JPH0323301Y2 - - Google Patents
Info
- Publication number
- JPH0323301Y2 JPH0323301Y2 JP1982087132U JP8713282U JPH0323301Y2 JP H0323301 Y2 JPH0323301 Y2 JP H0323301Y2 JP 1982087132 U JP1982087132 U JP 1982087132U JP 8713282 U JP8713282 U JP 8713282U JP H0323301 Y2 JPH0323301 Y2 JP H0323301Y2
- Authority
- JP
- Japan
- Prior art keywords
- rotation
- wall
- axis
- gear
- shaft
- 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.)
- Expired
Links
- 239000004570 mortar (masonry) Substances 0.000 claims description 14
- 238000003756 stirring Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 230000029058 respiratory gaseous exchange Effects 0.000 description 4
- 239000004568 cement Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
Landscapes
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Description
本考案は、自転する撹拌羽根を備えた自転軸と
公転する撹拌羽根を備える公転軸とを有するパン
型モルタルミキサにおける両軸の回転比を特定す
る提案に関するものである。従来のパン型ミキサ
を用いてモルタル練りを実施した場合、コンクリ
ート練りと同じ条件の自転軸及び公転軸の回転数
では均一で良質なモルタルを得ることは到底困難
であり、仮に各回転軸の回転数をさらに増加させ
るとか或は混練時間をさらに延長するなどして
も、コンクリート練りに比べ単位容量当りのセメ
ント容量が多いこと及び粗骨材が無いことなどの
相異点もあつて、ダマと称するセメントの固まり
が発生するなどの撹拌不良が生じていたのであ
る。
そこで本考案は、自転軸の回転数を従来ミキサ
のものよりも増加させると共に、自転軸と公転軸
との各回転数の比である自転公転比に着目してこ
れを鋭意研究試験し、その自転回転数を公転回転
数の4.5〜7倍の範囲の自転公転比に形成するこ
とによつて、均一・良質なモルタルをも短時間で
練り混ぜることを可能になしたものである。
ここに公転回転数とは公転軸の回転数であり、
また自転回転数とは自転軸の回転数である。両者
の回転比は各軸の回転方向が同じか、或は反対か
によつて次式で表わされる。
自転軸と公転軸の回転方向が同じである場合
自転回転数=(i+1)n
自転軸と公転軸の回転方向が反対である場合
自転回転数=(i−1)n
ここで
i……変速機構で定まる絶対回転比
n……公転回転数
上記した本考案の実施例を添付図面によつて詳
細に説明すると、第1図、第2図、第3図は具体
的な装置の構成であつて、底をもつ容器1は、外
側壁2と内側壁3とで形成される環状のパン型で
あり、内側壁3の中心部には駆動源に連結された
公転軸4が回転自在に設けられている。公転軸4
の上方端部にはこれと一体構造になす中空の水平
箱状支持部材5が設けられ、この支持部材5の内
部には、内側壁3の上部に固定され、且つ公転軸
4と同心の固定歯車6、これに噛み合う下側中間
歯車7、この下側中間歯車7に固定され同じ方向
へ回転をする上側中間歯車8、及びこの上側中間
歯車8に噛み合う遊星歯車9が収納され、これら
の歯車7,8及び9の中間軸10及び自転軸11
はこの支持部材5の水平面に対し垂直状態で支持
されている。
遊星歯車9の自転軸11は、図示のとおり外側
壁2と内側壁3の中間位置に配設されていると共
に、その下方端部には平板状の自転羽根12が軸
対象位置に2個固着されている。
他方、複数の平板状の公転羽根13は、支持部
材5の適所に腕を介して取付けられている。
ここで自転公転比を変更するためには、下側中
間歯車7及び上側中間歯車8の歯数を変更すれば
よい。しかるに水平箱状支持部材5には、中間軸
10の軸間距離が変わつても中間軸の支持を可能
にするため、複数の孔14,15が明けられてい
る。図において矢印16は自転軸の回転方向、矢
印17は公転軸の回転方向を示している。
自転羽根形状の他の実施例としては、第2図示
のような材料を下方に押えつける作用効果のある
自転羽根18及び第3図示のような自転羽根12
の巾に比べて半分の巾にした自転羽根19があ
る。
本実施例におけるミキサの自転軸と公転軸の回
転比は次式で表わされる。
回転比=〔自転軸回転数/公転軸回転数〕=(i−1
)
=〔固定歯車6の歯数/下側中間歯車7の歯数
×上側中間歯車8の歯数/遊星歯車9の歯数〕−1
次に、本実施例構造のミキサを用いて自転軸と
公転軸との最適回転比を解明するに、表3は公転
軸の回転数を一定(50r.p.m)にし、自転軸の回
転数即ち自転公転比を変更し実施した試験の結果
表である。表1はこの試験に使用した材料の種
類、表2はこの試験に使用した材料の配合であ
る。
なお、用いたパン型ミキサは、外側壁2の内径
948mm、内側壁3の外径216mm、公転軸と自転軸の
軸間距離300mm、公転軸の回転数は従来ミキサと
同じの50r.p.mであり、練り混ぜするモルタルの
容量はBatch0.05m3である。
表3におけるブリージング率の比とは、
JIS A 1123によつて試験し、且つ自転羽根1
2を用い回転比が6.1であるときを100として表わ
す。
この数値は小さい方が良質なモルタルである。
表3における圧縮強度の比とは、
JIS A 1132及びJIS A 1108によつて試験
し、その供試体は材令28日における圧縮強度で且
つ自転羽根12を用い回転比が6.1であるときを
100として表わす。この数値は大きい方が良質な
モルタルである。
表3において、
回転比が4以下の場合は、自転羽根の撹拌効果
が少なく、ブリージング率、圧縮強度共に悪くな
り、さらにダマの発生もみられた。
また回転比が7.5以上になると、自転羽根によ
る混練物の飛散が激しくなり、混練物が分離する
という傾向がみられた。
後者7.5以上の場合において、別な試験即ち混
練物の飛散を防止する目的のために巾の小さな自
転羽根19を使用してみたところ、飛散は防止で
きたが自転羽根の撹拌効果は期待程得られなかつ
た。さらに表3には記載していないが、公転軸の
回転数のみを低くし同じ自転羽根12を用いてみ
たところ、目的の飛散は防止できたが公転羽根の
撹拌効果が減少し良いモルタルが得られなかつ
た。どちらの試験においても期待する程の成果が
得られなかつた。
以上の試験から明らかなとおり、自転する自転
羽根を備える自転軸と公転する公転羽根を備える
公転軸とを併せもつパン型モルタルミキサは、両
軸における自転公転比が4〜7.5の範囲で使用す
ることが自転羽根及び公転羽根の撹拌効果を有効
に生かせ得るのであり、均一・良質の練り上りを
得るには、撹拌効果が最大限に生かせる5〜7の
範囲で使用することが好ましい事実を究明した。
よつて本考案ミキサは、従来のパン型ミキサと
同じ公転軸の回転数であつても自転軸の回転数が
増加していることから圧縮強度及びブリージング
The present invention relates to a proposal for specifying the rotation ratio of both shafts in a pan-type mortar mixer that has an autorotation shaft equipped with a rotating stirring blade and a revolving shaft equipped with a revolving stirring blade. When mixing mortar using a conventional pan-type mixer, it is extremely difficult to obtain uniform and high-quality mortar under the same conditions of rotation of the rotation axis and revolution axis as for concrete mixing. Even if the number of cements is further increased or the mixing time is further extended, there are differences such as the fact that the cement capacity per unit volume is larger than that of concrete mixing and there is no coarse aggregate, so it will not cause lumps. This resulted in poor mixing, such as the formation of cement lumps. Therefore, in this invention, we increased the rotational speed of the rotational axis compared to that of conventional mixers, and focused on the rotational revolution ratio, which is the ratio of the rotational speed of the rotational axis and the revolutional axis, and conducted intensive research and tests to improve this. By setting the rotation speed to a rotation/revolution ratio in the range of 4.5 to 7 times the revolution speed, it is possible to mix uniform and high quality mortar in a short time. Here, the revolution speed is the revolution speed of the revolution axis,
Furthermore, the rotation speed is the rotation speed of the rotation axis. The rotation ratio between the two is expressed by the following equation depending on whether the rotation direction of each axis is the same or opposite. When the direction of rotation of the rotation axis and the revolution axis is the same: Rotation speed = (i + 1) n When the rotation direction of the rotation axis and the revolution axis is opposite: rotation speed = (i - 1) n Here, i...speed change Absolute rotation ratio determined by the mechanism n...Revolutionary rotation speed The embodiment of the present invention described above will be explained in detail with reference to the attached drawings. The container 1 with a bottom is an annular bread-shaped container formed by an outer wall 2 and an inner wall 3, and a revolution shaft 4 connected to a drive source is rotatably provided at the center of the inner wall 3. It is being Revolution axis 4
A hollow horizontal box-shaped support member 5 is provided at the upper end of the support member 5 and is integrally formed with the support member 5. A gear 6, a lower intermediate gear 7 that meshes with the gear 6, an upper intermediate gear 8 that is fixed to the lower intermediate gear 7 and rotates in the same direction, and a planetary gear 9 that meshes with the upper intermediate gear 8 are housed. Intermediate shaft 10 and rotational shaft 11 of 7, 8 and 9
is supported perpendicularly to the horizontal surface of the support member 5. As shown in the figure, the rotation axis 11 of the planetary gear 9 is arranged at an intermediate position between the outer wall 2 and the inner wall 3, and two flat plate-shaped rotation blades 12 are fixed to the lower end thereof at symmetrical positions. has been done. On the other hand, the plurality of flat plate-shaped revolving blades 13 are attached to appropriate positions on the support member 5 via arms. In order to change the rotation/revolution ratio here, the number of teeth of the lower intermediate gear 7 and the upper intermediate gear 8 may be changed. However, the horizontal box-shaped support member 5 is provided with a plurality of holes 14 and 15 in order to enable support of the intermediate shaft even if the distance between the intermediate shafts 10 changes. In the figure, arrow 16 indicates the rotation direction of the rotation axis, and arrow 17 indicates the rotation direction of the revolution axis. Other examples of the rotating blade shape include a rotating blade 18 as shown in the second figure which has the effect of pressing down the material downward, and a rotating blade 12 as shown in the third figure.
There is a rotating blade 19 whose width is half that of the width of the blade. The rotation ratio between the rotation axis and the revolution axis of the mixer in this embodiment is expressed by the following equation. Rotation ratio = [Rotation axis rotation speed / Revolution axis rotation speed] = (i-1
)=[Number of teeth of fixed gear 6/Number of teeth of lower intermediate gear 7×Number of teeth of upper intermediate gear 8/Number of teeth of planetary gear 9]-1 Next, using the mixer having the structure of this embodiment, In order to find out the optimal rotation ratio between the rotation axis and the revolution axis, Table 3 shows the results of tests conducted by keeping the rotation speed of the revolution axis constant (50 rpm) and changing the rotation speed of the rotation axis, that is, the rotation-revolution ratio. . Table 1 shows the types of materials used in this test, and Table 2 shows the formulations of the materials used in this test. In addition, the bread-type mixer used has an inner diameter of the outer wall 2.
948mm, the outer diameter of the inner wall 3 is 216mm, the distance between the revolution axis and the rotation axis is 300mm, the rotation speed of the revolution axis is 50r.pm, which is the same as the conventional mixer, and the capacity of the mortar to be mixed is Batch 0.05m3 . be. The ratio of breathing rate in Table 3 is the ratio of the breathing rate tested according to JIS A 1123 and
When the rotation ratio is 6.1, it is expressed as 100. The smaller this value is, the better the quality of the mortar. The ratio of compressive strength in Table 3 refers to the compressive strength when tested according to JIS A 1132 and JIS A 1108, when the specimen has a compressive strength at 28 days old, and when the rotating blade 12 is used and the rotation ratio is 6.1.
Expressed as 100. The larger this value is, the better the quality of the mortar. In Table 3, when the rotation ratio was 4 or less, the stirring effect of the rotating blade was small, the breathing rate and compressive strength were both poor, and furthermore, the occurrence of lumps was observed. Furthermore, when the rotation ratio was 7.5 or more, the kneaded material was scattered more violently by the rotating blades, and there was a tendency for the kneaded material to separate. In the latter case of 7.5 or more, we tried using a rotating blade 19 with a small width for the purpose of another test, that is, to prevent the mixed material from scattering, and although the scattering could be prevented, the stirring effect of the rotating blade was not as expected. I couldn't help it. Furthermore, although it is not listed in Table 3, when we tried using the same rotating blades 12 by lowering only the rotational speed of the revolving shaft, we were able to prevent the desired scattering, but the stirring effect of the revolving blades decreased and a good mortar could not be obtained. I couldn't help it. Neither test yielded the expected results. As is clear from the above tests, a pan-type mortar mixer that has both an autorotation shaft with rotating blades that rotates on its own axis and a revolution shaft with revolving blades that revolves around its axis is used when the rotation-revolution ratio of both axes is in the range of 4 to 7.5. We investigated the fact that the stirring effect of the rotating blades and revolving blades can be effectively utilized, and in order to obtain a uniform and high-quality dough, it is preferable to use the stirring effect in the range of 5 to 7 to maximize the stirring effect. did. Therefore, even though the mixer of the present invention has the same rotational speed of the revolving shaft as the conventional pan-type mixer, the rotational speed of the rotating shaft is increased, so the compressive strength and breathing are improved.
【表】【table】
【表】【table】
第1図は一部の切断面を図示した斜視図、第2
図、第3図は自転羽根の他の例を示す斜視図であ
る。
1……容器、2……外側壁、3……内側壁、4
……公転軸、5……支持部材、{7……下側中間
歯車、8……上側中間歯車}中間歯車、10……
中間軸、11……自転軸、12,18,19……
自転羽根、13……公転羽根。
Fig. 1 is a perspective view showing a part of the cut surface, Fig. 2
3 are perspective views showing other examples of rotating blades. 1... Container, 2... Outer wall, 3... Inner wall, 4
...Revolution axis, 5... Support member, {7... Lower intermediate gear, 8... Upper intermediate gear} Intermediate gear, 10...
Intermediate axis, 11... Rotation axis, 12, 18, 19...
Rotating blade, 13...revolving blade.
Claims (1)
状の容器と、前記内側壁の中心を貫通する公転
軸と、該公転軸の上方端部に設けた支持部材
と、該支持部材の外方端部に備えた自転軸と、
該自転軸の下方端部に設けた自転羽根と、前記
支持部材に付設した公転羽根とからなるミキサ
が、次の構造に形成されていることを特徴とす
るパン型モルタルミキサ (ア) 前記自転軸11が、容器1の外側壁2の内
面及び内側壁3の外面に対し並行になして設
けられていること、 (イ) 前記公転軸4と自転軸11の各回転数が、
公転軸4の4.5〜7倍の自転軸回転数範囲で
ある自転公転比になされていること。 (2) 前記自転公転比が、内側壁3の上部に固定さ
れた固定歯車6と、自転軸11に固定された遊
星歯車9と、固定歯車6及び遊星歯車9の中間
部位に設けた歯車軸10に固定された中間歯車
とから形成された遊星歯車機構によつて得られ
ることを特徴とする実用新案登録請求の範囲第
1項記載のパン型モルタルミキサ。 (3) 前記中間歯車が、下側中間歯車7と上側中間
歯車8とから形成されていることを特徴とする
実用新案登録請求の範囲第2項記載のパン型モ
ルタルミキサ。 (4) 前記自転軸11が、容器1の外側壁2の内面
と内側壁3の外面の中間部位に配設されている
ことを特徴とする実用新案登録請求の範囲第1
項記載のパン型モルタルミキサ。 (5) 前記自転軸11が2軸設けられ且つ各軸に2
個の自転羽根12が軸対象位置に夫々設けられ
ていることを特徴とする実用新案登録請求の範
囲第1項記載のパン型モルタルミキサ。[Claims for Utility Model Registration] (1) An inner wall, a bottomed cylindrical container with the inner wall in the center, a revolving axis passing through the center of the inner wall, and an upper end of the revolving axis a support member provided at the support member; a rotation axis provided at the outer end of the support member;
A pan-type mortar mixer characterized in that a mixer comprising a rotating blade provided at the lower end of the rotating shaft and a revolving blade attached to the supporting member is formed in the following structure. The shaft 11 is provided parallel to the inner surface of the outer wall 2 and the outer surface of the inner wall 3 of the container 1; (a) the rotational speeds of the revolution shaft 4 and the rotation shaft 11 are
The rotation-revolution ratio is within the rotational speed range of 4.5 to 7 times that of the revolution axis 4. (2) The rotation/revolution ratio is the fixed gear 6 fixed to the upper part of the inner wall 3, the planetary gear 9 fixed to the rotation shaft 11, and the gear shaft provided at an intermediate location between the fixed gear 6 and the planetary gear 9. A pan-type mortar mixer according to claim 1, characterized in that it is obtained by a planetary gear mechanism formed by an intermediate gear fixed to a base plate. (3) The pan-type mortar mixer according to claim 2, wherein the intermediate gear is formed of a lower intermediate gear 7 and an upper intermediate gear 8. (4) Utility model registration claim 1, characterized in that the rotation axis 11 is disposed at an intermediate location between the inner surface of the outer wall 2 and the outer surface of the inner wall 3 of the container 1.
Pan type mortar mixer as described in Section 1. (5) Two rotation axes 11 are provided, and each axis has two rotation axes.
A pan-type mortar mixer according to claim 1, wherein the rotating blades 12 are provided at axially symmetrical positions.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982087132U JPS58190114U (en) | 1982-06-10 | 1982-06-10 | Rotation/revolution ratio of stirring blade for mortar mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982087132U JPS58190114U (en) | 1982-06-10 | 1982-06-10 | Rotation/revolution ratio of stirring blade for mortar mixer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58190114U JPS58190114U (en) | 1983-12-17 |
JPH0323301Y2 true JPH0323301Y2 (en) | 1991-05-21 |
Family
ID=30095870
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1982087132U Granted JPS58190114U (en) | 1982-06-10 | 1982-06-10 | Rotation/revolution ratio of stirring blade for mortar mixer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58190114U (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61147826A (en) * | 1984-12-20 | 1986-07-05 | Mitsubishi Alum Co Ltd | Apparatus for producing alloy |
JPH059066Y2 (en) * | 1988-08-15 | 1993-03-05 | ||
JP2010131214A (en) * | 2008-12-05 | 2010-06-17 | Emura Tekkosho:Kk | Fermented soybeans stirrer |
IT1401799B1 (en) * | 2010-09-29 | 2013-08-28 | Firex S R L | MACHINE FOR MIXING OR CUTTING, PARTICULARLY FOR THE PROCESSING OF FOOD, AGENT WITH PLANETARY MOVEMENT SHAFT |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56151515A (en) * | 1980-04-08 | 1981-11-24 | Jii Buarubetsuku Suben | Mixer |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5817623Y2 (en) * | 1979-07-23 | 1983-04-09 | 中部工業株式会社 | Forced kneading mixer |
-
1982
- 1982-06-10 JP JP1982087132U patent/JPS58190114U/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56151515A (en) * | 1980-04-08 | 1981-11-24 | Jii Buarubetsuku Suben | Mixer |
Also Published As
Publication number | Publication date |
---|---|
JPS58190114U (en) | 1983-12-17 |
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