JPH07106325B2 - Wet atomizer for cement grout - Google Patents

Wet atomizer for cement grout

Info

Publication number
JPH07106325B2
JPH07106325B2 JP26522487A JP26522487A JPH07106325B2 JP H07106325 B2 JPH07106325 B2 JP H07106325B2 JP 26522487 A JP26522487 A JP 26522487A JP 26522487 A JP26522487 A JP 26522487A JP H07106325 B2 JPH07106325 B2 JP H07106325B2
Authority
JP
Japan
Prior art keywords
processing cylinder
motor
cement
bead
grout material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP26522487A
Other languages
Japanese (ja)
Other versions
JPH01107852A (en
Inventor
吉田  裕
丞 岩渕
利雄 早矢仕
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.)
Electric Power Development Co Ltd
Original Assignee
Electric Power Development 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 Electric Power Development Co Ltd filed Critical Electric Power Development Co Ltd
Priority to JP26522487A priority Critical patent/JPH07106325B2/en
Publication of JPH01107852A publication Critical patent/JPH01107852A/en
Publication of JPH07106325B2 publication Critical patent/JPH07106325B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はグラウト材の微粒化装置に関し、より詳しくは
土木工事における止水及び基礎地盤改良のために施工現
場で使用するセメント系グラウト材の湿式微粒化装置に
関する。
TECHNICAL FIELD The present invention relates to a grout material atomizer, and more specifically, to a cement-based grout material used at a construction site for waterproofing in civil works and improvement of foundation ground. The present invention relates to a wet atomizer.

〔従来の技術〕[Conventional technology]

止水や水利用のためのダム建設は、産業の発展とともに
急速に増加している。しかし近時ダム建設に適した岩盤
を有する地点は殆んど開発し盡され、砂礫、粘土、軟岩
等からなる地質的にダム建設に不利な基礎地盤にもダム
を設けざるを得なくなった。一般にこの種の基礎地盤は
多くの微細間隙やアークラックを含んでいて、ダム建設
のためには設計及び施工上多くの難問題がある。
Dam construction for water stoppage and water use is increasing rapidly with industrial development. Recently, however, most of the sites that have suitable bedrock for dam construction have been developed and damned, and it has been unavoidable to install a dam on the foundation ground that is geologically disadvantageous for dam construction, such as gravel, clay, and soft rock. Generally, this kind of foundation ground contains many fine gaps and arc racks, and there are many problems in design and construction for dam construction.

このような基礎地盤の安定処理には薬液注入工法等の種
々の工法が開発されている。しかし薬液注入工法は薬品
による公害上の問題から、1974年以降は水ガラス系を除
いてその使用が規制されるようになった。このような環
境を踏まえて、薬液注入工法に代って現在はセメント系
グラウト材注入工法が基礎地盤安定処理工法の主流とな
りつつある。
Various methods such as a chemical injection method have been developed for such stable treatment of the foundation ground. However, since the chemical injection method is a pollution problem due to chemicals, its use has been restricted since 1974 except for water glass. In consideration of such an environment, the cement-based grout material injection method is now becoming the mainstream of the foundation ground stabilization method instead of the chemical injection method.

グラウト材注入工法に用いられる普通ポルトランドセメ
ントの平均粒径D50は約20μmで、基礎地盤の微細間隙
やヘアークラックに充填するには粒径的に注入限界があ
って使用できない。
The average particle size D 50 of ordinary Portland cement used in the grout material injection method is about 20 μm, and it cannot be used because there is an injection limit in particle size for filling fine gaps and hair cracks in the foundation ground.

そのためボールミル等の乾式微粒化装置を用いて平均粒
径D50を6〜8μmにしたセメント粒子が使用されてい
るが上述したような地盤間隙に注入するには未だ充分で
はない。しかも乾式微粒化は工数が多いため価格が普通
セメントの5〜10倍となり、さらに施工現場における注
入時にセメントと水を混合して使用するため粒子の団粒
化(複数の個々の粒子が集って体積の大きな粒子とな
る)を生じ、見かけのグラウト粒径が大きくなることに
より注入効果が低下する。またセメント粒子が微小であ
るため粒子の劣化が早く、長期保存が困難である。
Therefore, cement particles having an average particle diameter D 50 of 6 to 8 μm are used by using a dry atomizer such as a ball mill, but they are not sufficient to inject into the above-mentioned ground gap. Moreover, the cost of dry atomization is 5 to 10 times that of ordinary cement due to the large number of man-hours, and because the cement and water are mixed and used at the time of injection at the construction site, the particles are aggregated (multiple individual particles are collected. And becomes particles with a large volume) and the apparent grout particle size becomes large, so that the injection effect is reduced. Further, since the cement particles are minute, the particles are deteriorated quickly, and long-term storage is difficult.

上記の事情に鑑み本発明者等は特開昭57−33613号にか
かるグラウト注入工法及び特開昭59−88526号にかかる
グラウト剤湿式調整機構を提案した。
In view of the above circumstances, the present inventors have proposed a grout injection method according to JP-A-57-33613 and a grout agent wet adjustment mechanism according to JP-A-59-88526.

特開昭57−33613号に開示の工法はセメントグラウトが
スラリー状で用いられることに着目し、セメントの微粒
化を従来の乾式から湿式に変更することにより、粉砕の
効率化及びセメントグラウト性能の改善を計り、湿式微
粒化を施工現場で行なってこれを直ちに基礎地盤に注入
するものである。この工法によって乾燥微粉末セメント
の吸湿化しやすい性質を除去し、さらにセメント粒子を
水中に十分に分散することによって効果的な注入が可能
となった。
The method disclosed in JP-A-57-33613 focuses on the fact that cement grout is used in the form of a slurry, and by changing the conventional atomization method of cement from wet type to improve the efficiency of crushing and the cement grout performance. After making improvements, wet atomization is performed at the construction site and this is immediately injected into the foundation ground. By this method, the property of the dry fine powder cement that tends to absorb moisture was removed, and by further dispersing the cement particles in water, effective injection became possible.

また特開昭59−88526号に開示の調整機構は上記の工法
を実施するための装置であって、水平状の処理筒の中に
複数個のディスクを配設した回転軸を横架し、処理筒の
一端上部にセメント系グラウト材の送入口とビーズの投
入口を設けるとともに他端上部に過材を介して処理済
みのセメント系グラウト材を排出するオーバーフロー口
を設け、処理筒の底部にビーズの排出口を設ける。又上
記ディスクにはテーパを有する貫通孔を設け、テーパ付
貫通孔の拡開方向を反対としたディスクを組合わせ配設
して処理筒内におけるビーズによる破砕効果の向上を計
っている。このように処理筒の中にビーズを充填し、こ
のビーズにディスクによって高速回転運動を与え、その
中をセメント系グラウト材を連続的に通過させることに
よりセメント粒子を微粒化させるものである。
Further, the adjusting mechanism disclosed in JP-A-59-88526 is an apparatus for carrying out the above-mentioned construction method, in which a rotary shaft having a plurality of disks arranged horizontally in a horizontal processing cylinder, An inlet for cement grout material and an inlet for beads are provided at the upper end of the processing cylinder, and an overflow port for discharging the treated cement grout material is provided at the upper end of the processing cylinder at the bottom of the processing cylinder. Provide an outlet for beads. Further, the disk is provided with a through hole having a taper, and the disks having the tapered through holes whose opening directions are opposite to each other are arranged in combination so as to improve the crushing effect by the beads in the processing cylinder. Thus, the beads are packed in the treatment cylinder, the beads are subjected to a high-speed rotary motion by the disk, and the cement-based grout material is continuously passed through the beads to atomize the cement particles.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

上述した特開昭59−88526号の調整機構では、投入口を
通してのビーズの供給は一定時間間隔に手動により行な
われていた。そのため運転効率が低く、また均済なセメ
ント製品(微粒化されたセメント系グラウト材)が得ら
れなかった。従って本発明の目的は特開昭59−88526号
の調整機構にあった上記の欠点を解消することである。
In the adjusting mechanism of JP-A-59-88526 described above, the beads are supplied manually through the charging port at regular time intervals. As a result, the operating efficiency was low, and a leveled cement product (fine-grained cement-based grout material) could not be obtained. Therefore, an object of the present invention is to eliminate the above-mentioned drawbacks of the adjusting mechanism disclosed in JP-A-59-88526.

〔問題点を解決するための手段〕[Means for solving problems]

上記の目的は、略水平状に配設した円筒状の処理筒と、
該処理筒内に軸線方向に配設されてモータによって回転
駆動される回転軸と、上記の回転軸に所定の間隔をおい
て上記軸線に対して略直交状に固設された複数のディス
クとを備え、各ディスクは軸線方向に複数個のテーパ付
貫通孔を有するとともに各ディスクの貫通孔は処理筒の
長手方向の略中央部を境にして夫々のテーパ付貫通孔の
拡開方向が、互に反対にかつ処理筒の端部に向けて形成
され、上記処理筒の一端上部に微粒化すべきセメント系
グラウト材の送入口とビーズ投入口とを設け、また処理
筒の底部にビーズの排出口と、処理筒の他端上部に過
部材を介して微粒化処理済みのセメント系グラウト材の
オーバーフロー口を設けた装置において、 上記ビーズ投入口を処理筒の長手方向の中央部の上部に
設け、該ビーズ投入口に、底部を処理筒内に開口した垂
直状のビーズ装入ホッパを立設し、上記モータの負荷電
流値を検知する電流計と、該電流計から検知信号を受け
てモータの回路を切断するスイッチと、モータの停止後
一定時間が経過すればモータを再起動するタイマーとを
含んだ電気的制御装置をモータに付設したことを特徴と
するセメント系グラウト材の湿式微粒化装置によって達
成される。
The above-mentioned purpose is a cylindrical processing cylinder arranged in a substantially horizontal shape,
A rotary shaft that is disposed in the processing cylinder in the axial direction and is driven to rotate by a motor, and a plurality of disks that are fixed to the rotary shaft at a predetermined interval and that are substantially orthogonal to the axis. Each disk has a plurality of tapered through holes in the axial direction, and the through holes of each disk have a direction in which each tapered through hole expands with a substantially central portion in the longitudinal direction of the processing cylinder as a boundary. They are formed opposite to each other and toward the end of the processing cylinder, and an inlet for the cement-based grout material to be atomized and a bead inlet are provided at the upper end of one end of the processing cylinder, and the beads are discharged at the bottom of the processing cylinder. In an apparatus provided with an outlet and an overflow port of the cement-based grout material that has been subjected to atomization treatment through an excess member at the upper end of the other end of the processing cylinder, the bead charging port is provided above the central portion in the longitudinal direction of the processing cylinder. , The bottom of the bead input port A vertical bead loading hopper opened vertically in the processing cylinder is erected, an ammeter for detecting the load current value of the motor, a switch for receiving a detection signal from the ammeter and disconnecting the motor circuit, and a motor. This is achieved by a wet atomization device for cement-based grout material, which is characterized in that an electric control device including a timer for restarting the motor after a lapse of a certain time has been attached to the motor.

〔実施例〕〔Example〕

以下、添付図面を参照した実施例について本発明を詳細
に説明する。
Hereinafter, the present invention will be described in detail with reference to embodiments with reference to the accompanying drawings.

機台1上には水平状に円筒形の処理筒2が設けられ、処
理筒2内には、所定間隔にかつ処理筒の軸線に対し略直
交状に複数個のディスク3を固設した回転軸4が処理筒
2の両端に設けられたグランドパッキン5を介して回転
自在に横架されている。回転軸4はベルト6が巻回され
たプーリ7,8を介し、機台1に固設されたモータ9によ
って高速回転される。上記の処理筒2の一端上部にセメ
ント系グラウト材送入口10が設けられ、普通セメントを
水と混合したセメント系グラウト材が図示せぬ混合機よ
りポンプPを介して処理筒2内に連続的に供給されるよ
うになっている。処理筒2の長手方向の中央部には、鋼
球,鋼製ペレット、陶器質又は磁器質等の硬質粒材から
なるビーズの装入ホッパ11が設けられている。この装入
ホッパ11は垂直状の筒で下部は処理筒2の内部に開口し
ている。また処理筒2の他端上部にオーバーフロー口12
が設けられ、その底部にはウェッジ形のスクリーンバー
形の過部材13が配設されている。ウェッジ形スクリー
ンバーは軸線方向に配設され、ウェッジは外方に向って
拡開していてワイヤブラッシによる掃除が容易になって
いる。またオーバーフロー口12自体2重構造にして洗滌
のための取外し自在になっている。14は過部材13の上
部に設けた微粒化済グラウト材取出し管である。処理筒
2の中央底部に底蓋15Aを備えたビーズ排出口15が設け
られ、その下方には受皿16及び受皿16よりの取出口17が
設けられている。
A horizontally cylindrical processing cylinder 2 is provided on the machine base 1, and a plurality of disks 3 are fixedly mounted in the processing cylinder 2 at predetermined intervals and substantially orthogonal to the axis of the processing cylinder. A shaft 4 is rotatably mounted horizontally via gland packings 5 provided at both ends of the processing cylinder 2. The rotating shaft 4 is rotated at high speed by a motor 9 fixed to the machine base 1 via pulleys 7 and 8 around which a belt 6 is wound. A cement-based grout material inlet 10 is provided at one upper end of the processing cylinder 2, and a cement-based grout material in which ordinary cement is mixed with water is continuously fed into the processing cylinder 2 through a pump P from a mixer (not shown). To be supplied to. A bead charging hopper 11 made of hard particles such as steel balls, steel pellets, ceramics or porcelain is provided at the center of the processing cylinder 2 in the longitudinal direction. The charging hopper 11 is a vertical cylinder, and the lower part is opened inside the processing cylinder 2. Further, the overflow port 12 is provided on the other end of the processing cylinder 2.
Is provided, and a wedge-shaped screen bar-shaped excess member 13 is disposed at the bottom thereof. The wedge-shaped screen bar is arranged in the axial direction, and the wedge is expanded outward to facilitate cleaning with the wire brush. In addition, the overflow port 12 itself has a double structure, which is removable for cleaning. Reference numeral 14 denotes an atomized grout material take-out pipe provided on the upper member 13. A bead outlet 15 having a bottom lid 15A is provided at the center bottom of the processing cylinder 2, and a tray 16 and an outlet 17 from the tray 16 are provided below the bead outlet 15.

上述したディスク3は夫々回転軸4に直交状に固設され
ていて処理筒2内に供給されたビーズを撹拌してグラウ
ト材を粉砕すると共に処理筒2の中央部のビーズを両端
に向けて移動させる約割りをする。このためディスク3
には第2図に示すようにテーパを有する複数の貫通孔3A
が軸線方向に形成されている。この貫通孔3Aは処理筒2
の中央部を境にして左側のディスク3には左側に向けて
拡開するテーパが、また右側のディスク3には右側に向
けて拡開するテーパが設けられている。ビーズは、貫通
孔3Aのテーパが拡開する方向に移動するので、ディスク
3の回転運動により処理筒2の内部で律動的に移動し、
これによってグラウト材を微粒状に破砕する効果が向上
する。
The above-mentioned disks 3 are fixed to the rotating shaft 4 at right angles to each other. The beads supplied into the processing cylinder 2 are stirred to grind the grout material, and the beads at the center of the processing cylinder 2 are directed toward both ends. Make a contract to move. For this reason disk 3
As shown in FIG. 2, there are a plurality of tapered through holes 3A.
Are formed in the axial direction. This through hole 3A is the processing cylinder 2
The left side disk 3 is provided with a taper that expands toward the left side, and the right side disk 3 is provided with a taper that expands toward the right side with the center part of the boundary as a boundary. Since the beads move in the direction in which the taper of the through hole 3A expands, the beads move rhythmically inside the processing cylinder 2 due to the rotational movement of the disk 3,
This improves the effect of crushing the grout material into fine particles.

尚、処理筒2の周囲は水冷ジャケット18で囲まれてい
る。又19は電流計20、スイッチ21及びタイマー22を含ん
だ制御装置でモータ9及びポンプPに夫々接続されてい
る。
The processing cylinder 2 is surrounded by a water cooling jacket 18. Reference numeral 19 is a control device including an ammeter 20, a switch 21 and a timer 22, which are connected to the motor 9 and the pump P, respectively.

次に本発明の装置の操業例を説明する。Next, an operation example of the apparatus of the present invention will be described.

使用した処理筒の内容積は50、回転軸の回転数は700
〜800rpmであった。この処理筒2に粒径0.6〜2.0mmのビ
ーズを約300kg装入すると共に普通ポルトランドセメン
トをセメント水比(C/W)=1:3に混合したグラウト材を
7〜10l/minの速度で送入口10を通してポンプPで連続
的に送入して微粒化処理を行なった。この処理により平
均粒径D50=20μmの普通ポルトランドセメントが平均
粒径D50=2〜3μmに微細化された。オーバーフロー
口12から得られる微細化されたグラウト材の取出し速度
は平均8.5l/minである。
The inner volume of the processing cylinder used was 50, and the rotation speed of the rotating shaft was 700.
It was ~ 800 rpm. About 300 kg of beads having a particle size of 0.6 to 2.0 mm are charged into this treatment cylinder 2, and grout material in which ordinary Portland cement is mixed at a cement water ratio (C / W) = 1: 3 is used at a speed of 7 to 10 l / min. A pump P was continuously fed through the feed port 10 to carry out atomization treatment. By this treatment, ordinary Portland cement having an average particle size D 50 = 20 μm was refined to have an average particle size D 50 = 2 to 3 μm. The take-out speed of the finely-ground grout material obtained from the overflow port 12 is 8.5 l / min on average.

上記の微細化処理中にビーズはディスク3及びグラウト
材との摩擦によって摩耗し、平均粒径が0.1〜0.2mmにな
るとセメント粒子を有効に粉砕することができなくな
る。このようにして使用可能なビーズが1時間当り5kg
減少する。しかし品質のよいグラウト材を作るには処理
筒2内に使用可能な一定量のビーズを維持することが必
要である。
During the above-mentioned refining treatment, the beads are worn by friction with the disk 3 and the grout material, and when the average particle diameter becomes 0.1 to 0.2 mm, the cement particles cannot be effectively ground. 5 kg of beads that can be used in this way per hour
Decrease. However, in order to produce a good quality grout material, it is necessary to maintain a certain amount of usable beads in the processing cylinder 2.

本発明の装置によれば、底部のない装入ホッパ11の中に
は所定量のビーズが収容されている。装置の作動中は処
理筒2内に充満したビーズ及びグラウト材の充填物に遠
心力が作用するので、装入ホッパ11内のビーズは充填物
と平衡を保ち処理筒2内に落下しないで装入ホッパ中に
維持される。上述したように使用可能なビーズ即ち大径
のビーズが減少すると処理筒2内のビーズの充填率が減
少し、従ってモータ9の負荷が減少して電流のアンペア
値が低下する。制御装置19はモータ9に流れる電流のア
ンペア値を電流計20で検知し、その信号を受けたスイッ
チ21によりモータ9及びポンプPの作動を停止するよう
に構成されている。
According to the apparatus of the present invention, a predetermined amount of beads is contained in the bottomless charging hopper 11. During the operation of the apparatus, centrifugal force acts on the beads and grout material filled in the processing cylinder 2, so that the beads in the charging hopper 11 are in equilibrium with the filling and do not fall into the processing cylinder 2. Maintained in the incoming hopper. As described above, when the number of usable beads, that is, the beads having a large diameter, is reduced, the filling rate of the beads in the processing cylinder 2 is reduced, so that the load of the motor 9 is reduced and the ampere value of the current is reduced. The control device 19 is configured to detect the ampere value of the current flowing through the motor 9 with the ammeter 20 and stop the operation of the motor 9 and the pump P by the switch 21 that receives the signal.

モータ9が運転を停止すると充填物の遠心力が0になり
装入ホッパ11下方の充填物の表面スラリー部分23(作動
中にはこの部分にスラリーが現われない)に装入ホッパ
11の底部のビーズが落下する。タイマー22にセットされ
た時間が過ぎるとモータ9及びポンプPは再起動されて
運転を開始する。尚、上記の停止時間が僅小の場合には
ポンプPは停止させなくともよい。本実施例の場合ビー
ズの減少量が5kg/hrなので1日当りの操業時間を6時間
とすれば装入ホッパ11の収容量は30kgとなる。
When the operation of the motor 9 is stopped, the centrifugal force of the packing becomes 0, and the charging hopper is placed in the surface slurry part 23 of the packing below the charging hopper 11 (slurry does not appear in this part during operation).
The beads at the bottom of 11 fall. When the time set in the timer 22 has passed, the motor 9 and the pump P are restarted and the operation is started. The pump P does not have to be stopped when the above stop time is short. In the case of the present embodiment, the amount of beads reduced is 5 kg / hr, so if the operating time per day is 6 hours, the capacity of the charging hopper 11 will be 30 kg.

次にモータ9の負荷電流値をビーズ補充量との関係を第
3,4図及び〔表〕について説明する。
Next, the relationship between the load current value of the motor 9 and the bead replenishment amount
3 and 4 and [Table] will be described.

モータの負荷電流の下限電流値を170Aに設定し、またモ
ータの停止時間を8秒にセットした。第3図及び表に示
すように、モータ9が停止すると装入ホッパ11中のビー
ズの下面とスラリー部分23の表面間には平均7.6cmの落
下差を生じて平均2.5kgのビーズがスラリー部分23の表
面に落下する。モータが再起動されると負荷電流値は平
均182Aになる。運転サイクルは平均30分である。
The lower limit current value of the load current of the motor was set to 170A, and the stop time of the motor was set to 8 seconds. As shown in FIG. 3 and the table, when the motor 9 is stopped, an average drop difference of 7.6 cm occurs between the lower surface of the beads in the charging hopper 11 and the surface of the slurry portion 23, and an average of 2.5 kg of beads becomes the slurry portion. Drops to the surface of 23. When the motor is restarted, the load current value averages 182A. The average driving cycle is 30 minutes.

第4図はビーズの累加補充量を示す図で、〔表〕からも
判るように処理筒2内のビーズの減少に応じて、装入ホ
ッパ11から対応した量のビーズが補充される。
FIG. 4 is a diagram showing the cumulative replenishment amount of beads, and as can be seen from the table, the corresponding amount of beads is replenished from the charging hopper 11 according to the decrease of the beads in the processing cylinder 2.

長時間操業をすると処理筒2内の摩耗したビーズの量が
増加して微粒化効率が低下する。従って定期的に装置の
運転を止め排出口15を開いて充填物を取出しふるい分け
る。この際粒径が0.6mmよりも大きいビーズは再使用
し、他のビーズは廃棄する。
When operating for a long time, the amount of worn beads in the processing cylinder 2 increases and the atomization efficiency decreases. Therefore, the operation of the apparatus is periodically stopped, the discharge port 15 is opened, and the packing material is taken out and sieved. At this time, beads with a particle size larger than 0.6 mm are reused, and other beads are discarded.

〔発明の効果〕〔The invention's effect〕

本発明は上記のように構成して、モータの負荷電流が設
定値に到達すると装置の運転を停止して底のない装入ホ
ッパよりビーズが自重で処理筒内に一定量落下してビー
ズの消耗量を補充し、また運転中は処理筒内の充填物の
遠心力及び装入ホッパとの摩擦によって補充用ビーズが
落下しない状態に維持されるので構造簡単で極めて効率
的なビーズの自動装入効果が得られる。
The present invention is configured as described above, and when the load current of the motor reaches the set value, the operation of the apparatus is stopped and the beads from the bottomless charging hopper drop by a certain amount into the processing cylinder due to their own weight. The replenishment amount is replenished, and during operation, the replenishing beads are kept in a state of not falling due to the centrifugal force of the packing in the processing cylinder and friction with the charging hopper. The entry effect is obtained.

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

第1図は本発明の装置を部分破断して示した断面図、第
2図はその回転軸及びディスク部分の拡大断面図、第3
図は負荷電流の経時変化を示す図、第4図はビーズの累
加補充量を示す図である。 2……処理筒、3……ディスク、3A……テーパ付貫通
孔、4……回転軸、9……モータ、10……微粒化前グラ
ウト材の送入口、11……ビーズ装入ホッパ、12……微粒
化済グラウト材のオーバーフロー口、13……過部材、
15……ビーズの排出口、19……電気的制御装置、20……
電流計、21……スイッチ、22……タイマ。
FIG. 1 is a partially cutaway sectional view of the device of the present invention, FIG. 2 is an enlarged sectional view of its rotary shaft and disk portion, and FIG.
FIG. 4 is a diagram showing changes in load current with time, and FIG. 4 is a diagram showing cumulative replenishment amount of beads. 2 ... Processing cylinder, 3 ... Disc, 3A ... Tapered through hole, 4 ... Rotary shaft, 9 ... Motor, 10 ... Grout material inlet before atomization, 11 ... Bead loading hopper, 12 …… Overflow port of atomized grout material, 13 …… Over-material,
15 …… Bead outlet, 19 …… Electric control device, 20 ……
Ammeter, 21 …… switch, 22 …… timer.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 早矢仕 利雄 埼玉県志木市館2丁目4番1―301 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Toshio Hayaya 2-4-1-3, Shiki-shi, Saitama

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】略水平状に配設した円筒状の処理筒(2)
と、該処理筒内に軸線方向に配設されてモータ(9)に
よって回転駆動される回転軸(4)と、上記の回転軸に
所定の間隔をおいて上記軸線に対して略直交状に固設さ
れた複数のディスク(3)とを備え、各ディスクは軸線
方向に複数個のテーパ付貫通孔(3A)を有するとともに
各ディスクの貫通孔は処理筒の長手方向の略中央部を境
にして夫々のテーパ付貫通孔の拡開方向が、互に反対に
かつ処理筒の端部に向けて形成され、上記処理筒の一端
上部に微粒化すべきセメント系グラウト材の送入口(1
0)とビーズ投入口を設け、また処理筒の底部にビーズ
の排出口(15)と、処理筒の他端上部に過部材(13)
を介して微粒化処理済みのセメント系グラウト材のオー
バーフロー口(12)を設けた装置において、 上記ビーズ投入口を処理筒の長手方向の中央部の上部に
設け、該ビーズ投入口に、底部を処理筒内に開口した垂
直状のビーズ装入ホッパ(11)を立設し、上記モータ
(9)の負荷電流値を検知する電流計(20)と、該電流
計から検知信号を受けてモータの回路を切断するスイッ
チ(21)と、モータの停止後一定時間が経過すればモー
タを再起動するタイマー(22)とを含んだ電気的制御装
置(19)をモータに付設したことを特徴とするセメント
系グラウト材の湿式微粒化装置。
1. A cylindrical processing cylinder (2) arranged substantially horizontally.
A rotary shaft (4) arranged in the processing cylinder in the axial direction and driven to rotate by a motor (9); and a rotary shaft (4) at a predetermined interval from the rotary shaft so as to be substantially orthogonal to the rotary shaft. A plurality of fixed discs (3), each disc has a plurality of tapered through holes (3A) in the axial direction, and the through holes of each disc bound the substantially central portion in the longitudinal direction of the processing cylinder. Then, the expansion directions of the respective tapered through holes are formed so as to be opposite to each other and toward the end of the processing cylinder, and the inlet (1) of the cement-based grout material to be atomized is formed at the upper end of one end of the processing cylinder.
0) and a bead input port, a bead discharge port (15) at the bottom of the processing cylinder, and an excess member (13) at the upper end of the other end of the processing cylinder.
In an apparatus provided with an overflow port (12) for a cement-based grout material that has been subjected to atomization treatment, the bead charging port is provided at the upper part of the central part in the longitudinal direction of the processing cylinder, and the bead charging port is provided with a bottom part. A vertical bead loading hopper (11) having an opening in the processing cylinder is provided upright, and an ammeter (20) for detecting a load current value of the motor (9) and a motor receiving a detection signal from the ammeter. The electric control device (19) including a switch (21) for disconnecting the circuit of (1) and a timer (22) for restarting the motor after a lapse of a certain time after stopping the motor is attached to the motor. Wet atomizer for cement-based grout material.
JP26522487A 1987-10-22 1987-10-22 Wet atomizer for cement grout Expired - Fee Related JPH07106325B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26522487A JPH07106325B2 (en) 1987-10-22 1987-10-22 Wet atomizer for cement grout

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26522487A JPH07106325B2 (en) 1987-10-22 1987-10-22 Wet atomizer for cement grout

Publications (2)

Publication Number Publication Date
JPH01107852A JPH01107852A (en) 1989-04-25
JPH07106325B2 true JPH07106325B2 (en) 1995-11-15

Family

ID=17414249

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26522487A Expired - Fee Related JPH07106325B2 (en) 1987-10-22 1987-10-22 Wet atomizer for cement grout

Country Status (1)

Country Link
JP (1) JPH07106325B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6371024B1 (en) * 2018-02-15 2018-08-08 有限会社シモダ技術研究所 Method of injecting quick-setting hardened grout

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2719431B2 (en) * 1990-05-10 1998-02-25 関西ペイント株式会社 Media discharging device and discharging method for sand mill
JP7378941B2 (en) * 2019-02-27 2023-11-14 大王製紙株式会社 Grinding bead supply device, bead mill and grinding method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6371024B1 (en) * 2018-02-15 2018-08-08 有限会社シモダ技術研究所 Method of injecting quick-setting hardened grout

Also Published As

Publication number Publication date
JPH01107852A (en) 1989-04-25

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