CN1069223C - Horizontal stirring machine - Google Patents
Horizontal stirring machine Download PDFInfo
- Publication number
- CN1069223C CN1069223C CN94105009A CN94105009A CN1069223C CN 1069223 C CN1069223 C CN 1069223C CN 94105009 A CN94105009 A CN 94105009A CN 94105009 A CN94105009 A CN 94105009A CN 1069223 C CN1069223 C CN 1069223C
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- CN
- China
- Prior art keywords
- shaft
- stirrer paddle
- inclined plane
- triangular shape
- shape stirrer
- 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 - Fee Related
Links
- 238000003756 stirring Methods 0.000 title claims description 13
- 239000000463 material Substances 0.000 claims description 36
- 238000001035 drying Methods 0.000 claims description 9
- 230000002093 peripheral effect Effects 0.000 claims 1
- 238000013019 agitation Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 15
- 230000014509 gene expression Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention provide a horizontal agitator which agitates the the contents of blender uniformly and shortens the time required for discharge. An agitating shaft is provided rotatably at the part of the axis of a vessel 1 set horizontally, and rectangular flat-plate-shaped agitating vanes having slants and triangular agitating vanes having slants opposite to the ones of the agitating vanes and also having surfaces parallel to the agitating shaft are fitted to the agitating shaft, at positions at which they are concentric with the agitating shaft and symmetric with respect to it and alternately along the direction of the axis of the agitating shaft. Agitation is executed by rotating the agitating shaft in one direction, while the contents are discharged by rotating the shaft in the opposite direction.
Description
The present invention relates to a kind of handle and be contained in the mixer that the material in the horizontal vessel stirs, for example the sort of raw material that graininess, mud shape, body of powder etc. are wet stirs and makes used horizontal mixer on its dry drying machine.
In the past, above-mentioned this horizontal mixer can be arranged on shaft 2A on the axis part of cylindrical container 1A of horizontally set freely to rotate.Have as shown in Figure 7 for being contained in material in the container and send to a direction be fixed tightly in spiral helicine blade 3A on the shaft 2A with being integral, perhaps as shown in Figure 8, for material is sent to mutual stirrer paddle 3B in the opposite direction to the central part of shaft 2A, 3C is fixed tightly on the shaft 2A with being integral, also have as illustrated in fig. 9 and the stirrer paddle 3D with inclined plane that sends to a direction is arranged on the shaft 2A by hold-down arm 5A, a side or central part at above-mentioned cylindrical container 1A are provided with outlet 4A, carry out positive and negative revolution repeatedly and only carry out rotating various situation constantly to a direction.
But, mixer before above-mentioned is owing to be arranged on the feeding direction of the blade 3A～3C on the shaft 2A all towards a side or central part, therefore in use, when making above-mentioned shaft 2A only towards a direction revolution, material in the container can be forced on certain side plate 18 on one side, perhaps can focus on central part with being biased, thereby produce the problem that load is increased.
So, just make shaft 2A carry out positive and negative rotating measure at regular intervals repeatedly in order to solve the above problems, but in this case, act on the shaft 2A at the starting load that turns to conversion the time to have impact that carries out shaft 2A, for this reason, the just necessary intensity that improves shaft and bearing etc. perhaps increases power itself, and produces the problem that needs further to improve the intensity of above-mentioned member thus.In addition, to spend the disadvantage that more time is come material in the amount discharge container in addition.
The former mixer of Fig. 7,8,9 expressions is used in the drying machine, when thermophore being fed in the valve jacket that is installed on the container, the example that adheres to the material in the container on the internal face is quite a lot of, producing under this situation of adhering to, owing to reasons such as friction certainly will form excessive load, therefore when the positive and negative revolution of carrying out shaft is changed, big starting load effect is not only arranged but also require to increase power, making running become impossible problem in addition.
When the mixer before making continues revolution towards a direction, be contained in material in the mixer owing to the inclination of stirrer paddle is sent to, have the part biasing, thereby can not use heat transfer area effectively, and, can not carry out fully owing to stir, thereby drying time is just long, the degree of drying that material often takes place is inhomogeneous, is especially doing under the such mobile less solid situation of wet cake, and this phenomenon reflects more significantly.
The present invention is for solving above-mentioned making along with stirring the variety of problems that is produced, and purpose provides a kind of material that can stir equably in the container that is contained in horizontally set, and can make the horizontal mixer of the efflux time shortening of material.
To achieve the above object, horizontal mixer of the present invention can be arranged on shaft on the axis part of container of horizontally set freely to rotate; On the concentric symmetric position of this shaft, relative this shaft had the rectangular flat shape stirrer paddle on inclined plane and the triangular shape stirrer paddle that has the inclined plane opposite with this tabular stirrer paddle direction and have a parallel surface that parallels with above-mentioned shaft is installed on the above-mentioned shaft.
In addition, horizontal mixer of the present invention provides on a kind of axis part of the container that can be arranged on shaft freely to rotate horizontally set; The triangular shape stirrer paddle that relative this shaft is had the rectangular flat shape stirrer paddle on inclined plane and have the inclined plane opposite with this tabular stirrer paddle direction and have a parallel surface that parallels with above-mentioned shaft alternately is installed on the above-mentioned shaft along the axis direction of shaft.
In addition, the feature of horizontal mixer of the present invention is the inside that also thermal source is fed to the hold-down arm of the stirrer paddle of above-mentioned shaft, triangular shape stirrer paddle and rectangular flat shape and triangular shape stirrer paddle.
With above-mentioned structure, the revolution of shaft on making the cylindrical container that is arranged on horizontally set is so that when making the inclined plane of triangular shape stirrer paddle act on the material, because the inclined plane of this inclined plane and rectangular flat shape stirrer paddle is mutually towards opposite feeding direction effect, therefore the sending to of material that is contained in the mixer is cancelled, this material (spacing) on roughly the same circular arc is rocked from side to side, thereby can stir.And when making shaft and above-mentioned revolution on the contrary so that making the parallel surface of triangular shape stirrer paddle act on the material, because with this plane feed material on the longitudinally to the left and right, therefore the effect of having only the inclined plane of tabular stirrer paddle to export in one direction can discharge the material that is contained in the mixer.
Again since the material that is contained in the mixer between adjacent rectangular flat shape stirrer paddle and triangular shape stirrer paddle, reciprocatingly stirred, thereby can make the load that acts on the shaft this shaft axially on uniformity.
In addition, because thermal source is fed to the inside of the hold-down arm of shaft, triangular shape stirrer paddle and rectangular flat shape stirrer paddle and triangular shape stirrer paddle, the particularly inside of triangular shape stirrer paddle, therefore can be used the heat transfer area of these members as drying operation etc.
Fig. 1 is the front elevation that is fit to use horizontal mixer of the present invention,
Fig. 2 is the right hand view of mixer shown in Figure 1,
Fig. 3 is the partial enlarged drawing of mixer shown in Figure 1,
Fig. 4 is the expanded view of the installation site of expression stirrer paddle shown in Figure 1,
The schematic diagram of the effect when Fig. 5 is the explanation stirring,
The schematic diagram of the effect when Fig. 6 is the explanation discharge,
Fig. 7 is the front elevation of former horizontal mixer,
Fig. 8 is the front elevation of former horizontal mixer,
Fig. 9 is the front elevation of former horizontal mixer.
Below, explain embodiments of the invention with reference to accompanying drawing.
Fig. 1 is the front elevation that is fit to use horizontal mixer of the present invention, Fig. 2 is the right hand view of expression mixer shown in Figure 1, among the figure, the 1st, the cylindrical vessel of horizontally set, 2 are arranged on the shaft of the axis part of this cylindrical vessel 1, its two ends 2a, 2a is bearing in above the cylindrical vessel 1 etc., is connected with the motor that does not have expression among the figure and carries out positive and negative revolution.
Fig. 3 is the partial enlarged drawing of mixer shown in Figure 1, and 3 among the figure is stirrer paddles that above-mentioned relatively shaft 2 has the rectangular flat shape of inclined plane 3a; The 4th, have and inclined plane 4a that direction opposite identical and have the stirrer paddle of the triangular shape of the parallel surface 4b that parallels with above-mentioned shaft 2 with stirrer paddle 3 shapes.The stirrer paddle 3 of above-mentioned rectangular flat shape and the stirrer paddle 4 of triangular shape on the concentric symmetric position of above-mentioned shaft 2, are installed in respectively on the shaft 2 by hold-down arm 5,6 as illustrated in fig. 3.Present embodiment is represented the inclination situation that inclined plane 3a, 4a are roughly at 45 with respect to shaft 2.
Fig. 5 is the schematic diagram of above-mentioned tabular stirrer paddle 3 of explanation and the effect of triangular shape stirrer paddle 4 when stirring.As shown in Figure 3, when making drying machine 2, the material that is contained in the mixer is sent to the right direction a shown in this figure with to gyratory directions b by the effect of tabular stirrer paddle 3 to directions X, promptly towards b direction shown in Figure 5 revolution.And make the material that is contained in the mixer when gyratory directions b sends to by the effect of the inclined plane 4a of triangular shape stirrer paddle 4, it is sent to towards the left direction c opposite with above-mentioned a direction.Like this, owing to above-mentioned material moves back and forth between tabular stirrer paddle 3 and triangular shape stirrer paddle 4, thereby can stir fully.And, even only do unidirectional lasting revolution, because above-mentioned material concentration of local, not relatively not on one side not, thereby get quite evenly in the whole mixer with regard to filling, just can carry out fully and stirring uniformly, can obtain the good heat transfer effect.
Fig. 6 is the schematic diagram of above-mentioned tabular stirrer paddle 3 of explanation and the effect of triangular shape stirrer paddle 4 when discharging.When making shaft 2 as illustrated in fig. 3 to the y direction, during promptly towards d direction shown in Figure 6 revolution, the material that is contained in the mixer is sent to towards the gyratory directions d of shaft.And, owing to above-mentioned material is sent to towards gyratory directions d and left direction c as shown in the drawingly, therefore outlet is set in the left side of above-mentioned stirrer paddle 3 and 4 just can discharges above-mentioned material by the effect of tabular stirrer paddle 3.
As mentioned above, on shaft 2, when the triangular shape stirrer paddle 4 that relative shaft 2 is had the rectangular flat shape stirrer paddle 3 of inclined plane 3a and have and inclined plane 4a that direction opposite identical shaped with stirrer paddle 3 and have a parallel surface 4b that parallels with shaft 2 is installed on the concentric symmetric position of shaft 2, just make the material that is contained in the mixer be subjected to the effect of the inclined plane 4a of triangular shape stirrer paddle 4, thereby by shaft 2 revolutions just can be stirred uniformly to all materials.In addition, also make material be subjected to the effect of the parallel surface 4b of triangular shape stirrer paddle 4, when making shaft 2 revolutions, just material can be discharged.
Fig. 4 is the expanded view that is illustrated in the installation site of using the stirrer paddle in the horizontal mixer of the present invention shown in Figure 1, be relative shaft 2 have inclined plane 3a the rectangular flat shape stirrer paddle 3 with have but inclined plane 4a that direction opposite identical and have the triangular shape stirrer paddle 4 of the parallel surface 4b that parallels with shaft 2 with stirrer paddle 3 shapes, alternately be installed on the above-mentioned shaft 2 along the axis direction of shaft.But the parallel surface 4b of the stirrer paddle 4 of above-mentioned triangular shape is provided with along a direction.
As shown in Figure 4, be installed on the shaft 2 to above-mentioned tabular stirrer paddle 3 and triangular shape stirrer paddle 4 conversion phase places, shown in Figure 4 is expression is provided with these stirrer paddles 3,4 by 90 degree spacings example, but its installing space is arbitrarily.
By like that tabular stirrer paddle 3 and triangular shape stirrer paddle 4 being installed on the shaft 2 as mentioned above, and shaft 2 is turned round towards the arrow directions X, because the material that is contained in the mixer moves back and forth between adjacent stirrer paddle 3 or 4, thereby is stirred well.On the contrary, when making shaft 2 when arrow Y direction is turned round,, thereby just can promptly discharge material from outlet because material sent to as mentioned above like that toward the direction.
As mentioned above, on the axis part of the container of horizontal mixer of the present invention by being arranged on shaft freely to rotate horizontally set, on the concentric symmetric position of this shaft, the rectangular flat shape stirrer paddle that relative shaft is had the inclined plane, be installed on the above-mentioned shaft with the triangular shape stirrer paddle that has but inclined plane that direction is opposite identical and have a parallel surface that parallels with shaft with tabular stirrer paddle shape, therefore, even shaft is turned round continuously towards a direction, the material that is contained in the mixer can not be biased on certain position yet, can the material uniformity be filled on the longitudinally of shaft, stir uniformly, and make under the rotating in the opposite direction situation of shaft, can force ground and in the short time, material is sent to and discharged to a certain direction, the shortcoming of this class mixer before having overcome thus and reach intended purposes of the present invention.In addition, when carrying out drying with thermophore since can be not dry inhomogeneous and can use heat transfer area effectively, thereby just can carry out drying effectively.
And, because thermophore is fed this mixer inside as heat transfer area, this compares with only installing body heating valve jacket, and its heat transfer area increases more than 30%, owing to the effect common with the above-mentioned efficient that mixing effect improved arranged, just more helps the shortening of drying time.
Claims (2)
1. horizontal mixer, comprise the axis part of the cylindrical vessel central shaft that is arranged on horizontally set and be arranged on the shaft of this axis part freely to rotate, with the face of axial line quadrature on concentric symmetric position on, by with the face direction of the axial line quadrature of described axis part on extend the hold-down arm that is provided with to both sides from the outer peripheral face of shaft, described relatively shaft has the rectangular flat shape stirrer paddle on inclined plane and the triangular shape stirrer paddle that has the inclined plane opposite with this stirrer paddle direction and have a parallel surface that parallels with described shaft is arranged on the free end of this hold-down arm, thermal source is provided to described shaft, the inside of the hold-down arm of triangular shape stirrer paddle and rectangular flat shape stirrer paddle and triangular shape stirrer paddle, described shaft is in the continuously revolution and stir content material and carry out drying of a direction, and shaft turns round round about and discharges content material.
2. horizontal mixer as claimed in claim 1, it is characterized in that described relatively shaft has the rectangular flat shape stirrer paddle on inclined plane and the triangular shape stirrer paddle that has the inclined plane opposite with this stirrer paddle direction and have a parallel surface that parallels with described shaft alternately is installed in from the axle center of described axis part along axis direction extends both end positions on the plane of set a distance on radial direction.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3082294A JPH07218139A (en) | 1994-02-03 | 1994-02-03 | Horizontal agitator |
| JP30822/1994 | 1994-02-03 | ||
| JP30822/94 | 1994-02-03 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1118715A CN1118715A (en) | 1996-03-20 |
| CN1069223C true CN1069223C (en) | 2001-08-08 |
Family
ID=12314405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN94105009A Expired - Fee Related CN1069223C (en) | 1994-02-03 | 1994-05-10 | Horizontal stirring machine |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPH07218139A (en) |
| CN (1) | CN1069223C (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10169936A (en) * | 1996-12-05 | 1998-06-26 | Hitachi Chem Co Ltd | Waste carbonization processor |
| JP2002286366A (en) * | 2001-03-26 | 2002-10-03 | Tsukasa Kogyo Kk | Powder and grain drying device |
| KR100880094B1 (en) * | 2007-04-11 | 2009-01-23 | 현대건설주식회사 | A Dry system transfer screw |
| CN101837258A (en) * | 2009-03-18 | 2010-09-22 | 上海亦晨信息科技发展有限公司 | Mixing and impelling type horizontal premixing device and method thereof |
| JP5922385B2 (en) * | 2011-12-01 | 2016-05-24 | 株式会社村上製作所 | Stirring shaft and stirrer using the same stirring shaft |
| CN103895102A (en) * | 2012-12-27 | 2014-07-02 | 嘉兴市博宏新型建材有限公司 | Horizontal mortar mixing machine |
| CN104002353B (en) * | 2014-04-23 | 2017-02-15 | 信阳市四通机械制造有限公司 | Material mixing and stirring machine for plant fiberboards |
| CN105603523A (en) * | 2016-03-16 | 2016-05-25 | 江苏华盛天龙光电设备股份有限公司 | Raw material mixing device for single-crystal furnace |
| CN106440739B (en) * | 2016-08-28 | 2018-11-23 | 张淼 | Oar blade type whirlwind dryer production line and production method |
| CN107029576A (en) * | 2017-03-31 | 2017-08-11 | 浙江华庆元生物科技有限公司 | The agitating device of organic waste microbial processor |
| CN109059468A (en) * | 2018-06-14 | 2018-12-21 | 陈伟 | It is a kind of can be to the equipment of drying materials using air |
| CN109943881A (en) * | 2019-04-10 | 2019-06-28 | 中国科学院上海光学精密机械研究所 | A crystal carrier for the growth of KDP long-seed single-cone crystals |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4483625A (en) * | 1981-02-10 | 1984-11-20 | Technovators, Inc. | Continuous solid particulate mixer conveyor having variable capacity |
-
1994
- 1994-02-03 JP JP3082294A patent/JPH07218139A/en active Pending
- 1994-05-10 CN CN94105009A patent/CN1069223C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4483625A (en) * | 1981-02-10 | 1984-11-20 | Technovators, Inc. | Continuous solid particulate mixer conveyor having variable capacity |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07218139A (en) | 1995-08-18 |
| CN1118715A (en) | 1996-03-20 |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |