JPS62117621A - Mixing and kneading method - Google Patents
Mixing and kneading methodInfo
- Publication number
- JPS62117621A JPS62117621A JP60256646A JP25664685A JPS62117621A JP S62117621 A JPS62117621 A JP S62117621A JP 60256646 A JP60256646 A JP 60256646A JP 25664685 A JP25664685 A JP 25664685A JP S62117621 A JPS62117621 A JP S62117621A
- Authority
- JP
- Japan
- Prior art keywords
- mixing
- kneading
- package
- mixer
- cleaning
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
- B01F31/55—Mixers with shaking, oscillating, or vibrating mechanisms the materials to be mixed being contained in a flexible bag submitted to periodical deformation
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、医薬品、工業薬品、ビーズ類、顔料などの混
合およびインク、樹脂、セメント質材料などの混練方法
に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for mixing pharmaceuticals, industrial chemicals, beads, pigments, etc., and kneading inks, resins, cementitious materials, etc.
従来、粉体の混合においては、V型グレンダーに代表さ
れるような重力落下形式の混合機、あるいはポール・ミ
ルに代表されるような粉砕混合形式のもの、またロッキ
ング・ミキサのような回転揺動式形式のものと各種の機
器が使用されている。また、液体の混合に際して使用さ
れる攪拌機は、プロペラあるいはスクリューによる強制
攪拌タイプのものが一般的である。一方、混線について
は、ゴム、デフスチツク等の高粘性物質を除くほとんど
のものに、高トルクの強制攪拌ミキサが使用されている
。これらの機器は、大量混合、混線の場合や単一品種の
混合、混練には、高能率でありふされしいものである。Traditionally, powder mixing has been carried out using gravity drop type mixers such as V-type grinders, pulverized mixers such as pole mills, and rotary shakers such as rocking mixers. A dynamic type and various types of equipment are used. Further, the stirrer used for mixing liquids is generally of a forced stirring type using a propeller or a screw. On the other hand, as for crosstalk, high torque forced stirring mixers are used for most things except for high viscosity substances such as rubber and differential sticks. These devices are highly efficient and suitable for mass mixing, cross-mixing, and single variety mixing and kneading.
しかしながら、少量、多品種の混合、混線の場合には、
使用ごとに機器の清掃とプロペラあるいはスクリュー等
の調整(以下単に調整という)に時間がかかる欠点を有
している。また、医薬品や顔料などを混合する場合には
、添加する成分の微妙な差により効果に大きな違いが生
ずること、また少量成分の逸散やロット間のばらつきの
問題などもあるため、混合機器の清掃、調整には、非常
な時間が必要であった。However, in the case of small quantities, mixtures of many types, and cross-wires,
The drawback is that it takes time to clean the equipment and adjust the propeller, screw, etc. (hereinafter simply referred to as adjustment) after each use. Furthermore, when mixing pharmaceuticals, pigments, etc., subtle differences in the ingredients added can make a big difference in the effect, and there are also issues such as escaping of small amounts of ingredients and variations between lots, so it is important to consider the need for mixing equipment. Cleaning and adjustment required a lot of time.
一方、混練方法においても同様のことが言え、特にエポ
キシ樹脂のように硬化速度の速いものやセメント系材料
のように工事現場で少量ずつ、くυ返し混l[υする場
合には、洗い水の確保および混練機の清掃、調整に非常
な労力が必要であった。On the other hand, the same thing can be said about the kneading method, especially for materials such as epoxy resins that harden quickly or cement-based materials, which are mixed in small quantities at the construction site. A great deal of effort was required to ensure that the mixer was clean, and to clean and adjust the kneading machine.
本発明者らは、現行の混合方法、混練方法と比較し、混
合性状、混練性状に遜色がなく、かつ機器の清掃、調整
が不必要で、かつ、微量成分の逸散が無い混合方法ある
いは混練方法について、種々検討した結果、揺動式ミキ
サ(重力式ミキサともいう)と包装を用いれば良いこと
を知見して本発見を完成するに到った。The present inventors have developed a mixing method or kneading method that is comparable in mixing and kneading properties to current mixing methods and kneading methods, does not require cleaning or adjusting equipment, and does not cause trace components to escape. As a result of various studies regarding the kneading method, it was discovered that a rocking mixer (also called a gravity mixer) and packaging could be used, leading to the completion of this discovery.
即ち、本発明は、モーターの回転運動を混合あるいは混
練槽の揺動運動に変換するタイプのミキサと包装を用い
て混合、混練する方法である。That is, the present invention is a method of mixing and kneading using a mixer and packaging that converts the rotational motion of a motor into the oscillating motion of a mixing or kneading tank.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明に用いるミキサは、モーターの回転運動を混合槽
あるいは混練槽の揺動運動に変換するタイプのミキサ(
たとえば、千代田技研工業(株)製千代田ガpプロオム
ニ・ミキサ)で、かつ揺動サイケμが毎分100回以上
のもの、よυ好ましくは200回以上のものが良く、揺
動振幅が大きく、かつ揺動運動にむらの少ないものが良
い。まだ、揺動面は包装との接触面積の大きいほど混合
あるいは混練されるものに揺動運動が伝わυ混合、混練
性状が良好となり、さらに揺動面が揺動運動の方向と直
角な運af、t。The mixer used in the present invention is a type of mixer (
For example, a Chiyoda Gap Pro Omni Mixer (manufactured by Chiyoda Giken Kogyo Co., Ltd.) with a vibration amplitude of 100 times or more per minute, preferably 200 times or more, and a large vibration amplitude. It is also better to have less uneven rocking motion. However, the larger the contact area of the oscillating surface with the packaging, the more oscillating motion is transmitted to the materials to be mixed or kneaded, υ, the better the mixing and kneading properties, and the more the oscillating surface moves perpendicular to the direction of the oscillating motion af. , t.
ていればさらに良好となる(たとえば、揺動向の円運動
など)。一方、包装に用いる材料(以下包装材料という
)は、紙、布、ゴム、塩ビシート、ポリエチレンシート
などいずれでも良いが、混合、混線状態を確認できるの
で、透明な材料が好ましい。It will be even better if there is a circular motion in the rocking motion, for example. On the other hand, the material used for packaging (hereinafter referred to as packaging material) may be any paper, cloth, rubber, PVC sheet, polyethylene sheet, etc., but a transparent material is preferable since mixing and cross-wire conditions can be confirmed.
包装材料の厚さ、弾性率、形状について特に限定しない
が、極端に薄い場合には、混合、混練時に破損する可能
性がある。ゴムを包装材料に用いる場合には、弾性率が
lX10’〜1×10’kp/α2の範囲のものが特に
良好である。There are no particular limitations on the thickness, elastic modulus, or shape of the packaging material, but if it is extremely thin, it may be damaged during mixing and kneading. When rubber is used as a packaging material, a rubber having an elastic modulus in the range of 1 x 10' to 1 x 10' kp/α2 is particularly good.
包装の形状に関しては、特別な制限はないが、混合、混
練槽内に入る大きさであっても揺動面よりも大きなもの
は効率が落ちるため好ましくない。特に混線の場合には
、揺動面との接触面積が少ないと十分な混練が行なわれ
ない場合もあるので、ザブトンのように平面方向の表面
積が広いものが好ましく、底面の長い寸法に対して高さ
は1/2程度以下が好ましい。There are no particular restrictions on the shape of the package, but even if the package is large enough to fit into the mixing and kneading tank, it is not preferable to use a package that is larger than the rocking surface because efficiency will drop. Particularly in the case of mixed wires, if the contact area with the swinging surface is small, sufficient kneading may not be achieved, so it is preferable to use a product with a wide surface area in the plane direction, such as Zabuton, and to accommodate the long dimension of the bottom. The height is preferably about 1/2 or less.
混練方法は、通常の方法でよいが、混練の中間時点で空
気抜きを行うのが、混練時間の短縮の面から、又、巻込
み空気量を減少させる意味から好ましい。The kneading method may be any conventional method, but it is preferable to remove air at an intermediate point in the kneading process from the viewpoint of shortening the kneading time and reducing the amount of air involved.
即ち、所定量の粉体及び水を包装に投入し、混練を開始
すると造粒される。混線が進むと造粒物は大形化してい
き、包装中の混練物容積の割合が減少する。そしてミキ
サの揺動面に接触する面の寸法に対する高さの割合が大
きくなる。That is, when a predetermined amount of powder and water are put into a package and kneading is started, the powder is granulated. As the mixing progresses, the size of the granulated material increases, and the volume ratio of the kneaded material in the packaging decreases. Then, the ratio of the height to the dimension of the surface that contacts the swinging surface of the mixer increases.
こ−で空気抜きを行うと高さに対する平面方向の表面積
が広くなるため、より揺動動力が伝達され混線が十分に
行われる。When air is vented in this manner, the surface area in the plane direction relative to the height becomes larger, so that more swinging power is transmitted and crosstalk is sufficiently performed.
以下、実施例で本発明の詳細な説明する。 Hereinafter, the present invention will be explained in detail with reference to Examples.
実施例1
表1に示す割合のセメント材料4ゆをポリエチレン製の
袋(内容f#tsz)に入れ揺動サイク/I/1200
回/分で5分間混練りした。混練完了後、テーブル・フ
ロー値を測定し、その後2.5鱈篩にてふるい、ままこ
の量を測定した。Example 1 Four pieces of cement material in the proportions shown in Table 1 were placed in a polyethylene bag (content f#tsz) and shaken using a rocking cycle/I/1200.
The mixture was kneaded for 5 minutes at a rate of 5 times/min. After the kneading was completed, the table flow value was measured, and then the mixture was sieved using a 2.5 cod sieve and the amount of raw material was measured.
また、セメント・ペーストの一部を4×4×16cWt
の角柱供試体に採り1.TIS標準養生を行い材令28
日の圧縮強度の確認を行った。それぞれの結果は表2に
示す。なお、混練後の清掃時間は0分であった。Also, some of the cement paste was 4x4x16cWt.
1. Perform TIS standard curing and use material regulation 28.
The compressive strength was confirmed. The results are shown in Table 2. Note that the cleaning time after kneading was 0 minutes.
表1
〔比較例〕
強制攪拌型上pタル・ミキサを使用し、実施例1に示す
配合のセメント材料2;5 kgをJISR5201に
規定する練り混ぜ方法にて混練し、その後実施例と同様
の試験を行った。結果は表2に示す。Table 1 [Comparative Example] Using a forced agitation type upper ptal mixer, 5 kg of cement material 2 of the formulation shown in Example 1 was kneaded by the mixing method specified in JISR5201, and then mixed in the same manner as in Example. The test was conducted. The results are shown in Table 2.
表2
く使用材料〉
セメントjd気化学工業(株)製、普通ボμトランドセ
メント
超a扮 フェロシリコン製造時の7リカダスト(平均
粒径α1μ)
減水剤 電気化学工業(株)製、商品名「FT−50
0」
主成分、アpキ!レナフタレンスp
ホン酸ホyムアμデヒド縮合物の
塩、固形分換算で使用
水 水道水
揺動式ミキサ・・・千代田技研工業(株)製千代田ガル
ゾロオムニφミキサ
型式:0M−5
強制攪拌型上μりμ・ミキサ
・・・(株)マルイ製 MIC−562−1型実施例2
相模川産天然砂を絶乾状Hまで乾燥後、JI81102
に規定する方法にて、1o)c!?ふるい分けを行い、
各サイズのふるいにとどまる量を測定し表5に示した。Table 2 Materials used〉 Cement JD manufactured by Kei Kagaku Kogyo Co., Ltd., ordinary bottled cement super a 7 lyca dust (average particle size α1μ) during the production of ferrosilicon Water reducing agent Manufactured by Denki Kagaku Kogyo Co., Ltd., product name: FT-50
0” Main ingredient, Apki! Lenaphthalene p Salt of phonic acid conjugate μ dehyde condensate, water used in terms of solid content Tap water oscillating mixer... Chiyoda Garzoro Omniφ mixer manufactured by Chiyoda Giken Co., Ltd. Model: 0M-5 Forced stirring type upper μ Mixer: MIC-562-1 model manufactured by Marui Co., Ltd. Example 2 After drying natural sand from Sagami River to bone dry H, JI81102
In the method prescribed in 1o)c! ? Perform sieving,
The amount remaining on each size sieve was measured and shown in Table 5.
その後、実施例1で用いたポリエチレン製袋体に総重量
が5ゆになるように、各粒度の砂を構成比に従って投入
し、揺動サイクI%/1000回/分で7分間混合した
。Thereafter, sand of each particle size was put into the polyethylene bag used in Example 1 according to the composition ratio so that the total weight was 5 Yu, and mixed for 7 minutes at an oscillation cycle of I%/1000 times/min.
混合終了後、ポリエチレン製袋から任意に1ゆの砂を採
取し同じ<JIsllozに規定する方法にて再度ふる
い分は試験を行った。その結果を表4に示す。After the mixing was completed, one ounce of sand was arbitrarily taken from the polyethylene bag and the sieved portion was tested again in the same manner as specified in <JIslloz. The results are shown in Table 4.
表5と表4の結果に基いて粒度分布図を作製したところ
第1図に示すように両者はほぼ等しい粒度分布を有する
ことが判明した。When a particle size distribution chart was prepared based on the results of Tables 5 and 4, it was found that both had substantially the same particle size distribution as shown in FIG.
なお、混合機の清掃時間は0分である。Note that the cleaning time of the mixer is 0 minutes.
使用材料 相模川産天然砂(比重2.58)Materials used Natural sand from Sagami River (specific gravity 2.58)
第1図は、天然砂をふるい分けた場合の粒度分布並びに
ふるいわけた各粒度の砂を構成比に従って本発明方法に
より混合した場合の砂の粒度分布を示す。FIG. 1 shows the particle size distribution when natural sand is sieved, and the particle size distribution of sand when the sieved sand of each particle size is mixed according to the composition ratio according to the method of the present invention.
Claims (1)
る方法。 2、被混練物を包装に内封し、揺動式ミキサにて混練す
る方法。[Claims] 1. A method in which the materials to be mixed are sealed in a package and mixed using a rocking mixer. 2. A method in which the material to be kneaded is sealed in a package and kneaded using a rocking mixer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60256646A JPS62117621A (en) | 1985-11-18 | 1985-11-18 | Mixing and kneading method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60256646A JPS62117621A (en) | 1985-11-18 | 1985-11-18 | Mixing and kneading method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62117621A true JPS62117621A (en) | 1987-05-29 |
JPH0425053B2 JPH0425053B2 (en) | 1992-04-28 |
Family
ID=17295497
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60256646A Granted JPS62117621A (en) | 1985-11-18 | 1985-11-18 | Mixing and kneading method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62117621A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994009895A1 (en) * | 1992-11-02 | 1994-05-11 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | Reactor system |
WO1996023581A1 (en) * | 1995-02-01 | 1996-08-08 | Duracell Inc. | Slurry forming process and slurry transfer and densification through vacuum pumping |
US5632554A (en) * | 1995-02-01 | 1997-05-27 | Duracell Inc. | Slurry forming process using an inflatable/collapsible bag within a mixing device |
-
1985
- 1985-11-18 JP JP60256646A patent/JPS62117621A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994009895A1 (en) * | 1992-11-02 | 1994-05-11 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | Reactor system |
US5525305A (en) * | 1992-11-02 | 1996-06-11 | Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno | In vitro model of an in vivo digestive tract |
WO1996023581A1 (en) * | 1995-02-01 | 1996-08-08 | Duracell Inc. | Slurry forming process and slurry transfer and densification through vacuum pumping |
US5632554A (en) * | 1995-02-01 | 1997-05-27 | Duracell Inc. | Slurry forming process using an inflatable/collapsible bag within a mixing device |
Also Published As
Publication number | Publication date |
---|---|
JPH0425053B2 (en) | 1992-04-28 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |