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JP2000354750A - Continuous kneading device for powdery hydraulic material - Google Patents

Continuous kneading device for powdery hydraulic material

Info

Publication number
JP2000354750A
JP2000354750A JP11168359A JP16835999A JP2000354750A JP 2000354750 A JP2000354750 A JP 2000354750A JP 11168359 A JP11168359 A JP 11168359A JP 16835999 A JP16835999 A JP 16835999A JP 2000354750 A JP2000354750 A JP 2000354750A
Authority
JP
Japan
Prior art keywords
kneading
vertical
powdery hydraulic
hydraulic material
water
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
JP11168359A
Other languages
Japanese (ja)
Other versions
JP3736990B2 (en
Inventor
Takashi Mibe
隆 見辺
Kenji Hatta
建次 八田
Takeshi Koide
剛 小出
Ichiro Nasu
一郎 那須
Masaaki Ito
正明 伊藤
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP16835999A priority Critical patent/JP3736990B2/en
Publication of JP2000354750A publication Critical patent/JP2000354750A/en
Application granted granted Critical
Publication of JP3736990B2 publication Critical patent/JP3736990B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

(57)【要約】 【課題】 粉末状水硬性材料を水と連続的に混練し排出
する装置の提供。 【解決手段】 材料供給装置を竪型材料供給筒7に連接
し、粉末状水硬性材料9を竪型材料供給筒7へ連続的か
つ定量的に供給すると共に、該竪型材料供給筒7の下部
に設置される竪型ミキシング筒6の側面に水供給管5を
設け、水を連続的かつ定量的に供給し、竪型ミキシング
筒6の底部に粉末状水硬性材料9と水とを混練する攪拌
翼4を設け、連続で混練し、該竪型ミキシング筒6の側
面下部の混練物排出口13に接続された排出管14を、
その先端が前記排出口13より高い位置になるように立
ち上げ、竪型ミキシング筒6内の混練物を滞留させるよ
うにしたことを特徴とする粉末状水硬性材料の連続混練
装置。
(57) [Problem] To provide an apparatus for continuously kneading and discharging a powdery hydraulic material with water. SOLUTION: The material supply device is connected to a vertical material supply cylinder 7, and a powdery hydraulic material 9 is continuously and quantitatively supplied to the vertical material supply cylinder 7; A water supply pipe 5 is provided on a side surface of a vertical mixing cylinder 6 installed at a lower portion to supply water continuously and quantitatively, and a powdery hydraulic material 9 and water are kneaded at the bottom of the vertical mixing cylinder 6. A stirring pipe 4 is provided, which is continuously kneaded, and a discharge pipe 14 connected to a kneaded material discharge port 13 at the lower side of the vertical mixing cylinder 6 is
A continuous kneading apparatus for a powdery hydraulic material, characterized in that the tip is raised so as to be at a position higher than the discharge port 13 and the kneaded material in the vertical mixing cylinder 6 is retained.

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】本発明は、粉末状水硬性材料
を水と連続的に混練し排出する装置に関する。
The present invention relates to an apparatus for continuously kneading and discharging a powdery hydraulic material with water.

【0002】[0002]

【従来の技術とその課題】従来、粉末状水硬性材料の連
続混練装置としては、粉末状水硬性材料と水との混練機
構と圧送ポンプを駆動する動力源とを略同一直線上に配
置し、粉末状水硬性材料を連続的に混練し圧送する装置
が提案されている(特開平3−121815号公報)。
この連続混練装置の混練機構のミキシングシャフトは、
動力源により回転するシャフトと混練用パドルが溶接等
の手段により固定されたものであり、粉末状水硬性材料
に対する水の重量割合が20重量%程度ならば均質な混
練が可能である。しかしながら、粉末状水硬性材料に対
する水の重量割合を50重量%以上で混練しようとする
と、混練装置より排出される材料の中に練り玉ができ、
均質な混練ができないという課題があった。特に、粉末
状水硬性材料をミルク状の物として混練しようとする
際、この現象は顕著に表れ、粉末状水硬性材料の連続混
練は不可能とされていた。
2. Description of the Related Art Conventionally, as a continuous kneading apparatus for a powdery hydraulic material, a kneading mechanism of a powdery hydraulic material and water and a power source for driving a pressure pump are arranged on substantially the same straight line. An apparatus for continuously kneading and pressure-feeding a powdery hydraulic material has been proposed (Japanese Patent Laid-Open No. 3-121815).
The mixing shaft of the kneading mechanism of this continuous kneading device is
A shaft that is rotated by a power source and a kneading paddle are fixed by means such as welding, and if the weight ratio of water to the powdery hydraulic material is about 20% by weight, uniform kneading is possible. However, if the weight ratio of water to the powdery hydraulic material is to be kneaded at 50% by weight or more, kneaded balls are formed in the material discharged from the kneading device,
There was a problem that uniform kneading was not possible. In particular, when the powdery hydraulic material is to be kneaded as a milk-like material, this phenomenon is remarkable, and continuous kneading of the powdery hydraulic material has been considered impossible.

【0003】また、最近になり急硬性を有する粉末状水
硬性材料の連続混練装置を求める動きがでてきており、
前記連続混練装置により急硬性を有する粉末状水硬性材
料を混練しようとすると水の供給口付近の回転シャフ
ト、パドル部、及び/又はミキシング筒に充分に混練さ
れていない粉末状水硬性材料が付着し、短時間で硬化成
長することにより、スクリューフィーダーからの急硬性
を有する粉末状水硬性材料の供給量が徐々に低下し、所
定の割合で混練ができなくなるという課題があった。ま
た、前記混練装置の圧送ポンプを外しミキシング筒を横
型にしたものでは、粉末状水硬性材料に対する水の重量
割合が20重量%程度の場合には前記の課題の他にホッ
パー内に粉末を残した状態で混練を中断すると、未混練
の粉末状水硬性材料が残り硬化してしまったり、混練水
がスクリューあるいはホッパー側に染み込み再び混練を
行おうとする際、運転が不可能となる問題があった。
In recent years, there has been a movement for a continuous kneading apparatus for a powdery hydraulic material having rapid hardening.
When trying to knead the powdered hydraulic material having rapid hardening by the continuous kneading device, the powdery hydraulic material that is not sufficiently kneaded adheres to the rotating shaft, paddle portion, and / or mixing cylinder near the water supply port. However, the hardening growth in a short time causes a problem that the supply amount of the powdery hydraulic material having rapid hardening from the screw feeder gradually decreases, and kneading cannot be performed at a predetermined ratio. Further, in the case where the mixing cylinder is made horizontal by removing the pressure feed pump of the kneading apparatus, when the weight ratio of water to the powdery hydraulic material is about 20% by weight, powder remains in the hopper in addition to the above-mentioned problems. If kneading is interrupted in a mixed state, the unmixed powdered hydraulic material remains and hardens, or the kneading water soaks into the screw or hopper side and attempts to perform kneading again. Was.

【0004】また、バッチ式混練装置を使用した場合
は、粉末状水硬性材料に対する水の割合が50重量%以
上の粉末状水硬性材料でも均質な混練ができるが、混練
水や粉末状水硬性材料の計量が必要なため作業が繁雑で
あること、1バッチ分の混練量が固定されているため、
作業が終了した際に多量の混練済み材料が残った場合廃
棄せねばならず不経済であることなどの課題があった。
When a batch-type kneading apparatus is used, homogeneous kneading can be performed even with a powdery hydraulic material having a water content of 50% by weight or more with respect to the powdery hydraulic material. The work is complicated due to the need to weigh the materials, and the kneading amount for one batch is fixed.
When a large amount of kneaded material remains when the operation is completed, it must be discarded, which is uneconomical.

【0005】本発明者は、前記課題を解消すべく種々検
討した結果、特定の混練装置を使用することによって、
前記課題が解消することを知見して本発明を完成するに
至った。
The present inventor has conducted various studies to solve the above-mentioned problems, and as a result, by using a specific kneading apparatus,
The inventors have found that the above-mentioned problems are solved, and have completed the present invention.

【0006】[0006]

【課題を解決するための手段】即ち、本発明は、材料供
給装置を竪型材料供給筒7に連接し、粉末状水硬性材料
9を竪型材料供給筒7へ連続的かつ定量的に供給すると
共に該竪型材料供給筒7の下部に設置される竪型ミキシ
ング筒6の側面に水供給管5を設け水を連続的かつ定量
的に供給し、竪型ミキシング筒6の底部に粉末状水硬性
材料9と水とを混練する攪拌翼4を設け、該竪型ミキシ
ング筒6の側面下部の混練物排出口13に接続された排
出管14を、その先端が前記排出口13より高い位置に
なるように立ち上げ、竪型ミキシング筒6内の混練物を
滞留させるようにしたことを特徴とする粉末状水硬性材
料の連続混練装置である。
That is, according to the present invention, a material supply device is connected to a vertical material supply cylinder 7, and a powdery hydraulic material 9 is continuously and quantitatively supplied to the vertical material supply cylinder 7. At the same time, a water supply pipe 5 is provided on the side of a vertical mixing cylinder 6 installed below the vertical material supply cylinder 7 to supply water continuously and quantitatively. A stirring blade 4 for kneading the hydraulic material 9 and water is provided, and a discharge pipe 14 connected to a kneaded material discharge port 13 at the lower side of the vertical mixing cylinder 6 is disposed at a position where the tip is higher than the discharge port 13. This is a continuous kneading apparatus for a powdery hydraulic material, characterized in that the kneaded material in the vertical mixing cylinder 6 is kept standing.

【0007】[0007]

【発明の実施の形態】以下、図面を参照し本発明を詳細
に説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the drawings.

【0008】図1は本発明の連続混練装置の一例を示す
側面図である。混練機構について説明すると、1は動力
源でありこれを回転させ動力伝達装置2により動力を回
転シャフト3に伝達してこの回転シャフト3に取付けら
れた攪拌翼4を回転させる。材料の供給について説明す
ると、ホッパー8に供給された粉末状急硬性材料9は、
動力源10により駆動される定量供給装置11により、
材料供給口12から該竪型材料供給筒7へ供給される。
竪型材料供給筒7へ供給された粉末状水硬性材料9は、
自然落下により竪型ミキシング筒6へ供給される。一
方、混練水は、該竪型ミキシング筒6側面に設置された
水供給管5より定量供給される。粉末状水硬性材料9と
混練水は、攪拌翼4の回転により混練され、竪型ミキシ
ング筒6の側面下部に設けられた混練物排出口13及び
排出管14を通過し排出される。
FIG. 1 is a side view showing an example of the continuous kneading apparatus of the present invention. The kneading mechanism will be described. Reference numeral 1 denotes a power source, which is rotated to transmit power to the rotary shaft 3 by the power transmission device 2 to rotate the stirring blades 4 attached to the rotary shaft 3. Describing the supply of the material, the powdery hard material 9 supplied to the hopper 8
By the fixed amount supply device 11 driven by the power source 10,
The material is supplied from the material supply port 12 to the vertical material supply cylinder 7.
The powdered hydraulic material 9 supplied to the vertical material supply cylinder 7 is
It is supplied to the vertical mixing cylinder 6 by natural fall. On the other hand, kneading water is supplied at a constant rate from a water supply pipe 5 provided on the side of the vertical mixing cylinder 6. The powdered hydraulic material 9 and the kneading water are kneaded by the rotation of the stirring blade 4, and are discharged through a kneaded material discharge port 13 and a discharge pipe 14 provided at a lower portion of the side of the vertical mixing cylinder 6.

【0009】ここで排出管14の先端の立ち上げ高さは
100mm以上とするのが好ましい。立ち上げ高さが1
00mmより小さいと、滞留量が少なく滞留による混合
効果が小さくなり、混合物中に練り玉を残した状態で排
出される。また、排出管14の立ち上げ高さは、混練水
面が竪型材料供給筒7の壁面を濡らさない高さまで上昇
させることができる。竪型材料供給筒7の壁面が混練水
や混練物で濡れると、粉末状水硬性材料が竪型材料供給
筒7の壁面に付着し、竪型ミキシング筒6へ供給されに
くくなり、所定の濃度の混練ができなくなる。
Here, it is preferable that the rising height of the tip of the discharge pipe 14 be 100 mm or more. Launch height is 1
If it is smaller than 00 mm, the amount of stay is small and the mixing effect due to stay is small, and the mixture is discharged with the kneaded balls left in the mixture. Further, the rising height of the discharge pipe 14 can be increased to a level at which the mixing water surface does not wet the wall surface of the vertical material supply cylinder 7. When the wall surface of the vertical material supply cylinder 7 gets wet with the kneading water or the kneaded material, the powdery hydraulic material adheres to the wall surface of the vertical material supply cylinder 7 and becomes difficult to be supplied to the vertical mixing cylinder 6 and has a predetermined concentration. Can no longer be kneaded.

【0010】攪拌翼の形状はタービン翼が好ましい。タ
ービン翼は高速回転に向き,せん断効果があるため粉末
状水硬性材料に適している。
The shape of the stirring blade is preferably a turbine blade. Turbine blades are suitable for powdery hydraulic materials because they are suitable for high-speed rotation and have a shearing effect.

【0011】攪拌翼の回転数は、200rpm以上であ
るのが好ましい。200rpm未満では、攪拌効果は小
さく排出管14の立ち上げ高さが十分であってもせん断
効果が得られず均一な混練が出来ず混練物中に練り玉が
残る。
The rotation speed of the stirring blade is preferably 200 rpm or more. If the rotation speed is less than 200 rpm, the stirring effect is small, and even if the rising height of the discharge pipe 14 is sufficient, the shearing effect cannot be obtained and uniform kneading cannot be performed, so that kneaded balls remain in the kneaded material.

【0012】竪型材料供給筒7と竪型ミキシング筒6は
同一軸上に設置し、竪型材料供給筒7の内径を竪型ミキ
シング筒6の内径より小さくし、段差をつけることが好
ましい。段差をつけることにより、接液面と接粉面を区
別することが出来、粉末状水硬性材料の供給が安定化さ
れる。
It is preferable that the vertical material supply cylinder 7 and the vertical mixing cylinder 6 are installed on the same axis, the inner diameter of the vertical material supply cylinder 7 is smaller than the inner diameter of the vertical mixing cylinder 6, and a step is provided. By providing a step, the liquid contact surface and the powder contact surface can be distinguished, and the supply of the powdery hydraulic material is stabilized.

【0013】粉末状水硬性材料は竪型材料供給筒7の軸
線近くに投入するのが好ましい。軸線近くに投入するこ
とにより、竪型材料供給筒7や竪型ミキシング筒6の壁
面へ粉末状水硬性材料が付着するのを防止し、安定した
供給が行えるようになる。材料供給装置の先端を竪型材
料供給装置の軸線近くまで挿入することにより、容易に
粉末状水硬性材料を竪型材料供給筒7の軸線近くに投入
できる。
The powdery hydraulic material is preferably introduced near the axis of the vertical material supply cylinder 7. By charging the material near the axis, the powdery hydraulic material is prevented from adhering to the wall surfaces of the vertical material supply cylinder 7 and the vertical mixing cylinder 6, and stable supply can be performed. By inserting the tip of the material supply device near the axis of the vertical material supply device, the powdery hydraulic material can be easily charged near the axis of the vertical material supply cylinder 7.

【0014】本発明の混練装置は、水と混合・混練する
ことによって水和反応して硬化する粉末状水硬性材料に
対応できる。粉末状水硬性材料としては、セメント、モ
ルタル、石膏、及び石灰等の他、セメント等に混合して
それぞれ独自の性能を発揮するセメント混和材にも水硬
性物質がありこれらの混和材も含まれる。
The kneading apparatus of the present invention can cope with a powdery hydraulic material which is cured by a hydration reaction by mixing and kneading with water. As a powdery hydraulic material, in addition to cement, mortar, gypsum, lime, etc., there is a hydraulic substance also in cement admixtures that exhibit their own performance when mixed with cement etc., and these admixtures are also included. .

【0015】特に、粉末状水硬性材料の急硬性成分とし
ては、結晶質、非結晶質のいずれでも良いが、CaOを
C、Al23をA、及びSiO2をSとすると、C2
S、C3A、C127、CA、C117・CaF2、及びC
33・CaSO4等で示される鉱物や、硫酸アルミニウ
ム、ミョウバン類、アルミノケイ酸カルシウムガラス、
並びに、カルシウムやナトリュウム等のアルミン酸アル
カリ金属塩からなる群より選ばれた一種又は二種以上を
含むことが可能であり、さらに、遅延剤や促進剤などの
凝結時間調整剤を含有することも可能である。また、硬
化時間は混練後30秒から120分の間に調整されたも
のが使用できる。
In particular, the rapid hardening component of the powdery hydraulic material may be either crystalline or amorphous. If CaO is C, Al 2 O 3 is A, and SiO 2 is S, C 2 A
S, C 3 A, C 12 A 7 , CA, C 11 A 7 .CaF 2 , and C
3 minerals and represented by A 3 · CaSO 4 and the like, aluminum sulfate, alum such as calcium aluminosilicate glass,
In addition, it is possible to contain one or more selected from the group consisting of alkali metal aluminates such as calcium and sodium, and may further contain a setting time regulator such as a retarder or an accelerator. It is possible. The curing time adjusted between 30 seconds and 120 minutes after kneading can be used.

【0016】[0016]

【実施例】以下、実験例により本発明を詳細に説明す
る。
Hereinafter, the present invention will be described in detail with reference to experimental examples.

【0017】実験例1 図1に示す連続混練装置を用い、竪型材料供給筒7の軸
線近傍に粉末状水硬性材料を定量供給し、竪型ミキシン
グ筒6の底部にタービン翼式攪拌翼を設け、排出管を1
40mm立ち上げ、急硬成分であるカルシウムアルミネ
ート50重量部と石膏50重量部からなる粉末状水硬性
材料100重量部に、混練水を粉末状水硬性材料100
重量部に対し220重量部、凝結時間調整剤を粉末状水
硬性材料100重量部に対し0.5重量部を加え連続混
練を行った。なお、あらかじめ混練水には凝結時間調整
剤を溶かしておき、これを連続混練装置に定量供給し
た。攪拌翼の回転数は500rpmとした。また、竪型
材料供給筒の径は165mm、竪型ミキシング筒の径は
216mm、竪型ミキシング筒の高さ400mmとし
た。連続混練開始直後と30分後に排出管14より混練
物を採取し、混練物が均質に混練されているか確認する
ために、300μmの篩に混練物を通過させ、篩い上残
分の有無を目視観察し残分があるものを×、無いものを
○として判定した。また、粉末状水硬性材料が定量供給
されているかを判定するため、混練開始直後と30分経
過後の混練物の密度を測定し、密度が0.2g/cm3
以上低下したものを×、それ以外を○と判定した。比較
のため、図2と図3に示す従来の連続混練装置について
も同様に試験を行った。測定結果を表1に示す。
EXPERIMENTAL EXAMPLE 1 Using the continuous kneading apparatus shown in FIG. 1, a fixed amount of powdery hydraulic material was supplied near the axis of the vertical material supply cylinder 7, and a turbine blade type stirring blade was provided at the bottom of the vertical mixing cylinder 6. And one drain pipe
40 mm was started, and kneading water was mixed with 100 parts by weight of a powdery hydraulic material composed of 50 parts by weight of calcium aluminate and 50 parts by weight of gypsum, which were rapidly hardened components, to form a powdery hydraulic material 100
The kneading agent was added in an amount of 220 parts by weight based on 100 parts by weight of the powdery hydraulic material, and the mixture was continuously kneaded. In addition, the coagulation time adjusting agent was previously dissolved in the kneading water, and this was supplied to the continuous kneading device in a constant amount. The rotation speed of the stirring blade was 500 rpm. The diameter of the vertical material supply cylinder was 165 mm, the diameter of the vertical mixing cylinder was 216 mm, and the height of the vertical mixing cylinder was 400 mm. Immediately after the start of continuous kneading and 30 minutes later, the kneaded material is sampled from the discharge pipe 14, and the kneaded material is passed through a 300 μm sieve to check whether the kneaded material is homogeneously kneaded, and the presence or absence of residue on the sieve is visually observed. Observation was made as x when there was a residue, and as x when there was no residue. Further, in order to determine whether the powdery hydraulic material is supplied in a fixed amount, the density of the kneaded material immediately after the start of kneading and after 30 minutes has elapsed is measured, and the density is 0.2 g / cm 3.
A sample having the above-mentioned decrease was evaluated as x, and the others were evaluated as ○. For comparison, the same test was performed on the conventional continuous kneading apparatus shown in FIGS. 2 and 3. Table 1 shows the measurement results.

【0018】[0018]

【表1】 [Table 1]

【0019】実験例2 図1に示す連続混練装置を使用し、排出管の立ち上げ高
さを変えたこと以外は実験例1と同様に行った。結果を
表2に示す。
Experimental Example 2 An experiment was performed in the same manner as in Experimental Example 1 except that the continuous kneading apparatus shown in FIG. 1 was used and the rising height of the discharge pipe was changed. Table 2 shows the results.

【0020】[0020]

【表2】 [Table 2]

【0021】実験例3 図1に示す連続混練装置を使用し、攪拌翼の回転数を変
えたこと以外は実験例1と同様に行った。結果を表3に
示す。
Experimental Example 3 The experiment was performed in the same manner as in Experimental Example 1 except that the continuous kneading apparatus shown in FIG. 1 was used and the rotation speed of the stirring blade was changed. Table 3 shows the results.

【0022】[0022]

【表3】 [Table 3]

【0023】実験例4 図1に示す連続混練装置を使用し、粉末状水硬性材料1
00重量部に対する混練水量を変えたこと以外は実験例
1と同様に行った。結果を表4に示す。
Experimental Example 4 Using the continuous kneading apparatus shown in FIG.
The experiment was performed in the same manner as in Experimental Example 1 except that the amount of kneading water was changed with respect to 00 parts by weight. Table 4 shows the results.

【0024】[0024]

【表4】 [Table 4]

【0025】[0025]

【発明の効果】以上説明したように、本発明によれば以
下の効果を奏する。本発明の連続混練装置を用いること
により、粉末状水硬性材料と水とを連続的に混練するこ
とができる。特に、粉末状水硬性材料100重量部に対
し混練水量50重量部以上の範囲で均質な混練が可能と
なる。また、細骨材や粗骨材を含まないミルク状物の混
練に有効である。これにより、従来使用されてきたバッ
チ式ミキサの煩雑性や混練ロスを低減できる効果があ
る。
As described above, according to the present invention, the following effects can be obtained. By using the continuous kneading apparatus of the present invention, the powdery hydraulic material and water can be kneaded continuously. In particular, homogeneous kneading becomes possible in the range of 50 parts by weight or more of the mixing water with respect to 100 parts by weight of the powdery hydraulic material. It is also effective for kneading milk-like materials that do not contain fine aggregate or coarse aggregate. This has the effect of reducing the complexity and kneading loss of conventionally used batch mixers.

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

【図1】本発明の連続混練装置の一例を示す側面図であ
る。
FIG. 1 is a side view showing an example of a continuous kneading apparatus of the present invention.

【図2】従来の連続混練装置の側面図である。FIG. 2 is a side view of a conventional continuous kneading apparatus.

【図3】従来の連続混練装置の側面図である。FIG. 3 is a side view of a conventional continuous kneading apparatus.

【符号の説明】[Explanation of symbols]

1 動力源 2 動力伝達装置 3 回転シャフト 4 攪拌翼 5 水供給管 6 竪型ミキシング筒 7 竪型材料供給筒 8 ホッパー 9 粉末状水硬性材料 10 動力源 11 定量供給装置 12 材料供給口 13 混練物排出口 14 排出管 DESCRIPTION OF SYMBOLS 1 Power source 2 Power transmission device 3 Rotating shaft 4 Stirring blade 5 Water supply pipe 6 Vertical mixing cylinder 7 Vertical material supply cylinder 8 Hopper 9 Powdery hydraulic material 10 Power source 11 Quantitative supply device 12 Material supply port 13 Kneaded material Outlet 14 Outlet pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 那須 一郎 新潟県西頸城郡青海町大字青海2209番地 電気化学工業株式会社青海工場内 (72)発明者 伊藤 正明 新潟県西頸城郡青海町大字青海2209番地 電気化学工業株式会社青海工場内 Fターム(参考) 4G037 AA05 4G078 AA02 AA10 AA26 AB01 AB02 BA05 CA13 DA00 DA21 EA10 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Ichiro Nasu 2209 Aomi, Aomi-cho, Nishikubiki-gun, Niigata Inside the Aomi Plant of Denki Kagaku Kogyo Co., Ltd. 4G037 AA05 4G078 AA02 AA10 AA26 AB01 AB02 BA05 CA13 DA00 DA21 EA10

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 材料供給装置を竪型材料供給筒7に連接
し、粉末状水硬性材料9を竪型材料供給筒7へ連続的か
つ定量的に供給すると共に、該竪型材料供給筒7の下部
に設置される竪型ミキシング筒6の側面に水供給管5を
設け、水を連続的かつ定量的に供給し、竪型ミキシング
筒6の底部に粉末状水硬性材料9と水とを混練する攪拌
翼4を設け、連続で混練し、該竪型ミキシング筒6の側
面下部の混練物排出口13に接続された排出管14を、
その先端が前記排出口13より高い位置になるように立
ち上げ、竪型ミキシング筒6内の混練物を滞留させるよ
うにしたことを特徴とする粉末状水硬性材料の連続混練
装置。
1. A material supply device is connected to a vertical material supply cylinder to continuously and quantitatively supply a powdery hydraulic material to the vertical material supply cylinder. A water supply pipe 5 is provided on the side of a vertical mixing cylinder 6 installed at the bottom of the vertical mixing cylinder 6 to supply water continuously and quantitatively, and a powdery hydraulic material 9 and water are supplied to the bottom of the vertical mixing cylinder 6. A stirring pipe 4 for kneading is provided, kneading is performed continuously, and a discharge pipe 14 connected to a kneaded material discharge port 13 at a lower side of the vertical mixing cylinder 6 is connected to
A continuous kneading apparatus for a powdery hydraulic material, characterized in that the tip is raised so as to be at a position higher than the discharge port 13 and the kneaded material in the vertical mixing cylinder 6 is retained.
JP16835999A 1999-06-15 1999-06-15 Continuous kneading equipment for powdery hydraulic materials Expired - Lifetime JP3736990B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16835999A JP3736990B2 (en) 1999-06-15 1999-06-15 Continuous kneading equipment for powdery hydraulic materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16835999A JP3736990B2 (en) 1999-06-15 1999-06-15 Continuous kneading equipment for powdery hydraulic materials

Publications (2)

Publication Number Publication Date
JP2000354750A true JP2000354750A (en) 2000-12-26
JP3736990B2 JP3736990B2 (en) 2006-01-18

Family

ID=15866627

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16835999A Expired - Lifetime JP3736990B2 (en) 1999-06-15 1999-06-15 Continuous kneading equipment for powdery hydraulic materials

Country Status (1)

Country Link
JP (1) JP3736990B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010508180A (en) * 2006-11-01 2010-03-18 ユナイテッド・ステイツ・ジプサム・カンパニー Apparatus and method for wet mixing cement slurry for fiber reinforced structural cement panels
CN107715764A (en) * 2017-11-26 2018-02-23 抚州市鹤达实业有限公司 A kind of converted starch agitating device
CN117463240A (en) * 2023-12-27 2024-01-30 山西科福能源科技有限公司 Continuous production device for high-purity graphite

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5610325A (en) * 1979-07-05 1981-02-02 Nippon Kokudo Kaihatsu Kk Continuous mixer for powder with fluid
JPS5879530A (en) * 1981-11-04 1983-05-13 Kobe Steel Ltd Continuous kneader
JPH0725930U (en) * 1993-10-18 1995-05-16 株式会社今西 mixer
JPH0825343A (en) * 1994-07-13 1996-01-30 Tsukushi Kogyo Kk Mixing apparatus of cementitious injection material

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5610325A (en) * 1979-07-05 1981-02-02 Nippon Kokudo Kaihatsu Kk Continuous mixer for powder with fluid
JPS5879530A (en) * 1981-11-04 1983-05-13 Kobe Steel Ltd Continuous kneader
JPH0725930U (en) * 1993-10-18 1995-05-16 株式会社今西 mixer
JPH0825343A (en) * 1994-07-13 1996-01-30 Tsukushi Kogyo Kk Mixing apparatus of cementitious injection material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010508180A (en) * 2006-11-01 2010-03-18 ユナイテッド・ステイツ・ジプサム・カンパニー Apparatus and method for wet mixing cement slurry for fiber reinforced structural cement panels
CN107715764A (en) * 2017-11-26 2018-02-23 抚州市鹤达实业有限公司 A kind of converted starch agitating device
CN117463240A (en) * 2023-12-27 2024-01-30 山西科福能源科技有限公司 Continuous production device for high-purity graphite
CN117463240B (en) * 2023-12-27 2024-03-29 山西科福能源科技有限公司 Continuous production device for high-purity graphite

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