JPH04114427U - continuous mixer - Google Patents

continuous mixer

Info

Publication number
JPH04114427U
JPH04114427U JP2575091U JP2575091U JPH04114427U JP H04114427 U JPH04114427 U JP H04114427U JP 2575091 U JP2575091 U JP 2575091U JP 2575091 U JP2575091 U JP 2575091U JP H04114427 U JPH04114427 U JP H04114427U
Authority
JP
Japan
Prior art keywords
stirring
mixing
discharge hole
mixed
blades
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.)
Pending
Application number
JP2575091U
Other languages
Japanese (ja)
Inventor
伸敏 安藤
Original Assignee
三重機械鉄工株式会社
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 三重機械鉄工株式会社 filed Critical 三重機械鉄工株式会社
Priority to JP2575091U priority Critical patent/JPH04114427U/en
Publication of JPH04114427U publication Critical patent/JPH04114427U/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】 【目的】 砂利とセメント等の比重が大きく異なるか、
サイズが大きく異なる被混合物等を混合する混合機にお
いて、混合品質の向上と、連続して混合物を排出供給す
る混合物供給性能の向上を図る。 【構成】 堅形混合槽3の全体または少くとも下半部分
を、中空円錐形状の撹拌混合部5になすと共に、撹拌混
合部5の上方に被混合物の投入口9、撹拌混合部5の下
端を連続排出孔10になし、さらに、撹拌混合部5内
に、帯板12で形成されて巻き方向と巻き径を異にし、
かつ、それぞれが連続排出孔10の方向に巻き径を漸減
して同一方向に回転すると共に、帯板12の幅広面8を
回転中心7に臨ませて、幅広面8を回転中心7に対して
平行配列、または微傾斜配列になしたスパイラル形状の
撹拌混合羽根1・2を、少くとも一対設け、投入口9か
ら投入した被混合物を、撹拌混合羽根1・2によって撹
拌混合し、下端の連続排出孔10から連続排出する構造
が特徴である。
(57) [Summary] [Purpose] Is the specific gravity of gravel and cement significantly different?
In a mixer that mixes materials of widely different sizes, the mixing quality is improved and the mixture supply performance is improved by continuously discharging and supplying the mixture. [Structure] The entire or at least the lower half of the vertical mixing tank 3 is formed into a hollow conical stirring/mixing section 5, and there is an inlet 9 for materials to be mixed above the stirring/mixing section 5, and a lower end of the stirring/mixing section 5. is formed into a continuous discharge hole 10, and furthermore, a belt plate 12 is formed in the stirring and mixing part 5, and the winding direction and winding diameter are different.
In addition, each of them rotates in the same direction with the winding diameter gradually decreasing in the direction of the continuous discharge hole 10, and the wide surface 8 of the strip plate 12 faces the rotation center 7, and the wide surface 8 faces the rotation center 7. At least one pair of spiral-shaped stirring and mixing blades 1 and 2 arranged in a parallel or slightly inclined arrangement are provided, and the material to be mixed introduced from the input port 9 is stirred and mixed by the stirring and mixing blades 1 and 2, and the lower end is continuous. The structure is characterized by continuous discharge from the discharge hole 10.

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

本考案は、例えば水飴・アスファルト・高粘度糊、或は、石灰とセメント・砂 とセメント等の各種各様の固液系の物質群の混合物の生成に使用する連続混合機 に関するものである。 This invention can be applied to, for example, starch syrup, asphalt, high viscosity glue, or lime, cement, and sand. Continuous mixer used to produce mixtures of various solid-liquid substances such as and cement. It is related to.

【0002】0002

【従来の技術】[Conventional technology]

産業上利用される固液系の混合機は、対象混合物に適した多様な構造のものが 使用されている。しかし、その公知の混合機は、単体の混合槽に混合羽根を設け 、その混合槽に所定量の被混合物を投入して、混合羽根を上下作動または回転作 動させたり、混合槽自体を回転して所要時間混合処理し、しかるのち、その混合 槽から混合物を一括して取り出すと共に、次の加工サイクルの被混合物を投入し て混合処理を反覆する間欠生産タイプの混合機構造が共通的になっている。 Solid-liquid mixers used industrially have a variety of structures suitable for the target mixture. It is used. However, the known mixer is equipped with a mixing blade in a single mixing tank. , put a predetermined amount of materials to be mixed into the mixing tank, and move the mixing blade up and down or in rotation. Mix it for the required time by moving it or rotating the mixing tank itself, and then The mixture is taken out from the tank all at once, and the mixture for the next processing cycle is added. An intermittent production type mixer structure that repeats the mixing process has become common.

【0003】0003

【考案が解決しようとする課題】[Problem that the idea aims to solve]

以上の従来の混合機構造によると、比重差が大きい物質相互、または、粒子や 塊体のサイズ差が大きい物質相互、例えば砂利とセメントを混合させる場合は、 それ等の物理性状の異なる被混合物質は、それぞれ個別に分離凝集する定性があ ると共に、混合作用が不充分なデッドゾーンが混合槽内に存在するので、一様均 一な混合物が得難い難点がある。 According to the conventional mixer structure described above, substances with large specific gravity differences or particles or When mixing substances with large differences in aggregate size, such as gravel and cement, These mixed substances with different physical properties have a qualitative tendency to separate and aggregate individually. At the same time, there is a dead zone in the mixing tank where the mixing action is insufficient. The problem is that it is difficult to obtain a uniform mixture.

【0004】 そして、混合機による混合物の生成排出が間欠的になるので、量産ラインにお ける他の製造装置との連続性と整合性が得られず、撹拌混合処理を工程中に要す る量産ラインの生産性を阻害する要因となっている。0004 Since the mixer generates and discharges the mixture intermittently, the mass production line Continuity and consistency with other manufacturing equipment cannot be achieved, and stirring and mixing processing is required during the process. This is a factor that hinders the productivity of mass production lines.

【0005】 本考案は、以上の従来技術の難点を解消する連続混合機を提供するものである 。[0005] The present invention provides a continuous mixer that solves the above-mentioned difficulties of the conventional technology. .

【0006】[0006]

【課題を解決するための手段】[Means to solve the problem]

以上の技術課題を解決する本考案の連続混合機は「堅形混合槽の全体または少 くとも下半部分を、中空逆円錐状の撹拌混合部になすと共に、該撹拌混合部の上 方に被混合物投入部、該撹拌混合部の下端を混合物の連続排出孔になし、さらに 、該撹拌混合部内に、帯板で形成されて巻き方向と巻き径を異にすると共に、そ れぞれが該連続排出孔の方向に巻き径を漸減し、かつ、同一方向に回転する少く とも一対の撹拌混合羽根を設け、さらに、該撹拌混合羽根は、該帯板の幅広面を 該撹拌混合羽根の回転中心に臨ませ、該回転中心に対して該幅広面を平行配列、 または微傾斜配列になした構造」になっている。 The continuous mixer of the present invention solves the above technical problems. At least the lower half part is made into a hollow inverted conical stirring and mixing part, and the upper part of the stirring and mixing part is The lower end of the stirring and mixing part is made into a continuous discharge hole for the mixture, and , in the stirring and mixing part, is formed of a strip plate and has different winding directions and winding diameters. Each has a winding diameter that gradually decreases in the direction of the continuous discharge hole, and rotates in the same direction. A pair of stirring and mixing blades are provided in each case, and the stirring and mixing blades are arranged to cover the wide side of the strip. facing the rotation center of the stirring mixing blade, and arranging the wide surface parallel to the rotation center; Or a structure made in a slightly inclined array.

【0007】 なお、前記の撹拌混合羽根は前記の平行配列が原則であるが、微傾斜させると きは、被混合物の混合性を考慮して2°以内程度に傾斜させる。また、前記の連 続排出孔とは、混合槽内の混合物を意図的作業中断を除いて連続的に排出する排 出部を意味し、意図的な作業中断や非常停止・作業停止等に用いる閉鎖バルブを 設けることがある。[0007] In principle, the above-mentioned stirring mixing blades are arranged in parallel as described above, but if they are slightly tilted, In this case, the angle should be within 2° in consideration of the mixability of the materials to be mixed. Also, the above series A continuous discharge hole is an exhaust hole that continuously discharges the mixture in the mixing tank except during intentional work interruptions. A closing valve used for intentional work interruptions, emergency stops, work stoppages, etc. It may be provided.

【0008】[0008]

【作用】[Effect]

以上の構成の本考案の連続混合機は、中空逆円錐状をなして前記構成要件の少 くとも一対のスパイラル状の撹拌混合羽根を有する撹拌混合部が要部をなしてい るので、回転する一対の該撹拌混合羽根が、恰も薄い包丁を縦にして被混合物内 を激しく上下作動する状態を呈し、その上下作動が撹拌混合部内の各ポジシヨン において無数高密度に発生するので、比重差・サイズ差・粘性差が大きい難混合 性物群でも、極めて一様均一に混合される。 The continuous mixer of the present invention having the above configuration has a hollow inverted conical shape and meets the above-mentioned structural requirements. The main part is a stirring and mixing section with at least a pair of spiral stirring and mixing blades. The pair of rotating stirring and mixing blades inserts the thin knife vertically into the mixture. It exhibits a state in which it violently moves up and down, and the up and down movement affects each position in the stirring and mixing section. It is difficult to mix because there are large differences in specific gravity, size, and viscosity. Even the sex substances are mixed extremely uniformly.

【0009】 即ち、従来公知の撹拌機は、被混合物をまとめて上下混乱させる意図によって 構成されているので、恰も薄い包丁を横または斜めにして上下作動させる状態を 呈し、前記の難混合性物群は均一な混合物が生成できなかった。しかし、前記構 成の本考案の混合機は、前記の薄い包丁を縦にした上下作動を思想としているの で、極めて優れた混合作用を奏することができる。[0009] In other words, conventionally known stirrers are designed to mix the mixture up and down. Because it is structured, it is possible to operate the thin knife horizontally or diagonally up and down. However, it was not possible to form a homogeneous mixture with the above-mentioned group of difficult-to-mix substances. However, the structure The idea of the mixing machine of this invention is that the above-mentioned thin knife is vertically operated and operates vertically. Therefore, an extremely excellent mixing effect can be achieved.

【0010】 そして、その撹拌混合作用が、底すぼみの該撹拌混合部の下端まで連続され、 ネック状の該下端で仕上げ撹拌混合されながら、連続排出孔から連続排出される ので、従来の混合手段では一様な混合が得難い難混合性状を有する比重差の大き い被混合物群、サイズ差の大きい被混合物群、または、粘度差の大きい液状の被 混合物群等の場合でも、一様均一にして充分な混合形態の混合物が連続的に生成 できる。0010 Then, the stirring and mixing action is continued to the lower end of the stirring and mixing part in the bottom recess, It is continuously discharged from the continuous discharge hole while being finished agitated and mixed at the lower end of the neck shape. Therefore, it is difficult to mix uniformly with conventional mixing means, and with a large difference in specific gravity. Groups of mixed materials that are small in size, materials that have a large size difference, or liquid materials that have a large viscosity difference. Even in the case of a mixture group, etc., a mixture with a uniform and sufficient mixed form can be continuously generated. can.

【0011】[0011]

【実施例】【Example】

以下、実施例に基づいて詳しく説明する。まず、本考案一実施例を示す図1を 参照して、この実施例の連続混合機は、堅形の混合槽3の上方約1/3が中空円 柱形状、下方約2/3が中空逆円錐形状をなして、上下に連なる形状を有し、こ の中空逆円錐形状の部分が主撹拌混合部5、中空円柱形状の部分が補助撹拌混合 部4をなしている。そして、この混合槽3の上端に被混合物の投入口9、該中空 逆円錐の頂点に当る混合槽3の下端が、混合物を連続的に排出する連続排出孔1 0に形成されている。 Hereinafter, a detailed explanation will be given based on examples. First, let us look at Figure 1, which shows one embodiment of the present invention. For reference, in the continuous mixer of this embodiment, about the upper third of the solid mixing tank 3 is a hollow circle. It has a columnar shape, the lower 2/3 of which is hollow and an inverted conical shape, and has a vertically continuous shape. The hollow inverted cone-shaped part is the main stirring and mixing part 5, and the hollow cylindrical part is the auxiliary stirring and mixing part. It forms part 4. At the upper end of this mixing tank 3, there is an inlet 9 for the materials to be mixed, and the hollow The lower end of the mixing tank 3, which corresponds to the apex of the inverted cone, is a continuous discharge hole 1 through which the mixture is continuously discharged. 0.

【0012】 さらに、この混合槽3の内部には、混合槽3の上方から観て、右巻きのスパイ ラル形状の撹拌混合羽根1と、左巻きのスパイラル形状の撹拌混合羽根2が対と して縦方向に装着されると共に、混合槽3の縦中心線を回転中心7とする回転自 在の作動軸6が装着され、この作動軸6に撹拌混合羽根1・2が保持バー11を 介して支承固定されて図示矢印A方向に回転する。0012 Furthermore, inside the mixing tank 3, there is a right-handed spiral when viewed from above the mixing tank 3. A spiral-shaped stirring and mixing blade 1 and a left-handed spiral-shaped stirring and mixing blade 2 are paired. It is installed in the vertical direction and rotates freely with the vertical center line of the mixing tank 3 as the rotation center 7. The current operating shaft 6 is installed, and the stirring and mixing blades 1 and 2 hold the holding bar 11 on this operating shaft 6. It is supported and fixed through the shaft and rotates in the direction of arrow A in the figure.

【0013】 そして、この一対の撹拌混合羽根1・2は、回転中心7と直交する混合槽3の 同一横断面において、図示R12のように異なる巻き径を有すると共に、主撹拌 混合部5においては、主撹拌混合部5の逆円錐形状に追随して、それぞれの巻径 を下端方向に向って漸減するスパイラル形状を呈し、その下端は連続排出孔10 の入口に達している。さらに、この実施例の撹拌混合羽根1・2は、帯板12を 巻回してその幅広面8を回転中心7に臨ませる帯板スパイラルをなし、その幅広 面8は回転中心7と交角θ=1°の上方開きの微傾斜配列になっている。The pair of stirring and mixing blades 1 and 2 have different winding diameters as shown in R 1 R 2 in the same cross section of the mixing tank 3 perpendicular to the rotation center 7, and also have different winding diameters as shown in the figure R 1 R 2 . 5 has a spiral shape in which the diameter of each winding gradually decreases toward the lower end, following the inverted conical shape of the main stirring/mixing section 5, and the lower end reaches the inlet of the continuous discharge hole 10. Further, the stirring and mixing blades 1 and 2 of this embodiment form a spiral strip by winding the strip 12 so that its wide surface 8 faces the rotation center 7, and the wide surface 8 intersects with the rotation center 7 at an angle θ= It has a slightly inclined arrangement with an upward opening of 1°.

【0014】 そして、投入口9から被混合物が投入されると、回転する撹拌混合羽根1・2 によって槽内被混合物が、補助撹拌混合部4と主撹拌混合部5を経由して混合さ れ、下端の排出孔10から混合物を連続的に排出する構造になっている。以上の 連続混合機は、前記の作用を奏して一様均一な混合形態の混合物を連続排出する ことができる。[0014] When the materials to be mixed are introduced from the input port 9, the stirring and mixing blades 1 and 2 rotate. The materials to be mixed in the tank are mixed via the auxiliary stirring and mixing section 4 and the main stirring and mixing section 5. The structure is such that the mixture is continuously discharged from the discharge hole 10 at the lower end. More than A continuous mixer performs the above-mentioned action and continuously discharges a mixture in a uniformly mixed form. be able to.

【0015】 つぎに、図2を参照して本考案第二実施例を説明する。即ち、この実施例は前 記第一実施例と同一の補助撹拌混合部4と主撹拌混合部5を連設した混合槽3内 に、上から観て右巻きの撹拌混合羽根1Aと左巻きの撹拌混合羽根2A、および 、右巻きの撹拌混合羽根1Bと左巻きの撹拌混合羽根2Bからなる二対の撹拌混 合羽根が設けてあり、それ等四個の羽根は、回転中心7と直交する同一横断方向 において、それぞれの巻径が相違すると共に、前記実施例と同一に連続排出孔1 0の入口まで設けてある。この図2実施例は二対の撹拌混合羽根を有するので、 前記の本考案の作用が一段と顕著になる。[0015] Next, a second embodiment of the present invention will be described with reference to FIG. That is, this example Inside the mixing tank 3 in which the auxiliary stirring and mixing section 4 and the main stirring and mixing section 5, which are the same as in the first embodiment, are arranged in series. , a right-handed stirring mixing blade 1A, a left-handed stirring mixing blade 2A, and , two pairs of stirring and mixing blades consisting of a right-handed stirring and mixing blade 1B and a left-handed stirring and mixing blade 2B. Copper blades are provided, and these four blades are arranged in the same transverse direction perpendicular to the rotation center 7. , the respective winding diameters are different, and the continuous discharge hole 1 is the same as in the above embodiment. There are entrances up to 0. Since this embodiment in FIG. 2 has two pairs of stirring and mixing blades, The effect of the present invention described above becomes even more remarkable.

【0016】 なお、本考案の前記の構成において、逆円錐形の混合槽の主撹拌混合部5は不 可欠要件であるが、その主撹拌混合部5の上に連設する補助撹拌混合部4は省略 することができる。[0016] In addition, in the above-described configuration of the present invention, the main agitation mixing section 5 of the inverted conical mixing tank is not included. Although it is an essential requirement, the auxiliary stirring and mixing section 4 that is connected to the main stirring and mixing section 5 is omitted. can do.

【0017】[0017]

【考案の効果】[Effect of the idea]

以上の説明のとおり、本考案の連続混合機は、比重差の大きい被混合物群、ま たはサイズ差の大きい被混合物群、粘度差の大きい被混合物群、等の難混合性の 物質混合、その他一般の固液系物質の混合において、均一にして充分な混合形態 の高品質混合物を提供すると共に、その混合物の供給が連続的にできるので、混 合処理を工程中に要する加工ラインの連続性と整合性が向上し、生産性を向上す る効果がある。 As explained above, the continuous mixer of the present invention is suitable for mixing groups of materials with large differences in specific gravity, or or mixtures that are difficult to mix, such as mixtures with large size differences, mixtures with large viscosity differences, etc. Uniform and sufficient mixing form for mixing substances and other general solid-liquid substances In addition to providing a high-quality mixture of This improves the continuity and consistency of the processing line, which requires processing during the process, and improves productivity. It has the effect of

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

【図1】本考案第一実施例の連続混合機を示す正面断面
[Fig. 1] Front sectional view showing a continuous mixer according to the first embodiment of the present invention

【図2】本考案第二実施例の連続混合機を示す正面断面
[Fig. 2] Front sectional view showing a continuous mixer according to the second embodiment of the present invention

【符号の説明】[Explanation of symbols]

1 右巻き撹拌混合羽根 2 左巻き撹拌混合羽根 3 混合槽 4 補助撹拌混合部 5 主撹拌混合部 6 作動軸 7 回転中心 8 幅広面 9 投入口 11 連続排出孔 12 帯板 1 Right-handed stirring mixing blade 2 Left-handed stirring mixing blade 3 Mixing tank 4 Auxiliary stirring mixing section 5 Main stirring and mixing section 6 Operating axis 7 Center of rotation 8 Wide side 9 Inlet 11 Continuous discharge hole 12 Band plate

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 堅形混合槽の全体または少くとも下半部
分を、中空逆円錐状の撹拌混合部になすと共に、該撹拌
混合部の上方に被混合物投入部、該撹拌混合部の下端を
混合物の連続排出孔になし、さらに、該撹拌混合部内
に、帯板で形成されて巻き方向と巻き径を異にすると共
に、それぞれが該連続排出孔の方向に巻き径を漸減し、
かつ、同一方向に回転する少くとも一対の撹拌混合羽根
を設け、さらに、該撹拌混合羽根は、該帯板の幅広面を
該撹拌混合羽根の回転中心に臨ませ、該回転中心に対し
て該幅広面を平行配列、または微傾斜配列になした構造
を特徴とする連続混合機。
Claim 1: The entire or at least the lower half of the vertical mixing tank is formed into a hollow inverted cone-shaped stirring and mixing section, and above the stirring and mixing section there is a material inputting section, and the lower end of the stirring and mixing section is provided. There is no continuous discharge hole for the mixture, and further, a band plate is formed in the stirring mixing part to have a different winding direction and a different winding diameter, and each of the strips has a winding diameter that gradually decreases in the direction of the continuous discharge hole,
and at least a pair of stirring and mixing blades that rotate in the same direction are provided, and further, the stirring and mixing blades have a wide side of the strip facing the rotation center of the stirring and mixing blade, and the stirring and mixing blades are arranged so as to face the rotation center of the stirring and mixing blade. A continuous mixer characterized by a structure in which wide surfaces are arranged in parallel or slightly inclined.
JP2575091U 1991-03-25 1991-03-25 continuous mixer Pending JPH04114427U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2575091U JPH04114427U (en) 1991-03-25 1991-03-25 continuous mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2575091U JPH04114427U (en) 1991-03-25 1991-03-25 continuous mixer

Publications (1)

Publication Number Publication Date
JPH04114427U true JPH04114427U (en) 1992-10-08

Family

ID=31910418

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2575091U Pending JPH04114427U (en) 1991-03-25 1991-03-25 continuous mixer

Country Status (1)

Country Link
JP (1) JPH04114427U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010077705A (en) * 2000-02-08 2001-08-20 윤종용 Method and Apparatus for Preparing Styrene-based Polymer
JP2015077563A (en) * 2013-10-17 2015-04-23 プライミクス株式会社 Agitation blade and agitator
JP2019181458A (en) * 2018-04-04 2019-10-24 クレヴァー−カット・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Stirring device
KR20220007345A (en) * 2020-07-10 2022-01-18 한국해양과학기술원 sea sand cleaning device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010077705A (en) * 2000-02-08 2001-08-20 윤종용 Method and Apparatus for Preparing Styrene-based Polymer
JP2015077563A (en) * 2013-10-17 2015-04-23 プライミクス株式会社 Agitation blade and agitator
JP2019181458A (en) * 2018-04-04 2019-10-24 クレヴァー−カット・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Stirring device
KR20220007345A (en) * 2020-07-10 2022-01-18 한국해양과학기술원 sea sand cleaning device

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