prior art keywords
liquid
kneading
tank
powder
continuous
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
JP2001380611A
Other languages
Japanese (ja)
Other versions
JP3780499B2 (en
Inventor
Katsumi Kobayashi
克己 小林
Makoto Fukuyama
誠 福山
Hidenori Isoda
英典 礒田
Shoji Nakama
祥二 中間
Satoru Matsui
悟 松井
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.)
Obayashi Corp
Taiheiyo Materials Corp
Original Assignee
Obayashi Corp
Taiheiyo Materials Corp
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 Obayashi Corp, Taiheiyo Materials Corp filed Critical Obayashi Corp
Priority to JP2001380611A priority Critical patent/JP3780499B2/en
Publication of JP2003181254A publication Critical patent/JP2003181254A/en
Application granted granted Critical
Publication of JP3780499B2 publication Critical patent/JP3780499B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Accessories For Mixers (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To control the supply quantity of a liquid material and a liquid chemical agent in kneading. <P>SOLUTION: A powder tank 1 connected to a vertical mixer 10, a liquid material tank 20, a liquid chemical agent tank 30 and a control panel 60 for controlling the supply quantity of each tank 1, 20 and 30 and adjusting a gelating time are provided. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、土木、建築分野
等で用いられる連続混練方法及びその装置に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous kneading method and its apparatus used in the fields of civil engineering and construction.

【0002】[0002]

【従来の技術】従来、地盤改良の工事などにおいて、ペ
ースト状混練物が用いられている。この混練物は、一般
的には、パン型(たらい型ともいう)2槽式のグラウト
ミキサを用いて製造されている。
2. Description of the Related Art Conventionally, paste-like kneaded materials have been used in ground improvement work and the like. This kneaded product is generally manufactured using a pan-type (also called a tub-type) two-tank type grout mixer.

【0003】このミキサでは、上部の槽に各1バッチ分
ずつそれぞれ計算してある粉体、水及び薬剤を投入して
混練する。そして、一定時間混練した後、上部の槽の一
部を開口して混練物を下部の槽に移動させる。下部の槽
では、材料分離が起こらないように攪拌しながら混練物
を圧送装置へ供給し、注入等を行っている。
In this mixer, powder, water and chemicals, which have been calculated for each batch, are put into the upper tank and kneaded. Then, after kneading for a certain time, a part of the upper tank is opened to move the kneaded product to the lower tank. In the lower tank, the kneaded material is supplied to the pressure-feeding device while being stirred so that material separation does not occur, and injection is performed.

【0004】しかし、このミキサを用いる場合には、次
の様な問題がある。 (1)練り混ぜ作業が繁雑で手間がかかる。 (2)練りあがった混練物は、余ると全て廃棄処分しなけ
ればならない。 (3)添加する薬剤量の調整が合わないと、1バッチ全て
廃棄しいなければならない。
However, the use of this mixer has the following problems. (1) Kneading work is complicated and time-consuming. (2) Any kneaded mixture that has been kneaded must be discarded when it remains. (3) If the amount of chemicals added is not adjusted, one batch must be discarded.

【0005】(4)途中で作業が中断せざるを得ない場合
に、装置の洗浄に手間がかかると共に、廃棄量も多くな
る。これを防ぐために、バッチを小さくすると、水や薬
剤等の計量回数が増え、作業がより煩雑になる。 (5)バッチ式なので、連続して混練できない。そのた
め、多量の混練物を必要とする場合には、水や薬剤等の
計量回数が増え、作業がより煩雑になる。 (6)地盤注入工事を行っている時に、岩盤のクラックか
ら注入材が漏れ出すことがあるが、この場合には、凝結
時間及び又はゲルタイム(以下、単に「ゲルタイム」と
いう)を瞬時に調整し、ゲルタイムの短い混練物にしな
ければならい。しかし、このバッチ式ではこのような対
応は無理であるので、連続して混練できる連続混練装置
が開発されている(特開平5−345121号公報参
照)。
(4) If the work has to be interrupted in the middle of the process, it takes a lot of time to clean the device and the amount of waste increases. In order to prevent this, if the batch is made smaller, the number of times water, chemicals, etc. are measured increases, and the work becomes more complicated. (5) Since it is a batch type, it cannot be kneaded continuously. Therefore, when a large amount of kneaded material is required, the number of times water, chemicals, etc. are measured increases, and the work becomes more complicated. (6) The injection material may leak from the cracks in the rock during the ground injection work. In this case, the setting time and / or gel time (hereinafter simply referred to as "gel time") should be adjusted instantaneously. , It should be a kneaded product with a short gel time. However, since such a correspondence is not possible in this batch type, a continuous kneading device capable of continuously kneading has been developed (see Japanese Patent Laid-Open No. 5-345121).

【0006】この装置は、原料投入口より移送ケーシン
グに供給される被混練物を混練ケーシングに移送する移
送スクリュウと、該混練ケ−シングの導入部に設置した
着脱可能な流路制御板と、該混練ケーシング内に設置さ
れ移送スクリュウと同軸の混練羽根とを備えている。
This apparatus comprises a transfer screw for transferring the material to be kneaded supplied from the material input port to the transfer casing to the kneading casing, and a detachable flow path control plate installed at the introduction part of the kneading casing. The kneading blade is installed in the kneading casing and has a kneading blade coaxial with the transfer screw.

【0007】[0007]

【発明が解決しようとする課題】従来例では、薬剤は予
め粉体又は水に添加された状態で、連続混練装置に供給
するので、混練時に薬剤の量を調整することができな
い。そのため、薬剤量が足りない場合、該薬剤を別途計
量して添加しなければならないが、その場合には、粉体
混合装置、又は、液体混合装置が別途必要となり現実的
ではない。
In the conventional example, the chemicals are added to the powder or water in advance in the state of being supplied to the continuous kneading apparatus, so that the quantity of the chemicals cannot be adjusted during the kneading. Therefore, when the amount of the drug is insufficient, the drug must be separately measured and added, but in that case, a powder mixing device or a liquid mixing device is additionally required, which is not realistic.

【0008】逆に前記薬剤が多い場合には、粉体又は水
を添加した後混合しなければならないが、その場合に
は、粉体又は液体混合装置及びそれぞれの容器を、必要
以上に大きくしなければならない。要するに、従来例の
連続混練装置では、バッチ式と同様に運転中に、ゲルタ
イムを調整することができないので、作業現場の変化に
対応する、好適な混練物を製造することができない。
On the contrary, when the amount of the above-mentioned chemicals is large, it is necessary to add the powder or water and then mix them. In that case, the powder or liquid mixing device and each container are made larger than necessary. There must be. In short, in the continuous kneading apparatus of the conventional example, the gel time cannot be adjusted during operation as in the case of the batch type, so that a suitable kneaded material corresponding to changes in the work site cannot be manufactured.

【0009】本発明は、上記事情に鑑み、混練時に液状
物と液状薬剤の供給量を調整できるようにすることを目
的とする。
In view of the above circumstances, an object of the present invention is to make it possible to adjust the supply amounts of a liquid substance and a liquid medicine during kneading.

【0010】[0010]

【課題を解決するための手段】この発明は、粉体と液状
物と液状薬剤とを混合し、混練物を連続製造する方法に
おいて;前記液状物と液状薬剤の供給量を、それぞれ個
別に制御することを特徴とする。
SUMMARY OF THE INVENTION The present invention is a method for continuously producing a kneaded product by mixing a powder, a liquid substance, and a liquid medicine; controlling the supply amounts of the liquid substance and the liquid medicine individually. It is characterized by doing.

【0011】この発明は、それぞれ別個に収容されてい
る粉体と液状物と液状薬剤とを混練手段に供給して混合
し、混練物を連続製造する方法において;連続混練中
に、前記液状物の供給量と前記液状薬剤の供給量を調整
し、ゲルタイムを調整することを特徴とする。
The present invention relates to a method for continuously producing a kneaded product by supplying powder, a liquid substance, and a liquid drug, which are separately stored, to a kneading means to mix them, and the liquid substance is continuously produced during the continuous kneading. It is characterized in that the gel time is adjusted by adjusting the supply amount of the liquid medicine and the supply amount of the liquid medicine.

【0012】この発明は、粉体と液状物と液状薬剤とを
混練手段に供給し、混練物を連続製造する連続混練装置
において;前記混練手段に接続された、粉体タンク、液
状物タンク及び液状薬剤タンクと、前記各タンクの供給
量を個別に制御する制御手段と、を備えていることを特
徴とする。
The present invention relates to a continuous kneading device for continuously producing a kneaded product by supplying a powder, a liquid substance and a liquid chemical to a kneading device; a powder tank, a liquid substance tank and a liquid tank connected to the kneading device. It is characterized by comprising a liquid medicine tank, and a control means for individually controlling the supply amount of each tank.

【0013】この発明は、粉体と液状物と液状薬剤とを
混練手段に供給し、混練物を連続製造する連続混練装置
において;前記混練手段に接続された、粉体タンク、液
状物タンク及び液状薬剤タンクと、前記各タンクの供給
量を個別に制御するとともに、連続混練中にゲルタイム
を調整する制御手段と、を備えていることを特徴とす
る。
The present invention relates to a continuous kneading device for continuously producing a kneaded material by supplying a powder, a liquid material and a liquid chemical to a kneading means; a powder tank, a liquid material tank, and a tank connected to the kneading means. It is characterized by comprising a liquid medicine tank and a control means for individually controlling the supply amount of each tank and adjusting the gel time during continuous kneading.

【0014】[0014]

【発明の実施の形態】本発明は、粉体と液状物と液状薬
剤をそれぞれ別個のタンクに収容し、各タンクからの供
給量を別個に制御するものである。そのため、この連続
混練装置では、運転中でも任意に液状薬剤の供給量を個
別に調整できるので、ゲルタイム等所望の物性値の混練
物を所望量得ることができる。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, a powder, a liquid substance, and a liquid medicine are contained in separate tanks, and the supply amount from each tank is controlled separately. Therefore, in this continuous kneading device, the supply amount of the liquid chemical can be individually adjusted even during operation, so that a desired amount of the kneaded product having desired physical properties such as gel time can be obtained.

【0015】[0015]

【実施例】この発明の実施例を図1〜図3により説明す
る。粉体タンク1には、粉体Fが収容されている。この
粉体Fとして、例えば、ポルトランドセメント、アルミ
ナセメント、コロイドセメント、フライアッシュセメン
ト、高炉セメント、エコセメント等のセメント、ポゾラ
ン物質、スラグ粉末等の潜在水硬牲物質、セメント系固
化材、急硬剤やセメント膨張材等の粉体混和剤(材)、
細骨材若しくはこれらの2種以上の混合物等が用いられ
る。この粉体タンク1の下部には、定量供給装置2が設
けられている。この装置2は、モータ2mにより駆動さ
れ、該タンク1内の粉体を定量づづ竪型ミキサ10に供
給する。
Embodiments of the present invention will be described with reference to FIGS. The powder F is stored in the powder tank 1. Examples of the powder F include, for example, cement such as Portland cement, alumina cement, colloidal cement, fly ash cement, blast furnace cement, ecocement, pozzolanic substance, latent hydraulic substance such as slag powder, cement-based solidifying material, and rapid hardening. Powder admixtures (materials) such as agents and cement expanders,
Fine aggregate or a mixture of two or more kinds of these is used. A fixed quantity supply device 2 is provided below the powder tank 1. The device 2 is driven by a motor 2m and supplies the powder in the tank 1 to the vertical mixer 10 in a fixed quantity.

【0016】粉体タンク1の出口1bは、竪型ミキサ1
0の上部入口10aに連続している。該ミキサ10は、
ケーシング本体11と、該ケーシング本体11と同心状
の回転軸12と、該回転軸12に固定された羽根13〜
15と、を備えている。前記回転軸12は、モータ10
mにより回転する。
The outlet 1b of the powder tank 1 has a vertical mixer 1
0 is connected to the upper inlet 10a. The mixer 10 is
A casing main body 11, a rotary shaft 12 concentric with the casing main body 11, and blades 13 fixed to the rotary shaft 12.
15 and. The rotating shaft 12 is a motor 10
Rotate by m.

【0017】ケーシング本体11の上部10Aは逆円錐
台状に形成され、該上部10Aには、片羽根13が収容
されている。この片羽根13は、上部10A内で回転
し、粉体タンク1から供給される粉体Fを均一に胴部1
1B内に落下させる。
An upper part 10A of the casing body 11 is formed in an inverted truncated cone shape, and a single blade 13 is housed in the upper part 10A. The single blade 13 rotates in the upper portion 10A to uniformly distribute the powder F supplied from the powder tank 1.
Drop into 1B.

【0018】胴部11Bは、直筒状に形成され、該胴部
11Bには、攪拌羽根14が収容されている。 ケーシ
ング本体11の下部11Cは、前記胴部11Bより小径
の円筒状に形成され、該下部11Cの内面には、櫛歯状
の邪魔板11Dが設けられ、該邪魔板11Dの空間部に
対応するように、練り羽根15が配置されている。前記
下部11Cは、下部槽16に臨んでおり、該下部槽16
の上部には、出口16bが設けられている。
The body 11B is formed in a straight tube shape, and the stirring blade 14 is housed in the body 11B. A lower portion 11C of the casing body 11 is formed in a cylindrical shape having a diameter smaller than that of the body portion 11B, and a comb tooth-shaped baffle plate 11D is provided on an inner surface of the lower portion 11C and corresponds to a space part of the baffle plate 11D. Thus, the kneading blades 15 are arranged. The lower portion 11C faces the lower tank 16 and
An outlet 16b is provided on the upper part of the.

【0019】胴部11Bの下部側には、混合液入口18
が設けられている。この混合液入口18は、図3に示す
ように、接線方向で、かつ、上向きに傾斜している。こ
の傾斜角度θは、必要に応じて決定されるが、例えば、
傾斜角度θとして1度〜30度が選ばれる。
A mixed liquid inlet 18 is provided on the lower side of the body 11B.
Is provided. As shown in FIG. 3, the mixed liquid inlet 18 is tangential and inclined upward. This inclination angle θ is determined as necessary, but for example,
The inclination angle θ is selected to be 1 degree to 30 degrees.

【0020】液状物タンク20には、液状物W、即ち、
液体を含有し流動性を有するもの、が収容されている。
この液状物Wとして、例えば、水や溶液等の液体、懸濁
液、懸濁質、エマルジョン、ペースト等、が用いられ
る。この液状物タンク20の出口は、モータ21mの付
いたポンプ21の入口に接続され、該ポンプ21の出口
は第1パイプ23を介して混合液入口18に連結されて
いる。
In the liquid material tank 20, the liquid material W, that is,
It contains a liquid and has fluidity.
As the liquid material W, for example, a liquid such as water or a solution, a suspension, a suspension, an emulsion, a paste, or the like is used. The outlet of the liquid material tank 20 is connected to the inlet of a pump 21 equipped with a motor 21m, and the outlet of the pump 21 is connected to the mixed liquid inlet 18 via a first pipe 23.

【0021】液状薬剤タンク30には、液状薬剤Mが収
容されている。この液状薬剤Mとして、例えば、急結剤
を含む急硬材や遅延剤等の凝結時間調整剤、分散剤等、
ゲルタイム調整剤、膨張剤、防錆剤、防凍剤、着色材、
水和熱抑制剤、増粘剤、保水剤、収縮低減剤、セメント
ポリマ、フィラ、水中不分離性混和剤等の混和剤や混和
材等、が用いられる。
A liquid medicine M is stored in the liquid medicine tank 30. Examples of the liquid medicine M include a setting agent such as a quick-hardening material containing a quick-setting agent and a retarder, a dispersant, and the like.
Gel time adjuster, swelling agent, anticorrosive agent, antifreeze agent, coloring material,
Admixtures and admixtures such as a heat of hydration inhibitor, a thickener, a water retention agent, a shrinkage reducing agent, a cement polymer, a filler, and an inseparable admixture in water are used.

【0022】この液状薬剤タンク30の出口は、モータ
31mの付いたポンプ31の入口に接続され、該ポンプ
31の出口は第2パイプ33を介して第1パイプ23の
合流部33pに接続されている。 液状物タンク20の
液状物Wと液状薬剤タンク30の液状薬剤Mとは、前記
合流部33pで混合され混合液W・Mとなって混合液入
口18に圧送される。
The outlet of the liquid medicine tank 30 is connected to the inlet of a pump 31 equipped with a motor 31m, and the outlet of the pump 31 is connected to a merging portion 33p of the first pipe 23 via a second pipe 33. There is. The liquid substance W in the liquid substance tank 20 and the liquid drug M in the liquid drug tank 30 are mixed in the merging portion 33p to form a mixed liquid W · M, which is pressure-fed to the mixed liquid inlet 18.

【0023】下部槽16の出口16bは、滞留槽40を
介してモータ41m付きダイヤフラムポンプ41に連結
されている。ダイヤフラムポンプ41は、圧送装置であ
り、流量計50を介してノズル55に接続されている。
この流量計50は、ポンプ41からの混練物100の吐
出量を検出する。
The outlet 16b of the lower tank 16 is connected to a diaphragm pump 41 with a motor 41m via a retention tank 40. The diaphragm pump 41 is a pressure feeding device and is connected to the nozzle 55 via the flowmeter 50.
The flow meter 50 detects the discharge amount of the kneaded material 100 from the pump 41.

【0024】制御盤60には、コンピュータ61が配設
されており、該コンピュータ61には、定量供給装置2
のモータ2m、竪型ミキサ10のモータ10m、ダイヤ
フラムポンプ41のモータ41m、ポンプ21のモータ
21m、ポンプ31のモータ31m、がそれぞれインバ
ータを介して接続されている。なお、70は、操作パネ
ルで、前記コンピュータ61に接続されている。このパ
ネル70には、混練を開始させるスタートボタン71
と、水洗いを開始させる洗浄ボタン72と、運転を停止
させるストップボタン73と、が配設されている。
The control panel 60 is provided with a computer 61, and the computer 61 has a fixed amount supply device 2
2m, the vertical mixer 10 motor 10m, the diaphragm pump 41 motor 41m, the pump 21 motor 21m, and the pump 31 motor 31m are respectively connected via inverters. An operation panel 70 is connected to the computer 61. This panel 70 has a start button 71 for starting kneading.
A washing button 72 for starting washing with water and a stop button 73 for stopping the operation are provided.

【0025】次に、本実施例の作動について説明する。
操作パネル70により、水(液状物W)設定量(100
%)の内割りとして、添加剤(液状薬剤M)を比率設定
する。そうすると、コンピュータ61が二液の流量を自
動設定する。
Next, the operation of this embodiment will be described.
Using the operation panel 70, set amount of water (liquid material W) (100
%, The additive (liquid medicine M) is set as a ratio. Then, the computer 61 automatically sets the flow rates of the two liquids.

【0026】操作パネル70のスタートボタン71を押
すと、各モータが始動し、粉体タンク1から定量ずつ粉
体Fが竪型ミキサ10にが投入されると共に、液状物タ
ンク20の液状物W、液状薬剤タンク30の液状薬剤M
も前記ミキサ10に供給される。
When the start button 71 of the operation panel 70 is pressed, each motor is started, and the powder F is fed into the vertical mixer 10 in a fixed amount from the powder tank 1 and the liquid material W in the liquid material tank 20 is supplied. , Liquid medicine M in the liquid medicine tank 30
Is also supplied to the mixer 10.

【0027】ミキサ10の上部10Aに流入した粉体F
は、片羽根13に掻き落とされながら胴部11B内に落
下する。液状物Wと液状薬剤Mとは、混合部33pで混
合されて混合液W・Mとなって混合液入口18からミキ
サ10内に圧送される。この時、混合液入口18が接線
方向で、かつ、上向きに傾斜しているので、該混合液W
・Mは旋回流A10となりながら胴部11Bの内面に沿
って上昇し、粉体Fと混合される。そのため、胴部11
Bの内面は、前記旋回流A10に洗われるので、粉体F
が内面に付着するのを防止することができる。
Powder F flowing into the upper portion 10A of the mixer 10
Falls into the body portion 11B while being scraped off by the single blade 13. The liquid substance W and the liquid drug M are mixed in the mixing portion 33p to form a mixed liquid W · M, which is pressure-fed from the mixed liquid inlet 18 into the mixer 10. At this time, since the mixed liquid inlet 18 is tangential and inclined upward, the mixed liquid W
The M rises along the inner surface of the body 11B while forming the swirling flow A10, and is mixed with the powder F. Therefore, the body 11
Since the inner surface of B is washed by the swirling flow A10, the powder F
Can be prevented from adhering to the inner surface.

【0028】胴部11Bで混合攪拌され、製造された混
練物100は、練り羽根15により更に攪拌されながら
下部槽16に落下し、出口16bから滞留槽40内に供
給される。
The kneaded material 100 produced by mixing and stirring in the body portion 11B drops into the lower tank 16 while being further stirred by the kneading blade 15, and is supplied into the retention tank 40 from the outlet 16b.

【0029】滞留槽40内の混練物100は、ダイヤフ
ラムポンプ41によりノズル55に圧送される。この
時、混練物100の圧送量は、流量計50により計測さ
れており、その計測値はコンピュータ61へ送出され
る。コンピュータ61は、前記計測値と予め設定されて
いる設計値とが一致しないときには、モータ41m、モ
ータ2m、モータ10m、モータ21m、モータ31m
の回転数を変更させてダイヤフラムポンプ41、定量供
給装置2、ポンプ21、ポンプ31及び竪型ミキサ10
を変速させ、混練物の吐出量が設計値になる様に調整す
る。
The kneaded material 100 in the retention tank 40 is pressure-fed to the nozzle 55 by the diaphragm pump 41. At this time, the amount of the kneaded material 100 fed under pressure is measured by the flow meter 50, and the measured value is sent to the computer 61. When the measured value and the preset design value do not match, the computer 61 determines that the motor 41m, the motor 2m, the motor 10m, the motor 21m, and the motor 31m.
The diaphragm pump 41, the constant quantity supply device 2, the pump 21, the pump 31, and the vertical mixer 10 are changed by changing the rotation speed of
And adjust so that the discharge amount of the kneaded material becomes the designed value.

【0030】連続混練中に、環境が急変した場合、例え
ば、地盤注入材工事中に岩盤のクラックから注入材が漏
れだした場合には、液状薬剤タンク30から供給される
凝結時間調整剤(ゲルタイム調整剤)の量を瞬時に増や
し(硬化促進剤の場合)若しくは減らし(遅延剤の場
合)、凝結時間及びゲルタイムの短かい混練物を製造
し、供給する。こらにより注入材の漏れを止めることが
できる。
When the environment suddenly changes during continuous kneading, for example, when the injection material leaks from a crack in the rock during the ground injection material construction, a setting time adjusting agent (gel time) supplied from the liquid chemical tank 30 is used. The amount of the modifier is instantly increased (in the case of a curing accelerator) or decreased (in the case of a retarder), and a kneaded product having a short setting time and a short gel time is produced and supplied. This can prevent the injection material from leaking.

【0031】注入材の漏れが止まった後、再び液状物と
液状薬剤の供給量を調整し、混練物のゲルタイムを元に
戻す。この様に、作業現場の環境に対応して自由にゲル
タイムを調整することができる。
After the injection material has stopped leaking, the supply amounts of the liquid material and the liquid medicine are adjusted again to restore the gel time of the kneaded material to the original value. In this way, the gel time can be adjusted freely according to the environment of the work site.

【0032】混練作業が終了したときには、ストップボ
タン73を押して運転を停止する。運転停止後、洗浄ボ
タン72を押してミキサ10等の水洗いを行う。このボ
タン72を押すと、モータ21m、41m、10mが始
動し、液状物タンク20内の水Wがミキサ10内に噴射
される。この時、モータ10mは、混練時より高速に回
転するので、該水Wが羽根13〜15、胴部11B、邪
魔板11D及び下部槽16に付着した粉体Fを効率よく除
去する。又、混合液入口18は接線方向で、かつ、上向
きに傾斜しているので、水Wは胴部11Bの内面に沿っ
て旋回しながら上昇し、該内面に付着している混練物を
洗い流す。
When the kneading operation is completed, the stop button 73 is pressed to stop the operation. After the operation is stopped, the washing button 72 is pressed to wash the mixer 10 and the like with water. When the button 72 is pressed, the motors 21m, 41m, 10m are started, and the water W in the liquid material tank 20 is injected into the mixer 10. At this time, since the motor 10m rotates at a higher speed than during kneading, the water W efficiently removes the powder F adhered to the blades 13 to 15, the body portion 11B, the baffle plate 11D and the lower tank 16. Further, since the mixed liquid inlet 18 is tangential and inclined upward, the water W rises while swirling along the inner surface of the body portion 11B to wash away the kneaded material adhering to the inner surface.

【0033】ミキサ10内の水Wは、滞留槽40内に流
下し、ダイヤフラムポンプ41を介してノズル55から
放出される。その為、ダイヤフラムポンプ41、流量計
50、ノズル55等は前記水Wにより洗浄され、混練物
が除去される。
The water W in the mixer 10 flows down into the retention tank 40 and is discharged from the nozzle 55 via the diaphragm pump 41. Therefore, the diaphragm pump 41, the flowmeter 50, the nozzle 55, etc. are washed with the water W to remove the kneaded material.

【0034】この発明の実施例は、上記に限定されるも
のではなく、例えば、次の様にしても良い。 (1)粉体と、水及び一種又は二種以上の液状混和材を混
練しても良い。 (2)二台の連続混練装置を配設し、一方の連続混練装置
により、粉体の凝結時間調整剤と、水及び1種又は2種
以上の液状混和剤を混合して混合物を製造し、該混合物
に他方の連続混練装置により練り混ぜた水硬牲粉体混合
物を混合して混練しても良い。
The embodiment of the present invention is not limited to the above, and may be, for example, as follows. (1) The powder may be kneaded with water and one or more liquid admixtures. (2) Two continuous kneading devices are provided, and one of the continuous kneading devices is used to prepare a mixture by mixing the powder setting time adjusting agent, water and one or more liquid admixtures. Alternatively, the hydraulic powder mixture kneaded by the other continuous kneading device may be mixed and kneaded with the mixture.

【0035】(3)二台の連続混練装置を配置し、各装置
の操作パネルを連動切換ボタンを介して連結する。この
ボタンを押して連動操作に切りかえると、一方の装置の
操作パネルを操作するだけで、他方の装置の操作を同時
に行うことができる。従って、一方の操作パネルにより
運転の開始や停止を指示だけで、他方の装置も始動した
り停止したりする。
(3) Two continuous kneading devices are arranged, and the operation panel of each device is connected via the interlocking switching button. When this button is pressed to switch to the interlocked operation, the operation of the other device can be simultaneously performed by operating the operation panel of the one device. Therefore, only by instructing the start or stop of the operation from one operation panel, the other device is also started or stopped.

【0036】[0036]

【発明の効果】この発明は、以上のように構成したの
で、液状物と液状薬剤との供給量を個別に調整すること
ができる。そのため、運転中でも液状物の供給量と液状
薬剤の供給量とを調整し、任意の混合比の混練物を得る
ことができるので、ゲルタイム等所望の物性値の混練物
を所望量得ることができる。
Since the present invention is constructed as described above, it is possible to individually adjust the supply amounts of the liquid substance and the liquid medicine. Therefore, it is possible to obtain a kneaded product having a desired physical property value such as gel time by adjusting the supply amount of the liquid substance and the supply amount of the liquid drug even during operation and obtaining a kneaded product having an arbitrary mixing ratio. .

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

【図1】本発明の実施例を示すフロー図である。FIG. 1 is a flow chart showing an embodiment of the present invention.

【図2】竪型ミキサの拡大縦断面図である。FIG. 2 is an enlarged vertical cross-sectional view of a vertical mixer.

【図3】図2のIII-III線拡大断面図である。FIG. 3 is an enlarged sectional view taken along line III-III of FIG.

【符号の説明】[Explanation of symbols]

1 粉体タンク 10 竪型ミキサ 20 液状物タンク 21m モータ 30 液状薬剤タンク 31m モータ 40 滞留槽 50 流量計 60 制御盤 70 操作パネル 100 混練物 1 powder tank 10 Vertical mixer 20 Liquid tank 21m motor 30 Liquid drug tank 31m motor 40 retention tank 50 flow meter 60 control panel 70 Control panel 100 kneaded products

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B28C 5/16 B28C 5/16 7/12 7/12 (72)発明者 福山 誠 東京都中央区日本橋本町4丁目8番15号 太平洋マテリアル株式会社内 (72)発明者 礒田 英典 東京都中央区日本橋本町4丁目8番15号 太平洋マテリアル株式会社内 (72)発明者 中間 祥二 東京都港区港南2−15−2 株式会社大林 組東京本社内 (72)発明者 松井 悟 東京都千代田区西神田三丁目8番1号 大 平洋マテリアル株式会社内 Fターム(参考) 4G035 AA23 AA28 AB46 AE02 AE13 4G037 AA02 AA03 AA18 BA05 BB01 BB15 BB23 BC04 BD05 BE02 EA04 4G056 AA07 CB35 CC12 4G078 AA10 AA11 AA20 AB01 BA05 BA09 BA11 CA01 CA05 CA12 CA20 DA01 DA03 DA28 DA30 DB01 EA10 Front page continuation (51) Int.Cl. 7 identification code FI theme code (reference) B28C 5/16 B28C 5/16 7/12 7/12 (72) Inventor Makoto Fukuyama 4-8 Nihonbashihonmachi, Chuo-ku, Tokyo No. 15 within Pacific Materials Co., Ltd. (72) Inventor Hidenori Isoda 4-8-15 Nihonbashihonmachi, Chuo-ku, Tokyo Inside Pacific Materials Co., Ltd. (72) Inventor Shoji 2-15-2 Konan, Minato-ku, Tokyo Stocks Obayashi Corporation Tokyo Head Office (72) Inventor Satoru Matsui 3-8-1, Nishikanda, Chiyoda-ku, Tokyo F-term in Daiheiyo Material Co., Ltd. (reference) 4G035 AA23 AA28 AB46 AE02 AE13 4G037 AA02 AA03 AA18 BA05 BB01 BB15 BB23 BC04 BD05 BE02 EA04 4G056 AA07 CB35 CC12 4G078 AA10 AA11 AA20 AB01 BA05 BA09 BA11 CA01 CA05 CA12 CA20 DA01 DA03 DA28 DA30 DB01 EA10

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】粉体と液状物と液状薬剤とを混合し、混練
物を連続製造する方法において;前記液状物と液状薬剤
の供給量を、それぞれ個別に制御することを特徴とする
連続混練方法。
1. A method for continuously producing a kneaded product by mixing a powder, a liquid and a liquid medicine; continuous kneading, wherein the amounts of the liquid and the liquid medicine supplied are individually controlled. Method.
【請求項2】それぞれ別個に収容されている粉体と液状
物と液状薬剤とを混練手段に供給して混合し、混練物を
連続製造する方法において;連続混練中に、前記液状物
の供給量と前記液状薬剤の供給量を調整し、ゲルタイム
を調整することを特徴とする連続混練方法。
2. A method for continuously producing a kneaded product by supplying a powder, a liquid substance, and a liquid drug, which are separately stored, to a kneading means to mix them, and to supply the liquid substance during continuous kneading. A continuous kneading method, characterized in that the gel time is adjusted by adjusting the amount and the supply amount of the liquid medicine.
【請求項3】液状物と液状薬剤の供給量の合計が、一定
となるように制御されることを特徴とする請求項1、又
は、2記載の連続混練方法。
3. The continuous kneading method according to claim 1, wherein the total supply amount of the liquid substance and the liquid medicine is controlled to be constant.
【請求項4】液状物と液状薬剤とが、粉体と混合する前
に予め混合されていることを特徴とする請求項1、又
は、2記載の連続混練方法。
4. The continuous kneading method according to claim 1 or 2, wherein the liquid substance and the liquid medicine are mixed in advance before mixing with the powder.
【請求項5】粉体と液状物と液状薬剤とを混練手段に供
給し、混練物を連続製造する連続混練装置において;前
記混練手段に接続された、粉体タンク、液状物タンク及
び液状薬剤タンクと、 前記各タンクの供給量を個別に制御する制御手段と、 を備えていることを特徴とする連続混練装置。
5. A continuous kneading apparatus for supplying a powder, a liquid and a liquid medicine to a kneading means to continuously produce a kneaded material; a powder tank, a liquid material tank and a liquid medicine connected to the kneading means. A continuous kneading apparatus comprising: a tank; and a control unit that individually controls the supply amount of each tank.
【請求項6】粉体と液状物と液状薬剤とを混練手段に供
給し、混練物を連続製造する連続混練装置において;前
記混練手段に接続された、粉体タンク、液状物タンク及
び液状薬剤タンクと、 前記各タンクの供給量を個別に制御するとともに、連続
混練中にゲルタイムを調整する制御手段と、 を備えていることを特徴とする連続混練装置。
6. A continuous kneading apparatus for continuously producing a kneaded product by supplying a powder, a liquid and a liquid medicine to the kneading means; a powder tank, a liquid material tank and a liquid medicine connected to the kneading means. A continuous kneading apparatus comprising: a tank; and a control unit for individually controlling the supply amount of each tank and adjusting a gel time during the continuous kneading.
【請求項7】前記液状物タンクと液状薬剤タンクとが、
合流手段を介して混練手段に接続されていることを特徴
とする請求項5、又は、6記載の連続混練装置。
7. The liquid material tank and the liquid chemical tank,
7. The continuous kneading device according to claim 5 or 6, wherein the continuous kneading device is connected to the kneading means via a merging means.
【請求項8】混練手段は、上部に粉体供給口が設けら
れ、胴部に混合液入口が設けられている竪型ミキサであ
ることを特徴とする請求項5、又は、6記載の連続混練
装置。
8. The continuous mixer according to claim 5, wherein the kneading means is a vertical mixer having a powder supply port provided on an upper portion and a mixed liquid inlet provided on a body part. Kneading equipment.
【請求項9】混合液入口が、接線方向、かつ、上向きに
傾斜して設けられているを特徴とする請求項8記載の連
続混練装置。
9. The continuous kneading device according to claim 8, wherein the mixed liquid inlet is provided so as to be inclined in a tangential direction and upward.
【請求項10】請求項5、又は、6記載の連続混練物の
製造装置による混練物の連続混練方法であって;二台の
混練物の連続製造装置を配設し、 一方の該装置により、粉体の凝結時間調整剤と、水及び
1種又は2種以上の液状混和剤を混合して混合物を製造
し、該混合物に他方の該装置により練り混ぜた水硬牲粉
体混合物を混合して混練することを特徴とする連続混練
方法。
10. A method for continuously kneading a kneaded material by the continuous kneaded material manufacturing apparatus according to claim 5 or 6, wherein two kneaded material continuous manufacturing apparatuses are provided, and one of the apparatuses is used. , A powder setting time adjusting agent, water and one or more liquid admixtures are mixed to produce a mixture, and the hydraulic mixture of the other powder is kneaded by the device. A continuous kneading method which comprises kneading and kneading.
JP2001380611A 2001-12-13 2001-12-13 Continuous kneading method and apparatus Expired - Fee Related JP3780499B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001380611A JP3780499B2 (en) 2001-12-13 2001-12-13 Continuous kneading method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001380611A JP3780499B2 (en) 2001-12-13 2001-12-13 Continuous kneading method and apparatus

Publications (2)

Publication Number Publication Date
JP2003181254A true JP2003181254A (en) 2003-07-02
JP3780499B2 JP3780499B2 (en) 2006-05-31

Family

ID=27591583

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012111218A1 (en) * 2011-02-17 2012-08-23 新東工業株式会社 Tank apparatus, circulating-type dispersion system, and dispersion method
CN103768972A (en) * 2014-01-27 2014-05-07 黄山晶品建筑集料科技有限公司 Humidification stirring system
CN113230935A (en) * 2021-05-24 2021-08-10 四川省威沃敦化工有限公司 Low intelligent production facility that hinders degree of depth acidizing fluid densifier uses

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012111218A1 (en) * 2011-02-17 2012-08-23 新東工業株式会社 Tank apparatus, circulating-type dispersion system, and dispersion method
JP5895853B2 (en) * 2011-02-17 2016-03-30 新東工業株式会社 Tank apparatus, circulation type dispersion system, and dispersion method
US10086344B2 (en) 2011-02-17 2018-10-02 Sintokogio, Ltd. Tank apparatus, a system for dispersing by circulating a mixture, and a method for dispersing by circulating a mixture
CN103768972A (en) * 2014-01-27 2014-05-07 黄山晶品建筑集料科技有限公司 Humidification stirring system
CN113230935A (en) * 2021-05-24 2021-08-10 四川省威沃敦化工有限公司 Low intelligent production facility that hinders degree of depth acidizing fluid densifier uses

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