CN104984677A - Viscous liquid material mixing and stirring device - Google Patents
Viscous liquid material mixing and stirring device Download PDFInfo
- Publication number
- CN104984677A CN104984677A CN201510439880.7A CN201510439880A CN104984677A CN 104984677 A CN104984677 A CN 104984677A CN 201510439880 A CN201510439880 A CN 201510439880A CN 104984677 A CN104984677 A CN 104984677A
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- stirring
- shaft
- stirring shell
- liquid material
- thick liquid
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- 238000003756 stirring Methods 0.000 title claims abstract description 70
- 239000011344 liquid material Substances 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 abstract description 32
- 230000000694 effects Effects 0.000 abstract description 4
- 230000005540 biological transmission Effects 0.000 abstract 1
- 239000012530 fluid Substances 0.000 description 29
- 239000000463 material Substances 0.000 description 9
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention provides a viscous liquid material mixing and stirring device comprising a stirring housing. A coaxial stirring shaft is assembled inside the stirring housing. The stirring shaft is rotatably assembled in the stirring housing. The stirring shaft is connected with a transmission structure. The stirring shaft is divided into an upper section and a lower section. A spiral blade around the shaft is arranged on the upper section of the stirring shaft, and stirring bars are arranged on the circumferential surface of the lower section of the stirring shaft. A thin liquid cavity is processed in the stirring shaft at the middle part along the axis. Liquid inlet holes communicating with the thin liquid cavity are distributed on the stirring bars. Viscous liquid is arranged in the stirring housing, and thin liquid is arranged in the thin liquid cavity. The device has the advantages of a simple and compact structure and a small volume. With the device, viscous liquid can be gradually mixed, and a mixing effect is better. Also, hydraulic pressure can be added to the viscous liquid, such that the viscous liquid can flow faster.
Description
Technical field
The invention belongs to fluent material technical field of processing equipment, especially relate to a kind of thick liquid material mixed stirring device.
Background technology
Material manifests different character according to the difference of its component; in order to make the combination property of material more excellent; people usually can be used in combination by different materials, or with some materials for main some other materials that add wherein make this material obtain excellent performance.The mixing of material has been come by special equipment, for the mixing of liquid, people use the equipment of stirring structure usually, in concrete process of producing, the liquid of thickness class is difficult to stir, and the liquid of thickness class is difficult to carry in pipeline, and the liquid of thickness class is difficult to stir when stirring, and is also difficult to other materials mixing.
Summary of the invention
For above-mentioned problem, the object of the present invention is to provide and a kind ofly can will be blended in thick liquid easily by sparse uniform liquid, the thick liquid material mixed stirring device of larger liquid-driving pressure can be produced simultaneously in liquid.
The technical solution adopted for the present invention to solve the technical problems is: this thick liquid material mixed stirring device comprises stirring shell, described stirring shell is round tube shape, described stirring shell is vertically assembled, the mounted inside of described stirring shell has coaxial shaft, rotatable assembling between described shaft and stirring shell, described shaft is connected with drive mechanism; Described shaft is divided into two sections, the epimere of described shaft is equipped with the blade around axle spiral, the periphery of the hypomere of described shaft is equipped with puddler, described shaft is processed with sparse sap cavity along the centre position of axis, described puddler is distributed with the inlet opening be communicated with described sparse sap cavity; Be equipped with viscous fluid in described stirring shell, in described sparse sap cavity, be equipped with sparse solution.
As preferably, the upper design of described stirring shell has the admission chamber of inclination, and the upper design of described admission chamber has closing cap, described closing cap is designed with the feed liquor mouth of pipe, and described closing cap is stretched out on the top of described shaft.
As preferably, the bottom of described stirring shell is connected with output pipe by pressure valve.
As preferably, the outer edge of described blade is less than 2mm to the gap of wall pieces in stirring shell.
As preferably, the number of described puddler is more than three, is distributed in the circumference of described shaft bottom.
Beneficial effect of the present invention is: this thick liquid material mixed stirring device is mainly used to realize mixing of comparatively sparse liquid and thick liquid, wherein sparse liquid needs to pass in described shaft when there being elevated pressures, and the liquid of thickness passes in described stirring shell, when described shaft is driven to rotate, the blade of described spiral can produce downward extruding force to viscous fluid in atwirl situation, for viscous fluid provides output pressure, described viscous fluid is when entering the lower ranges of described shaft simultaneously, described puddler can play the stirring action to viscous fluid, in described shaft, sparse liquid can enter in viscous fluid by the inlet opening of sparse sap cavity and puddler simultaneously, due to the rotation of shaft, described puddler constantly stirs in viscous fluid, what make the uniform liquid in described shaft enters viscous fluid, simultaneously due to the stirring of blade, viscous fluid is constantly flowed downward, sparse liquid can be made so constantly evenly to dissolve in viscous fluid.This apparatus structure is simply compact, small volume, can to thick liquid mixing progressively, and mixed effect is better, can increase hydraulic pressure simultaneously, viscous fluid can be added as and flow fast viscous fluid.
Accompanying drawing explanation
Fig. 1 is the structural representation of thick liquid material mixed stirring device forward section;
Fig. 2 is the structural representation that thick liquid material mixed stirring device overlooks direction.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention is further described:
As shown in embodiment in Fig. 1 and Fig. 2, this thick liquid material mixed stirring device comprises stirring shell 1, described stirring shell 1 is round tube shape, described stirring shell 1 is vertically assembled, the mounted inside of described stirring shell 1 has coaxial shaft 2, rotatable assembling between described shaft 2 and stirring shell 1, described shaft 2 is connected with drive mechanism; It is characterized in that: described shaft 2 is divided into two sections, the epimere of described shaft 2 is equipped with the blade 21 around axle spiral, the periphery of the hypomere of described shaft 2 is equipped with puddler 22, described shaft 2 is processed with sparse sap cavity 23 along the centre position of axis, described puddler 22 is distributed with the inlet opening 24 be communicated with described sparse sap cavity; Be equipped with viscous fluid in described stirring shell 1, in described sparse sap cavity 23, be equipped with sparse solution.
This thick liquid material mixed stirring device is mainly used to realize mixing of comparatively sparse liquid and thick liquid, wherein sparse liquid needs to pass in described shaft 2 when there being elevated pressures, and the liquid of thickness passes in described stirring shell 1, when described shaft 2 is driven to rotate, the blade 21 of described spiral can produce downward extruding force to viscous fluid in atwirl situation, for viscous fluid provides output pressure, described viscous fluid is when entering the lower ranges of described shaft 2 simultaneously, described puddler 22 can play the stirring action to viscous fluid, in described shaft 2, sparse liquid can enter in viscous fluid by the inlet opening 24 of sparse sap cavity 23 and puddler 22 simultaneously, due to the rotation of shaft 2, described puddler 22 constantly stirs in viscous fluid, what make the uniform liquid in described shaft 2 enters viscous fluid, simultaneously due to the stirring of blade 21, viscous fluid is constantly flowed downward, sparse liquid can be made so constantly evenly to dissolve in viscous fluid.This apparatus structure is simply compact, small volume, can to thick liquid mixing progressively, and mixed effect is better, can increase hydraulic pressure simultaneously, viscous fluid can be added as and flow fast viscous fluid.
As depicted in figs. 1 and 2, the upper design of described stirring shell 1 has the admission chamber 11 of inclination, and the upper design of described admission chamber 11 has closing cap 12, and described closing cap 12 is designed with the feed liquor mouth of pipe 13, and described closing cap 12 is stretched out on the top of described shaft 2.The described feed liquor mouth of pipe 13 is designed with helicitic texture, is convenient to be connected with screwed pipe, the design of described admission chamber 11 makes viscous fluid be more prone to enter described stirring shell 1.
As shown in Figure 1, the bottom of described stirring shell 1 is connected with output pipe by pressure valve 3.The pressure of described viscous fluid in stirring shell 1 can be kept like this, make viscous fluid have larger fluid pressure when being stirred and exporting stirring shell 1.
The outer edge of described blade 21 is less than 2mm to the gap of wall pieces in stirring shell 1.The pressure effect of blade 21 pairs of viscous fluids can be ensured like this.
As shown in Figure 1, the number of described puddler 22 is more than three, is distributed in the circumference of described shaft 2 bottom.The number of puddler 22 is more, is uniformly mixed efficiency higher, but consumed power is also larger.
Claims (5)
1. a thick liquid material mixed stirring device, it comprises stirring shell (1), described stirring shell (1) is round tube shape, described stirring shell (1) is vertically assembled, the mounted inside of described stirring shell (1) has coaxial shaft (2), rotatable assembling between described shaft (2) and stirring shell (1), described shaft (2) is connected with drive mechanism; It is characterized in that: described shaft (2) is divided into two sections, the epimere of described shaft (2) is equipped with the blade (21) around axle spiral, the periphery of the hypomere of described shaft (2) is equipped with puddler (22), described shaft (2) is processed with sparse sap cavity (23) along the centre position of axis, described puddler (22) is distributed with the inlet opening (24) be communicated with described sparse sap cavity (23).
2. thick liquid material mixed stirring device according to claim 1, it is characterized in that: the upper design of described stirring shell (1) has the admission chamber (11) of inclination, the upper design of described admission chamber (11) has closing cap (12), described closing cap (12) is designed with the feed liquor mouth of pipe (13), described closing cap (12) is stretched out on the top of described shaft (2).
3. thick liquid material mixed stirring device according to claim 1, is characterized in that: the bottom of described stirring shell (1) is connected with output pipe by pressure valve (3).
4. thick liquid material mixed stirring device according to claim 1, is characterized in that: the outer edge of described blade (21) is less than 2mm to the gap of stirring shell (1) interior wall pieces.
5. thick liquid material mixed stirring device according to claim 1, is characterized in that: the number of described puddler (22) is more than three, is distributed in the circumference of described shaft (2) bottom.
Priority Applications (1)
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CN201510439880.7A CN104984677B (en) | 2015-07-24 | 2015-07-24 | Viscous liquid material mixing and stirring device |
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CN201510439880.7A CN104984677B (en) | 2015-07-24 | 2015-07-24 | Viscous liquid material mixing and stirring device |
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CN104984677A true CN104984677A (en) | 2015-10-21 |
CN104984677B CN104984677B (en) | 2017-05-03 |
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CN201510439880.7A Active CN104984677B (en) | 2015-07-24 | 2015-07-24 | Viscous liquid material mixing and stirring device |
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Citations (11)
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---|---|---|---|---|
US3618903A (en) * | 1969-04-02 | 1971-11-09 | Buss Ag | Mixing and kneading device |
CN2138521Y (en) * | 1992-10-06 | 1993-07-21 | 翟学良 | Hollow material feeding stirrer |
JP2006239567A (en) * | 2005-03-03 | 2006-09-14 | Atsushi Ichiki | Impeller |
CN202570119U (en) * | 2012-06-06 | 2012-12-05 | 上虞市双良化工设备有限公司 | Gas-liquid reaction kettle |
CN203227483U (en) * | 2012-11-14 | 2013-10-09 | 中国石油天然气股份有限公司 | Mixing and coagulating kettle |
CN203990643U (en) * | 2014-06-30 | 2014-12-10 | 宁波大学 | A kind of for stirring the substance reaction still of high viscosity |
CN204034603U (en) * | 2014-06-26 | 2014-12-24 | 北京盛昌百年石油科技有限公司 | A kind of mixing tank |
CN204208567U (en) * | 2014-08-28 | 2015-03-18 | 杭州协红科技咨询有限公司 | A kind of petrochemical industry reactor |
CN204247128U (en) * | 2014-12-04 | 2015-04-08 | 沈信敏 | A kind of agitating device adjusting oil tank |
CN204429156U (en) * | 2015-01-30 | 2015-07-01 | 湖北吉斯生物科技有限公司 | A kind of biochemical reagents mixing plant |
CN204973668U (en) * | 2015-07-24 | 2016-01-20 | 苏州硅果电子有限公司 | Thick liquid material mixture agitating unit |
-
2015
- 2015-07-24 CN CN201510439880.7A patent/CN104984677B/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3618903A (en) * | 1969-04-02 | 1971-11-09 | Buss Ag | Mixing and kneading device |
CN2138521Y (en) * | 1992-10-06 | 1993-07-21 | 翟学良 | Hollow material feeding stirrer |
JP2006239567A (en) * | 2005-03-03 | 2006-09-14 | Atsushi Ichiki | Impeller |
CN202570119U (en) * | 2012-06-06 | 2012-12-05 | 上虞市双良化工设备有限公司 | Gas-liquid reaction kettle |
CN203227483U (en) * | 2012-11-14 | 2013-10-09 | 中国石油天然气股份有限公司 | Mixing and coagulating kettle |
CN204034603U (en) * | 2014-06-26 | 2014-12-24 | 北京盛昌百年石油科技有限公司 | A kind of mixing tank |
CN203990643U (en) * | 2014-06-30 | 2014-12-10 | 宁波大学 | A kind of for stirring the substance reaction still of high viscosity |
CN204208567U (en) * | 2014-08-28 | 2015-03-18 | 杭州协红科技咨询有限公司 | A kind of petrochemical industry reactor |
CN204247128U (en) * | 2014-12-04 | 2015-04-08 | 沈信敏 | A kind of agitating device adjusting oil tank |
CN204429156U (en) * | 2015-01-30 | 2015-07-01 | 湖北吉斯生物科技有限公司 | A kind of biochemical reagents mixing plant |
CN204973668U (en) * | 2015-07-24 | 2016-01-20 | 苏州硅果电子有限公司 | Thick liquid material mixture agitating unit |
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CN104984677B (en) | 2017-05-03 |
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Effective date of registration: 20231219 Address after: 310000 Cibi Village, Huanghu Town, Yuhang District, Hangzhou City, Zhejiang Province Patentee after: Hangzhou Huanghu Xinye Chemical Factory Address before: 215101 102, room 3, 9 Jin Feng Nan Road, Mu Du Town, Wuzhong District, Suzhou, Jiangsu. Patentee before: SUZHOU SILICON FRUIT ELECTRONICS Co.,Ltd. |
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