JPS62180732A - Vertical mixer - Google Patents

Vertical mixer

Info

Publication number
JPS62180732A
JPS62180732A JP61021125A JP2112586A JPS62180732A JP S62180732 A JPS62180732 A JP S62180732A JP 61021125 A JP61021125 A JP 61021125A JP 2112586 A JP2112586 A JP 2112586A JP S62180732 A JPS62180732 A JP S62180732A
Authority
JP
Japan
Prior art keywords
pellets
container
powder
blade
guide plate
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
JP61021125A
Other languages
Japanese (ja)
Other versions
JPH0217218B2 (en
Inventor
Haruyoshi Fujita
藤田 晴義
Takafumi Shimada
嶋田 隆文
Katsuaki Makino
槙野 勝昭
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP61021125A priority Critical patent/JPS62180732A/en
Publication of JPS62180732A publication Critical patent/JPS62180732A/en
Publication of JPH0217218B2 publication Critical patent/JPH0217218B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/92Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with helices or screws
    • B01F27/921Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with helices or screws with helices centrally mounted in the receptacle
    • B01F27/9212Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with helices or screws with helices centrally mounted in the receptacle with conical helices

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PURPOSE:To enhance the efficiency in mixing powdery particles by rotating a driving shaft which is arranged coaxially with a vessel, additionally providing an inclined blade or a spiralstrip blade for pushing up the powder to the driving shaft, and eliminating the vortex. CONSTITUTION:The charged pellets Z (A and B) are pushed up along the peripheral wall surface in the direction as shown by the arrow P by the rotation of a ribbon-type agitating blade 3. In this case, since the powder is forcibly guided by a guide plate 6 to the axial center part as shown by the arrow Q' in the surface layer, vortices are not formed on the surface layer, and the surface is practically flattened. Consequently, even the pellets having different particle diameters are moved in the same manner, stagnant parts are not formed, and the pellets are uniformly mixed. The guide plate 6 is appropriately allowed to slide up and down.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は粉粒体を混合する竪形混合装置に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a vertical mixing device for mixing powder and granular materials.

(従来の技術) 粉粒体を混合処理する操作は化学工業、黙業等の多くの
分野で生じるものであり、混合操作で均一な混合を達成
することは製品々質上極めて重要である。
(Prior Art) The operation of mixing powder and granules occurs in many fields such as the chemical industry and industrial industry, and achieving uniform mixing in the mixing operation is extremely important in terms of product quality.

これらの用に供される回転式の攪拌翼を内部に設置した
竪形混合装置は、設置面積が少くてすみ、粉粒体の送入
、抜取シが容易で、かつ、構造が単純で維持管理が簡単
である特徴を持っているために多用されているが、混合
性能については細形式、例えばV型、ダブルコーン型と
呼ばれる容器本体が水平に設けられた回転軸によ多回転
する混合器に較べ劣る欠点がある。
Vertical mixing devices with rotating stirring blades installed inside are used for these purposes, require less installation space, are easy to feed and extract powder and granules, and have a simple structure that is easy to maintain. It is widely used because it is easy to manage, but in terms of mixing performance, narrow types, such as V-type and double-cone type containers, have a horizontally installed container body that rotates multiple times on a rotating shaft. It has some disadvantages compared to pottery.

従来の竪型混合装置を図によシ説明する。第3図に示す
混合装置の構成は、円錐型の竪型固定容器の内部中心に
、リボン型攪拌羽根(螺旋帯翼)を設けたものであり、
1は竪型逆円錐状容器の本体、2は攪拌用の駆動軸であ
り、これにリボン状の攪拌羽根3が支腕を介して固定さ
れている。4は混合清粉粒体の排出口、5は混合すべき
粉粒体の入口である。
A conventional vertical mixing device will be explained with reference to the drawings. The configuration of the mixing device shown in FIG. 3 is such that a ribbon-type stirring blade (spiral band blade) is provided at the center of the interior of a conical vertical fixed container.
1 is a main body of a vertical inverted conical container, 2 is a drive shaft for stirring, and a ribbon-shaped stirring blade 3 is fixed to this via a support arm. Reference numeral 4 indicates an outlet for the mixed clean powder and granules, and 5 indicates an inlet for the powder and granules to be mixed.

第4図は上述構造の従来の混合装置に関する欠点を説明
する1例としてポリエステルペレットzの混合に適用し
た混合状態を示したものである。下記2′P!i類のポ
リニスチクペレットA。
FIG. 4 shows a mixing state applied to mixing polyester pellets z as an example to explain the drawbacks of the conventional mixing device having the above structure. 2'P below! Class I polynistic pellets A.

Bが重量比で一=コーの割合 B Oペレット人(寸法 8111mφ×10醪 密度 0
.5 fr/q)OペレットB(寸法 3咽φ× 3圏
 密度 Q、81r膚)で挿入され、混合した場合ペレ
ットはリボン型回転羽根1の回転によシ、矢印Pで示し
たペレットzめ動き方向のように容器周壁面を上昇し、
その後、矢印Q、Rの如く内部中心の下方に向い下降す
る。その形態は第4図で明らかなとおシ、攪拌羽根1の
遠心力によシベンツ)Zは周壁を迫シ上がシ、中央が沈
降するいわゆるポルテックス状を呈するため、粒径の大
きなペレット人が、粒径の小さなベンツ)Bよシ斜面を
ころげやすく容器中央にあつまる0このため中間には粒
径め小さなベンツ)Bのゾーンができるため動きの悪い
停滞部ができて均一な混合が不可能であった。第1表は
、上記従来例においての混合器内の混合度を測定するた
めに、下部排出口よシ排出しながらサンプリングし、ペ
レット人の濃度を測定した結果であり、標準偏差値σn
=98と大きく混合性能が悪い欠点が判明した0 第1表 (発明が解決しよ□うとする問題点) 本発明は従来の竪形混合装置の欠点を解消し、混合装置
の容器壁に沿りて押し上げられた粉粒体を容器の中心部
に誘導して粉粒体の表層を平らKすることによシ、ポル
テックスを消滅させ、粉粒体の混合性能を向上させた竪
型混合装置を提供しよ□:うとするものである。
B is 1 in weight ratio = proportion of Coe B O pellet person (Dimensions 8111 mφ x 10 mash Density 0
.. 5 fr/q) O pellet B (dimensions 3 throats φ x 3 circles density Q, 81r skin) is inserted and mixed, the pellets are rotated by the ribbon-shaped rotating blade 1, and the pellets z indicated by arrow P are inserted. Rise up the container peripheral wall surface in the direction of movement,
Thereafter, it descends downward toward the center of the interior as indicated by arrows Q and R. Its form is clearly seen in Figure 4. Due to the centrifugal force of the stirring blade 1, Z is shaped like a portex in which the peripheral wall is pushed up and the center settles, so that pellets with large particle sizes are , Benz) B with a small particle size easily rolls down the slope and collects in the center of the container 0 Therefore, a zone of Benz) B with a smaller particle size is created in the middle, creating a stagnation area with poor movement, making it impossible to mix uniformly. Met. Table 1 shows the results of measuring the concentration of pellets by sampling while discharging from the lower discharge port in order to measure the degree of mixing in the mixer in the above conventional example, and the standard deviation value σn
Table 1 (Problems to be Solved by the Invention) The present invention solves the drawbacks of the conventional vertical mixing device, and it A vertical mixing device that improves the mixing performance of powder and granules by guiding the pushed up powder to the center of the container and flattening the surface layer of the powder, thereby eliminating portex. □: Provide what you are trying to do.

(問題点を解決するための手段) 本発□明は竪形円筒形又は竪形逆円錐形の容器内部に□
、″該容器軸線と同軸に配置した駆動軸を回転さ贅□る
ことによシ容器周辺部の粉粒体を上方に押し上げる機能
を有する傾斜翼又は螺旋帯翼を該駆動軸に付設し、同傾
斜翼又は螺旋帯翼の上部に□押し上げられた粉粒体を容
器中心部に案内する機能を有する案内板を上記容器内上
部に付設したととを特徴とする竪形混合装置である0 
 ′ (実施例) 以下、本発明装置の一実施例を第1図に従って詳述する
(Means for Solving the Problems) The present invention has a vertical cylindrical or vertical inverted conical container.
``By rotating a drive shaft disposed coaxially with the axis of the container, an inclined blade or a spiral band blade is attached to the drive shaft, which has the function of pushing up the powder and granules in the periphery of the container, A vertical mixing device characterized in that a guide plate is attached to the upper part of the container, which has a function of guiding the granular material pushed up to the center of the container on the upper part of the inclined blade or the spiral band blade.
(Embodiment) An embodiment of the apparatus of the present invention will be described below in detail with reference to FIG.

第1図はポリエステルベンツ)Zの混合装置に適用した
例を示すものである。第1図において、1′は竪型逆円
錐状の混合容器本体、2は攪拌用の駆動軸であり、これ
にリボン状の攪拌羽根3が固定されている。4は厳科ペ
レットの装入口、―は製品排出口である。また6は器壁
表層のペレットを容器中心部に案内する案内板であって
、その形態は第1・図(t)) K示すように、2枚の
湾曲した板帯であって、その1圏部は夫々容器本体10
周壁に接し、他端部は、駆動軸2付近に延在し、□かつ
これらの案内板6,6は該軸2に関し点対称の位ff!
111C配置設されている。
FIG. 1 shows an example in which the present invention is applied to a mixing device for polyester benz). In FIG. 1, 1' is a vertical inverted conical mixing container body, 2 is a stirring drive shaft, and a ribbon-shaped stirring blade 3 is fixed to this. 4 is the loading port for the strict pellets, and - is the product discharge port. 6 is a guide plate that guides the pellets on the surface of the vessel wall to the center of the vessel, and its form is as shown in Fig. 1 (t) K, which consists of two curved plate bands. Each part is the container body 10
The other end is in contact with the peripheral wall and extends near the drive shaft 2, and these guide plates 6, 6 are point symmetrical with respect to the shaft 2 ff!
111C is installed.

尚、案内板61の配置数は任意である。7は案内板の固
定具を・示すもの・である。なおこの案内板7は上下に
スライドしりミよう・K設けることが好ましい。案内板
を上下に移動することによシ、ペレット表層面の形態を
変えることが簡単に行える。
Note that the number of guide plates 61 to be arranged is arbitrary. 7 indicates a fixture for the guide plate. Note that it is preferable that this guide plate 7 is provided with a sliding guide plate 7 up and down. By moving the guide plate up and down, the shape of the pellet surface can be easily changed.

なお、混合容器本体の形状は竪形円筒形容器としても効
果は同様である〇 (作用) 第2図は前記従来例と同様に、粒径の異る2種類のペレ
ット人、Bを用いて、本発明で設置した案内板60機能
を説明したものである。
Note that even if the shape of the mixing container body is a vertical cylindrical container, the effect is the same. (Function) Figure 2 shows the case where two types of pellets B with different particle sizes are used, as in the conventional example. , which explains the function of the guide plate 60 installed in the present invention.

挿入されたペレットz(ム、B)は、リボン型攪拌羽根
3の回転によシ、矢印pの如く周壁面を上昇するが、表
層面において案内板6により矢印Q′で示すように強制
的に軸中心部に案内されるため、表層面はポルテックス
状を呈することなく、はぼ平となシ粒径の異るベレット
でも、同じ動きをすることKより動きの悪い停滞部が存
在しなくなりペレットは均一に混合される。
The inserted pellets z (mu, B) move up the peripheral wall surface as shown by the arrow p due to the rotation of the ribbon-type stirring blade 3, but are forcibly moved by the guide plate 6 on the surface layer as shown by the arrow Q'. Since the pellet is guided to the center of the shaft, the surface layer is flat without exhibiting a portex-like shape.Even pellets with different grain sizes move in the same way.There is no stagnant part where movement is slower than K. The pellets are mixed evenly.

(効果) 第2表は混合容器内の混合度を測定するために、下部排
出口より排出しながらサンプリングし、ベレットムの濃
度を測定した結果であり、標準偏差値σ。=1.3と小
さく混合性能が向上した0 (発明の効果) 本発明は上記構成を採用することKより、従来装置にお
ける表層面のポルテックスを消滅させ、粒径の大きな粉
粒体の中央部へのころがシによる偏在を防ぎ、結果とし
て、粉粒体の均一な混合を可能とした。
(Effects) Table 2 shows the results of sampling while discharging from the lower outlet in order to measure the degree of mixing in the mixing container, and measuring the concentration of Beretum, and the standard deviation value σ. = 1.3, and the mixing performance was improved. The rollers prevented uneven distribution due to grains, and as a result, it was possible to mix the powder and granules uniformly.

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

第1図は本発明による竪型混合装置の概要図で、同図(
a)は縦断面図、同図(1))は矢視ムー人断面図であ
る。第2図は第1図の装置における攪拌混合状態図であ
る。第3図は従来の竪型混合装置の概要図、第4図は第
3図の装置における攪拌混合状態図である。 復代理人  内 1)  明 復代理人  萩 原 亮 − 復代理人  安 西 篤 夫 第3図
FIG. 1 is a schematic diagram of a vertical mixing device according to the present invention.
A) is a longitudinal cross-sectional view, and (1)) is a cross-sectional view taken in the direction of the arrows. FIG. 2 is a diagram of the stirring and mixing state in the apparatus of FIG. 1. FIG. 3 is a schematic diagram of a conventional vertical mixing device, and FIG. 4 is a diagram of the stirring and mixing state in the device of FIG. 3. Sub-Agents 1) Meifuku Agent Ryo Hagiwara - Sub-Agent Atsuo Anzai Figure 3

Claims (1)

【特許請求の範囲】[Claims] 竪形円筒形又は竪形逆円錐形の容器内部に、該容器軸線
と同軸に配置した駆動軸を回転させることにより容器周
辺部の粉粒体を上方に押し上げる機能を有する傾斜翼又
は螺旋帯翼を該駆動軸に付設し、同傾斜翼又は螺旋帯翼
の上部に押し上げられた粉粒体を容器中心部に案内する
機能を有する案内板を上記容器内上部に付設したことを
特徴とする竪形混合装置。
Inclined blades or spiral band blades inside a vertical cylindrical or vertical inverted conical container that have the function of pushing up the powder and granules in the periphery of the container by rotating a drive shaft arranged coaxially with the axis of the container. is attached to the drive shaft, and a guide plate is attached to the upper part of the container, the guide plate having the function of guiding the powder pushed up to the upper part of the inclined blade or the spiral band blade to the center of the container. Shape mixing device.
JP61021125A 1986-02-04 1986-02-04 Vertical mixer Granted JPS62180732A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61021125A JPS62180732A (en) 1986-02-04 1986-02-04 Vertical mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61021125A JPS62180732A (en) 1986-02-04 1986-02-04 Vertical mixer

Publications (2)

Publication Number Publication Date
JPS62180732A true JPS62180732A (en) 1987-08-08
JPH0217218B2 JPH0217218B2 (en) 1990-04-19

Family

ID=12046165

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61021125A Granted JPS62180732A (en) 1986-02-04 1986-02-04 Vertical mixer

Country Status (1)

Country Link
JP (1) JPS62180732A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010058088A (en) * 2008-09-05 2010-03-18 Okawara Mfg Co Ltd Apparatus for mixing processing of conical ribbon with improved detergency and maintenance property
NL1037079C2 (en) * 2009-06-26 2010-12-28 Lekner B V MIXER FOR PREPARING A LOW FISH FISH MIXTURE.

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010058088A (en) * 2008-09-05 2010-03-18 Okawara Mfg Co Ltd Apparatus for mixing processing of conical ribbon with improved detergency and maintenance property
NL1037079C2 (en) * 2009-06-26 2010-12-28 Lekner B V MIXER FOR PREPARING A LOW FISH FISH MIXTURE.

Also Published As

Publication number Publication date
JPH0217218B2 (en) 1990-04-19

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