JPH09294925A - Powder mixing apparatus - Google Patents

Powder mixing apparatus

Info

Publication number
JPH09294925A
JPH09294925A JP8111547A JP11154796A JPH09294925A JP H09294925 A JPH09294925 A JP H09294925A JP 8111547 A JP8111547 A JP 8111547A JP 11154796 A JP11154796 A JP 11154796A JP H09294925 A JPH09294925 A JP H09294925A
Authority
JP
Japan
Prior art keywords
tank
powder
mixed
mixing
mixing apparatus
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
JP8111547A
Other languages
Japanese (ja)
Other versions
JP3209088B2 (en
Inventor
Hitoshi Ogata
仁 緒形
Shinji Sakuragi
信司 桜木
Atsushi Hasegawa
敦 長谷川
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi 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 Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP11154796A priority Critical patent/JP3209088B2/en
Publication of JPH09294925A publication Critical patent/JPH09294925A/en
Application granted granted Critical
Publication of JP3209088B2 publication Critical patent/JP3209088B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a powder mixing apparatus which can homogenize even a mixture in which a large amount of powder is added with only a small amount of another kind of powder. SOLUTION: The upper part of the second hopper-shaped tank 32 is made to communicate with the bottom part of the first tank 31 through piping 34 with a butterfly type intermediate valve 33. The bottom part of the second tank 32 is made to communicate with the upper part of the first tank 31 by piping 36 with a rotary valve 35 and piping 38 for pneumatic transportation with a valve 37. Powder is mixed by being circulated between the tanks 31, 32.

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】本発明は粉体混合装置に係
り、特に第1の粉体に対しそれとは別種の粉体を少量だ
け添加混合する場合にきわめて均一に混合することがで
きる粉体混合装置に関する。詳しくは、重力流れを利用
したタイプの粉体混合装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powder mixing apparatus, and more particularly, to a powder mixing method in which a powder of a different type from the first powder can be mixed very uniformly when added in a small amount. Regarding the device. More specifically, the present invention relates to a powder mixing device of the type that uses gravity flow.

【0002】[0002]

【従来の技術】動力流れを利用した重力混合型混合機と
しては、図3(a)に示す導入管、合流室形、図3
(b)に示す樹脂状内筒形、図3(c)に示す断続内筒
形などがある。この重力混合型混合機の原理は、貯槽内
を重力流動する粉体を定量ずつ貯槽の各部より取出し集
合させて均一な混合物とするというものである。この重
力混合型混合機は、粉体物性のあまり差のない粉体の大
量混合を行う場合に使用されるが、粒度分布の幅が広い
粉体では偏析をおこすことがある。
2. Description of the Related Art As a gravity mixing type mixer utilizing a power flow, an introduction pipe shown in FIG.
There are a resin-like inner cylindrical shape shown in (b) and an intermittent inner cylindrical shape shown in FIG. 3 (c). The principle of this gravity-mixing type mixer is that a quantity of powder that gravity-flows in the storage tank is taken out from each part of the storage tank in a fixed amount and collected to form a uniform mixture. This gravity mixing type mixer is used when a large amount of powders having little difference in powder properties are mixed, but segregation may occur in powders having a wide particle size distribution.

【0003】なお、図3(a)において、混合槽1内に
多数の導入管2が配設され、各導入管2の上端がノズル
(開口部)3となっている。この混合槽1の中央流下口
4の下側に合流室5が設けられ、その中にも導入管6が
配設されている。各導入管2,6と中央流下口4からの
粉体が合流室5内で混ざり合い、出口7から取り出され
る。
In FIG. 3A, a large number of introducing pipes 2 are arranged in the mixing tank 1, and the upper end of each introducing pipe 2 is a nozzle (opening) 3. A merging chamber 5 is provided below the central flow port 4 of the mixing tank 1, and an introducing pipe 6 is also disposed therein. The powders from the respective introduction pipes 2 and 6 and the central flow-down port 4 are mixed in the merging chamber 5 and taken out from the outlet 7.

【0004】図3(b)において、混合槽10内の中央
に内筒(垂直内筒)11が立設され、それから多数の樹
枝状内筒12が斜めに分岐している。各樹枝状内筒12
の先端が開口しており、各内筒12内に取り込まれた粉
体が内筒11内で混ざり合い、出口13から取り出され
る。
In FIG. 3 (b), an inner cylinder (vertical inner cylinder) 11 is erected at the center of the mixing tank 10, and a large number of dendritic inner cylinders 12 are obliquely branched therefrom. Each dendritic inner cylinder 12
Of the inner cylinder 12 is open, and the powders taken in the inner cylinders 12 are mixed in the inner cylinder 11 and taken out from the outlet 13.

【0005】図3(c)において、貯槽15内に配管1
6から導入された粉体は、多孔板17あるいは内筒18
を通って次第に落下し、混合される。混合粉体は、ロー
タリバルブ19及び配管20を経て取り出される。な
お、配管20の切換え弁21から分岐した配管22を介
して粉体が槽体15の上部に循環可能とされている。な
お、貯槽15の上部には粉体分離器(セパレータ)23
が設置され、除塵した空気を大気中へ排出可能としてい
る。
In FIG. 3C, the pipe 1 is placed in the storage tank 15.
The powder introduced from 6 is the perforated plate 17 or the inner cylinder 18
Gradually falls through and is mixed. The mixed powder is taken out through the rotary valve 19 and the pipe 20. It should be noted that the powder can be circulated to the upper portion of the tank body 15 via a pipe 22 branched from a switching valve 21 of the pipe 20. A powder separator (separator) 23 is provided above the storage tank 15.
Is installed so that the dust-free air can be discharged into the atmosphere.

【0006】[0006]

【発明が解決しようとする課題】種々の研究の結果、上
記従来の重力型混合機においては、例えばセメントに対
し添加剤を混合する場合のように、第1の粉体(例えば
セメント)に対しそれとは別種の第2の粉体(例えば、
添加剤)を少量だけ添加混合する場合、混合後の均一度
が不十分であることが認められた。
As a result of various researches, in the above-mentioned conventional gravity type mixer, as in the case where an additive is mixed with cement, for example, the first powder (for example, cement) is added. A second powder of a different type (eg,
When only a small amount of (additive) was added and mixed, it was found that the uniformity after mixing was insufficient.

【0007】本発明は、このような従来技術の問題点を
解決し、多量の粉体に対し別種の粉体を少量だけ添加混
合する場合でもきわめて均一に混合することができる粉
体混合装置を提供することを目的とする。
The present invention solves the above-mentioned problems of the prior art and provides a powder mixing apparatus capable of extremely uniformly mixing a large amount of powder even when a small amount of another kind of powder is added and mixed. The purpose is to provide.

【0008】[0008]

【課題を解決するための手段】本発明の粉体混合装置
は、被処理粉体が導入される第1のタンクと、該第1の
タンクから粉体が第1の輸送手段を介して導入される第
2のタンクと、該第2のタンクから粉体を第1のタンク
へ戻す第2の輸送手段と、を備えてなり、該第1及び第
2の輸送手段のうち少なくとも一方が空気輸送装置より
なるものである。
In the powder mixing apparatus of the present invention, the first tank into which the powder to be treated is introduced and the powder from the first tank are introduced via the first transportation means. And a second transportation means for returning the powder from the second tank to the first tank, at least one of the first and second transportation means being air. It consists of a transportation device.

【0009】かかる粉体混合装置にあっては、第1のタ
ンクに複数の粉体を所要量ずつ供給し、(なお、これら
の粉体は予めある程度混合されていても良く、全く混合
されていなくても良い。)次いで、第1のタンクの粉体
を第2のタンクに移し、再び第2のタンクから第1のタ
ンクへ戻す。これを1サイクルとし、複数サイクル繰り
返す。このタンク間の移送のうち少なくとも一方は空気
輸送であるため、粉体が空気輸送される間に十分に混合
されるようになる。
In such a powder mixing apparatus, a plurality of powders are supplied to the first tank in a required amount each (these powders may be mixed to some extent in advance, or they may not be mixed at all). Then, the powder in the first tank is transferred to the second tank and then returned from the second tank to the first tank again. This is set as one cycle, and a plurality of cycles are repeated. At least one of the transfers between the tanks is pneumatic, so that the powder is well mixed while pneumatically transported.

【0010】また、一方のタンク内から他方のタンク内
へ輸送される粉体は、該他方のタンク内に投入された時
に混合されるようになり、タンク内の粉体全体としての
混合の均一度が高いものとなる。
Further, the powder particles transported from one tank to the other tank are mixed when they are charged into the other tank, and the mixing of the powder particles in the tank as a whole is made uniform. Once it becomes expensive.

【0011】本発明では、第2のタンクが第1のタンク
の下方に配置されており、第1のタンクの底部と第2の
タンクの上部とが、バルブを介して粉体が重力落下によ
って供給可能に連通されていることが好ましい。
According to the present invention, the second tank is arranged below the first tank, and the bottom portion of the first tank and the top portion of the second tank are gravitationally dropped through the valve. It is preferable that they are connected so that they can be supplied.

【0012】このように構成することにより、バルブを
開けることにより第1のタンク内の粉体が第2のタンク
内に自重で落下するようになり、粉体移送のための動力
コストが大幅に低減される。
With this structure, the powder in the first tank falls into the second tank by its own weight by opening the valve, and the power cost for transferring the powder is significantly increased. Will be reduced.

【0013】[0013]

【発明の実施の形態】図1は実施の形態に係る粉体混合
装置の構成図であり、粉砕機から原料粉体(この実施の
形態にあっては、セメント約65重量%、石膏約34重
量%、添加剤約1重量%が粉砕機中で予めある程度混合
された粉体)がホッパ状の第1のタンク31へ供給され
る。この第1のタンク31の底部にホッパ状の第2のタ
ンク32の上部がバタフライ式中間バルブ33付き配管
34を介して連通されている。第2のタンク32の底部
と第1のタンク31の上部とは、ロータリバルブ35付
き配管36と、バルブ37付き空気輸送用配管38とに
より連通されている。この配管38にはブロワ39から
空気が供給され、粉体を空気輸送可能としている。配管
38からは製品取出用配管40が分岐しており、この配
管にもバルブ(図示略)が設けられている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a block diagram of a powder mixing apparatus according to an embodiment, in which raw material powder (about 65% by weight of cement and about 34 gypsum in this embodiment) is fed from a crusher. A powder in which 1% by weight of the additive and about 1% by weight of the additive are mixed in advance in the pulverizer) is supplied to the hopper-shaped first tank 31. An upper portion of a hopper-shaped second tank 32 is connected to a bottom portion of the first tank 31 via a pipe 34 with a butterfly type intermediate valve 33. The bottom of the second tank 32 and the top of the first tank 31 are connected by a pipe 36 with a rotary valve 35 and a pipe 38 for pneumatic transportation with a valve 37. Air is supplied to the pipe 38 from a blower 39 so that the powder can be transported by air. A product take-out pipe 40 is branched from the pipe 38, and a valve (not shown) is also provided in this pipe.

【0014】第1のタンク31の上部にはバグフィルタ
41が設けられ、第1のタンク31内の空気を除塵して
大気放出可能としている。なお、第2のタンク32内の
空気も、配管42を介して該バグフィルタ41に導入さ
れ、除塵された後、大気放出されるよう構成されてい
る。
A bag filter 41 is provided above the first tank 31 to remove air from the first tank 31 and release it into the atmosphere. The air in the second tank 32 is also introduced into the bag filter 41 through the pipe 42 to remove dust and then released into the atmosphere.

【0015】第1及び第2のタンク31,32には、そ
れぞれバイブレータ43,44と粉体重量検出用ロード
セル47とが設けられている。符号45はサンプリング
孔設置箇所を示す。
The first and second tanks 31 and 32 are provided with vibrators 43 and 44 and a powder weight detecting load cell 47, respectively. Reference numeral 45 indicates a sampling hole installation location.

【0016】次に、図2を参照してこの粉体混合装置に
よる粉体混合作動を説明する。なお、以下の作動制御は
コンピュータによって行われる。
Next, the powder mixing operation by this powder mixing apparatus will be described with reference to FIG. The following operation control is performed by a computer.

【0017】まず、第1のタンク(上部タンク)31に
粉体を所定量導入すると共に、バグフィルタ41を作動
させておく。次いで、混合回数の初期値を0とした後、
中間バルブ33を開け、タンク31のバイブレータ43
を作動させ、タンク1内の粉体の殆どすべてを第2のタ
ンク(下部タンク)32へ落下させる。
First, a predetermined amount of powder is introduced into the first tank (upper tank) 31, and the bag filter 41 is operated. Next, after setting the initial value of the number of times of mixing to 0,
The intermediate valve 33 is opened, and the vibrator 43 of the tank 31 is opened.
Is operated to drop almost all of the powder in the tank 1 into the second tank (lower tank) 32.

【0018】次いで、中間バルブ33を閉じ、バイブレ
ータ43を停止した後、ブロワ39及びロータリバルブ
35を運転開始する。これにより、タンク32内の粉体
が配管38を介してタンク31へ戻り始める。
Next, after closing the intermediate valve 33 and stopping the vibrator 43, the blower 39 and the rotary valve 35 are started to operate. As a result, the powder in the tank 32 begins to return to the tank 31 via the pipe 38.

【0019】タンク31内の粉体量が規定量まで増加し
てきたならば、タンク32のバイブレータ44の間欠作
動を開始させる。なお、ロータリバルブ35を始動して
から2時間経過してもタンク32内の粉体量が該規定量
にまで減少しないときにも、バイブレータ44の間欠作
動を開始させる。
When the amount of powder in the tank 31 has increased to the specified amount, the intermittent operation of the vibrator 44 of the tank 32 is started. The intermittent operation of the vibrator 44 is started even when the amount of powder in the tank 32 does not decrease to the specified amount even after 2 hours have passed since the rotary valve 35 was started.

【0020】その後、タンク31内の粉体量が予め設定
された設定量まで増加してきたならば、タイマーを始動
させ、ロータリバルブ35の回転をその後30分だけ継
続させる。
After that, when the amount of powder in the tank 31 has increased to a preset amount, the timer is started and the rotation of the rotary valve 35 is continued for 30 minutes thereafter.

【0021】30分経過後、ロータリバルブ35及びバ
イブレータ44を停止し、2分間待機した後、ブロワ3
9を停止する。次いで、混合回数Nを1だけ増す。
After 30 minutes, the rotary valve 35 and the vibrator 44 are stopped, and after waiting for 2 minutes, the blower 3
9 is stopped. Then, the mixing number N is increased by one.

【0022】この一連の混合サイクルを合計3回繰り返
した後、バグフィルタ41を停止し、混合終了とし、必
要に応じ混合された粉体を製品タンクへ空気輸送する。
After repeating this series of mixing cycles a total of three times, the bag filter 41 is stopped to terminate the mixing, and the mixed powder is pneumatically transported to the product tank as needed.

【0023】かかる粉体混合装置によると、微少量の速
硬性セメント混和材であっても、セメントおよび石膏に
対しきわめて十分に混合されることが認められた。これ
は、粉体が第1のタンク31から第2のタンク32へ落
下するとき、あるいは第2のタンクから第1のタンク3
1へ戻されるときに、粉体の全量がタンク32又は31
内で混合されると共に、タンク32からタンク31へ戻
る配管38内において十分に混合されるためであろうと
考えられる。
According to such a powder mixing apparatus, it was found that even a very small amount of the fast-hardening cement admixture can be mixed extremely well with cement and gypsum. This is when the powder falls from the first tank 31 to the second tank 32, or from the second tank to the first tank 3.
When it is returned to 1, the total amount of powder is in the tank 32 or 31.
It is considered that this is because it is sufficiently mixed within the pipe 38 that returns from the tank 32 to the tank 31 while being mixed inside.

【0024】なお、この原料粉体を図3に示した各種の
混合機を用いて混合してみたが、本発明の粉体混合装置
ほどには高均一度にまで混合することはできなかった。
The raw material powders were mixed using various mixers shown in FIG. 3, but they could not be mixed to the degree of uniformity as high as the powder mixing apparatus of the present invention. .

【0025】[0025]

【発明の効果】以上の通り、本発明の粉体混合装置によ
ると、粉体を高均一度にまで混合することができる。
As described above, according to the powder mixing apparatus of the present invention, powder can be mixed to a high degree of uniformity.

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

【図1】実施の形態に係る粉体混合装置の系統図であ
る。
FIG. 1 is a system diagram of a powder mixing device according to an embodiment.

【図2】実施の形態に係る粉体混合装置の作動を示すフ
ローチャートである。
FIG. 2 is a flowchart showing the operation of the powder mixing apparatus according to the embodiment.

【図3】従来例を示す断面図である。FIG. 3 is a cross-sectional view showing a conventional example.

【符号の説明】[Explanation of symbols]

31 第1のタンク 32 第2のタンク 35 ロータリバルブ 39 ブロワ 41 バグフィルタ 43,44 バイブレータ 47 ロードセル 31 First Tank 32 Second Tank 35 Rotary Valve 39 Blower 41 Bag Filter 43,44 Vibrator 47 Load Cell

フロントページの続き (72)発明者 長谷川 敦 福岡県北九州市八幡西区洞南町1番地1 三菱マテリアル株式会社セメント開発セン ター内Front Page Continuation (72) Inventor Atsushi Hasegawa 1 Konan-cho, Hachimansai-ku, Kitakyushu, Fukuoka 1 Mitsubishi Materials Corporation Cement Development Center

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 被処理粉体が導入される第1のタンク
と、 該第1のタンクから粉体が第1の輸送手段を介して導入
される第2のタンクと、 該第2のタンクから粉体を第1のタンクへ戻す第2の輸
送手段と、を備えてなり、該第1及び第2の輸送手段の
うち少なくとも一方が空気輸送装置よりなる粉体混合装
置。
1. A first tank into which a powder to be treated is introduced, a second tank into which powder is introduced from the first tank via a first transportation means, and a second tank And a second transporting means for returning the powder from the first transporting means to the first tank, wherein at least one of the first and second transporting means is an air transporting device.
【請求項2】 請求項1において、前記第2のタンクが
第1のタンクの下方に配置されており、第1のタンクの
底部と第2のタンクの上部とが、バルブを介して粉体が
重力落下によって供給可能に連通されていることを特徴
とする粉体混合装置。
2. The first tank according to claim 1, wherein the second tank is arranged below the first tank, and the bottom of the first tank and the top of the second tank are powdered via a valve. The powder mixing device is characterized in that it is connected so that it can be supplied by gravity falling.
JP11154796A 1996-05-02 1996-05-02 Powder mixing equipment Expired - Lifetime JP3209088B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11154796A JP3209088B2 (en) 1996-05-02 1996-05-02 Powder mixing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11154796A JP3209088B2 (en) 1996-05-02 1996-05-02 Powder mixing equipment

Publications (2)

Publication Number Publication Date
JPH09294925A true JPH09294925A (en) 1997-11-18
JP3209088B2 JP3209088B2 (en) 2001-09-17

Family

ID=14564155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11154796A Expired - Lifetime JP3209088B2 (en) 1996-05-02 1996-05-02 Powder mixing equipment

Country Status (1)

Country Link
JP (1) JP3209088B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010089446A1 (en) * 2008-12-29 2010-08-12 Upm-Kymmene Corporation Process and apparatus for the homogenization of feed stock
JP2012232866A (en) * 2011-04-28 2012-11-29 Tokuyama Corp Fired material production apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010089446A1 (en) * 2008-12-29 2010-08-12 Upm-Kymmene Corporation Process and apparatus for the homogenization of feed stock
CN102271793A (en) * 2008-12-29 2011-12-07 芬欧汇川有限公司 Process and apparatus for the homogenization of feed stock
JP2012232866A (en) * 2011-04-28 2012-11-29 Tokuyama Corp Fired material production apparatus

Also Published As

Publication number Publication date
JP3209088B2 (en) 2001-09-17

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