CN204017699U - A kind of horizontal solid-liquid mixing apparatus - Google Patents
A kind of horizontal solid-liquid mixing apparatus Download PDFInfo
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- CN204017699U CN204017699U CN201420390329.9U CN201420390329U CN204017699U CN 204017699 U CN204017699 U CN 204017699U CN 201420390329 U CN201420390329 U CN 201420390329U CN 204017699 U CN204017699 U CN 204017699U
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- cylindrical shell
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Abstract
The utility model provides a kind of horizontal solid-liquid mixing apparatus, comprises feeding-in solid body mouth, exhaust outlet, liquid inlet opening, pulverizing fly cutter, discharge port, shaft, stirring colter, cylindrical shell and scraper plate; The coaxial setting of described shaft and cylindrical shell, the side of described cylindrical shell Lower Half is provided with pulverizing fly cutter, and the axis of described pulverizing fly cutter is along the radially setting of cylindrical shell.The utility model 1. solid meter and liquid meter is realized the weight proportion automatic gauge of powder and liquid; 2. pulverize fly cutter strong throwing after the crushing material of flowing through fallen apart, make the continuous convection current of material, spread, stir, reach uniform mixing within the extremely short time, mixing efficiency is high; 3. liquid distribution trough contacts with solid after uniform liquid is disperseed, and increases solid-liquid contact area, reduces the phenomenon of uniting; 4. in the cavity forming with heat exchange jacket in cylindrical shell outside, pass into cooling or heat medium, prevent or the mixture coagulates that slows down, stir more abundant, simple in structure, low in energy consumption.
Description
Technical field
The utility model relates to a kind of horizontal solid-liquid mixing apparatus, specifically a kind of horizontal solid-liquid mixing apparatus for powdered rubber or stickum mixing.
Background technology
From the forties in last century, solid-liquid stirring operation is widely used in industrial process.Conventional solid-liquid mixed method is that liquid and solid are joined in mixing plant and make its mixing by mechanical agitation according to certain ratio.
Traditional mixing plant for granularity thinner powder or the liquid viscosity that need to mix when larger, liquid only can rest on the surface dissolution of powder, can not be penetrated into powder inside, easily there is the wall sticking phenomenon of uniting, need to repeatedly be uniformly mixed just and can reach ideal effect, greatly increase mixed cost.
In addition, in traditional hybrid technique process, do not consider that solid-liquid mixes the impact of the anti-energy that should absorb or discharge of generation chemistry on mixing effect.The intermediate for example producing in total utilization of PCA technique mixes the generation of generation chemical reaction fluosilicate with sulfuric acid can lump when temperature is lower, thereby easily stick in to stir on colter, loses mixed effect.
Chinese patent CN201375884Y discloses a kind of horizontal solid-liquid mixer, and this device passes through the rotating speed of reduction shaft to reduce shaft, to stir colter and the wearing and tearing of scraper plate in whipping process, and by increasing the effect that guarantees mixing in incorporation time.The mixing efficiency of this device is low, and can not solve granularity thinner powder or the liquid viscosity that need to mix when larger, sticky wall or easily stick in the problem stirring on colter occurs uniting; The weight proportion of powder and liquid obtains human metering, can not directly measure by equipment, and when having various ingredients to mix, operating process extremely bothers.
Utility model content
For solving the problems of the technologies described above, the utility model provides a kind of horizontal solid-liquid mixing apparatus, this horizontal solid-liquid mixing apparatus is by cylindrical shell Lower Half, pulverizing fly cutter being set, and in the top of feeding-in solid body mouth and liquid inlet opening correspondence, solid meter and liquid meter is set respectively.
The utility model is achieved by the following technical programs.
A kind of horizontal solid-liquid mixing apparatus that the utility model provides, comprises feeding-in solid body mouth, exhaust outlet, liquid inlet opening, pulverizing fly cutter, discharge port, shaft, stirring colter, cylindrical shell and scraper plate; The coaxial setting of described shaft and cylindrical shell, described shaft is provided with stirring colter, in the middle of the top of described cylindrical shell, be provided with exhaust outlet, the left side of described exhaust outlet is provided with feeding-in solid body mouth, right side is provided with liquid inlet opening, on the shaft corresponding with feeding-in solid body mouth, be fixed with scraper plate, the bottom of described cylindrical shell is provided with discharge port, and the side of described cylindrical shell Lower Half is provided with pulverizing fly cutter, and the axis of described pulverizing fly cutter is along the radially setting of cylindrical shell.
The dihedral angle forming between the normal plane at the axis place of described pulverizing fly cutter and horizontal plane is 30 °～60 °.
Described pulverizing fly cutter assembly comprises fly cutter and motor B, and described fly cutter is fixedly connected with the output shaft of motor B; The fly cutter of described pulverizing fly cutter assembly is placed in cylindrical shell inner side, and motor B is placed in cylindrical shell outside.
Described feeding-in solid body mouth top is also fixedly connected with solid meter, and described liquid inlet opening top is also fixedly connected with liquid meter.
Before and after described pulverizing fly cutter, be symmetrically distributed on the side of cylindrical shell Lower Half.
Described cylindrical shell outside is provided with heat exchange jacket, and the length of described heat exchange jacket is less than the length of cylindrical shell, and described heat exchange jacket is surrounded on cylindrical shell outside, and is connected with the side seal of cylindrical shell.
The lower end of described liquid inlet opening is fixedly connected with liquid distribution trough, and the bus of described liquid distribution trough and cylindrical shell be arranged in parallel.
On described shaft, every 300-500mm, arrange one group and stir colter, every group is provided with 3～5 stirring colters, and described stirring colter is evenly distributed and makes progress in the week of shaft.
The outer surface of described stirring colter is through Wear-resistant Treatment, and surface treatment thickness is 0.1mm～0.5mm.
The valve of described discharge port is selected manually-operated gate, operated pneumatic valve or electrically operated valve.
The beneficial effects of the utility model are: the liquid meter that is 1. arranged on the solid meter on feeding-in solid body mouth top and is arranged on liquid inlet opening can be realized the weight proportion automatic gauge of powder and liquid; 2. on the side of cylindrical shell Lower Half, the pulverizing fly cutter of High Rotation Speed falls apart strong throwing after the crushing material of flowing through, and makes the continuous convection current of material, spreads, stirs, and reaches uniform mixing within the extremely short time, and mixing efficiency is high; 3. the liquid distribution trough being connected with liquid inlet opening lower end contacts with solid after uniform liquid is disperseed, and increases solid-liquid contact area, reduces as much as possible the phenomenon of uniting; 4. in the cavity forming with heat exchange jacket in cylindrical shell outside, pass into cooling or heat medium, with the heat that absorbs or discharge in balance mixed process, prevent from or slow down the mixture coagulates of chemical reaction occurs, make to stir more abundant, simple in structure, low in energy consumption.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the left view of Fig. 1;
Fig. 3 is the structural representation of pulverizing fly cutter assembly of the present utility model;
In figure: 1-solid meter, 2-feeding-in solid body mouth, 3-exhaust outlet, 4-liquid meter, 5-liquid inlet opening, 6-heat exchange jacket, 7-pulverizes fly cutter assembly, 8-discharge port, 9-shaft, 10-stirs colter, 11-cylindrical shell, 12-liquid distribution trough, 13-scraper plate, 14-decelerator, 15-motor A, 16-fly cutter, 17 motor B.
The specific embodiment
Further describe the technical solution of the utility model below, but described in claimed scope is not limited to.
A kind of horizontal solid-liquid mixing apparatus as depicted in figs. 1 and 2, comprises feeding-in solid body mouth 2, exhaust outlet 3, liquid inlet opening 5, pulverizing fly cutter 7, discharge port 8, shaft 9, stirs colter 10, cylindrical shell 11 and scraper plate 13; The coaxial setting of described shaft 9 and cylindrical shell 11, described shaft 9 is provided with and stirs colter 10, in the middle of the top of described cylindrical shell 11, be provided with exhaust outlet 3, the left side of described exhaust outlet 3 is provided with feeding-in solid body mouth 2, right side is provided with liquid inlet opening 5, on the shaft 9 corresponding with feeding-in solid body mouth 2, be fixed with scraper plate 13, the bottom of described cylindrical shell 11 is provided with discharge port 8, and the side of described cylindrical shell 11 Lower Halves is provided with pulverizes fly cutter 7, and the axis of described pulverizing fly cutter 7 is along the radially setting of cylindrical shell 11.
The dihedral angle forming between the normal plane at the axis place of described pulverizing fly cutter 7 and horizontal plane is 30 °～60 °.Mixture after the stirring colter 10 on shaft 9 stirs is stirring under the effect of colter 10, a part is splashed to longitudinal end along cylindrical shell 11 inwalls, along stirring colter 10 sides, outwards splash again on the other hand, the position of pulverizing fly cutter 7 installations can make all materials that splash all need just can enter the discharge port 8 of cylindrical shell 11 bottoms after pulverizing fly cutter 7.
Described pulverizing fly cutter assembly 7 comprises fly cutter 16 and motor 17, and described fly cutter 16 is fixedly connected with the output shaft of motor 17; The fly cutter 16 of described pulverizing fly cutter assembly 7 is placed in cylindrical shell 11 inner sides, and motor B17 is placed in cylindrical shell 11 outsides.Pulverizing fly cutter assembly 7 is arranged on cylindrical shell 11 by bearing seal.
Described feeding-in solid body mouth 2 tops are also fixedly connected with solid meter 1, and described liquid inlet opening 5 tops are also fixedly connected with liquid meter 4.The weight that solid meter 1 and liquid meter 4 are metered into the various components of mixing chamber mixing accurately, can realize accurate weight proportion; Solid meter 1 and liquid meter 4 replace manual metering, simplified operating procedure, and the data of metering are reliable.
Described pulverizing fly cutter 7 front and back are symmetrically distributed on the side of cylindrical shell 11 Lower Halves.The material splashing can be fallen apart by strong throwing of pulverizing fly cutter 7 of High Rotation Speed more fully, further guarantees that material fully mixes.
The quantity of described pulverizing fly cutter 7 is 3～6.Pulverizing the quantity of fly cutter 7 can set according to actual needs, the waste that fly cutter 7 can cause energy consumption is pulverized in too much arranging, very few setting pulverized fly cutter 7 and can be caused mixing of materials insufficient, can not reach desirable mixed effect, so 3～6 pulverizing fly cuttves 7 are preferably set on cylindrical shell 11.
Described cylindrical shell 11 outsides are provided with heat exchange jacket 6, and the length of described heat exchange jacket 6 is less than the length of cylindrical shell 11, and described heat exchange jacket 6 is surrounded on cylindrical shell 11 outsides, and are connected with the side seal of cylindrical shell 11.According to the character of mixing solid liquid phase, in heat exchange jacket 6, pass into cooling or heat medium, with the heat that absorbs or discharge in balance mixed process, prevent from or slow down the mixture coagulates of chemical reaction occurs, thus the effect that assurance mixes.
The lower end of described liquid inlet opening 5 is fixedly connected with liquid distribution trough 12, and described liquid distribution trough 12 be arranged in parallel with the bus of cylindrical shell 11.Liquid enters liquid distribution trough 12 by liquid inlet opening 2, and liquid rear evenly the flowing to lentamente in cylindrical shell 11 of liquid distribution trough 12 of flowing through contacts mixing with solid, effectively prevent the wall sticking phenomenon of uniting.
On described shaft, every 300-500mm, arrange one group and stir colter, every group is provided with 3～5 stirring colters, and described stirring colter is evenly distributed and makes progress in the week of shaft.
The outer surface process Wear-resistant Treatment of described stirring colter 10, the wearing and tearing in whipping process, its surface treatment thickness is 0.1mm～0.5mm.The quantity of described stirring colter 10 is 4～10.
The valve of described discharge port 8 can be selected manually-operated gate, operated pneumatic valve or electrically operated valve etc.
Solid material is entered in cylindrical shell 11 by feeding-in solid body mouth 2 by solid meter 1, and liquid material enters liquid distribution trough 12 by liquid meter 4 by liquid inlet opening 5, and then enters in cylindrical shell 11 and solids mixing from liquid distribution trough 12.The output shaft of motor A15 drives shaft 9 rotations through decelerator 14, be fixed at and on shaft 9, stir colter 10 and follow shaft 9 and rotate together, material in cylindrical shell 11 is stirring under the effect of colter 10, to longitudinal end and stirring colter 10 both sides of cylindrical shell 11, splashes.When material flow is when pulverizing fly cutter 7, by strong throwing of pulverizing fly cutter 7 of High Rotation Speed, fallen apart; Material, stirring colter 10 and pulverizing under the compound action of fly cutter 7, makes the continuous convection current of material, spreads, stirs, and reaches uniform mixed effect within the extremely short time.In mixed process according to the character of mixing solid liquid phase, in the cavity forming to cylindrical shell outside and heat exchange jacket, pass into cooling or heat medium, with the heat that absorbs or discharge in balance mixed process, prevent from or slow down the mixture coagulates of chemical reaction occurs, thereby guarantee the effect of mixing, the gas producing in mixed process is by outside exhaust outlet 3 discharge systems.Material after mixing transports arrival desired location after being discharged by discharge port 8.
Claims (10)
1. a horizontal solid-liquid mixing apparatus, comprise feeding-in solid body mouth (2), exhaust outlet (3), liquid inlet opening (5), pulverize fly cutter assembly (7), discharge port (8), shaft (9), stir colter (10), cylindrical shell (11) and scraper plate (13), it is characterized in that: the coaxial setting of described shaft (9) and cylindrical shell (11), described shaft (9) is provided with and stirs colter (10), in the middle of the top of described cylindrical shell (11), be provided with exhaust outlet (3), the left side of described exhaust outlet (3) is provided with feeding-in solid body mouth (2), right side is provided with liquid inlet opening (5), on the shaft (9) corresponding with feeding-in solid body mouth (2), be fixed with scraper plate (13), the bottom of described cylindrical shell (11) is provided with discharge port (8), the side of described cylindrical shell (11) Lower Half is provided with pulverizes fly cutter assembly (7), the axis of described pulverizing fly cutter assembly (7) is along the radially setting of cylindrical shell (11).
2. horizontal solid-liquid mixing apparatus as claimed in claim 1, is characterized in that: the dihedral angle forming between the normal plane at the axis place of described pulverizing fly cutter assembly (7) and horizontal plane is 30 °～60 °.
3. horizontal solid-liquid mixing apparatus as claimed in claim 1, is characterized in that: described pulverizing fly cutter assembly (7) comprises fly cutter (16) and motor B (17), and described fly cutter (16) is fixedly connected with the output shaft of motor B (17); The fly cutter (16) of described pulverizing fly cutter assembly (7) is placed in cylindrical shell (11) inner side, and motor B (17) is placed in cylindrical shell (11) outside.
4. horizontal solid-liquid mixing apparatus as claimed in claim 1, it is characterized in that: described feeding-in solid body mouth (2) top is also fixedly connected with solid meter (1), described liquid inlet opening (5) top is also fixedly connected with liquid meter (4).
5. horizontal solid-liquid mixing apparatus as claimed in claim 2 or claim 3, is characterized in that: before and after described pulverizing fly cutter assembly (7), be symmetrically distributed on the side of cylindrical shell (11) Lower Half.
6. horizontal solid-liquid mixing apparatus as claimed in claim 1, it is characterized in that: described cylindrical shell (11) outside is provided with heat exchange jacket (6), the length of described heat exchange jacket (6) is less than the length of cylindrical shell (11), described heat exchange jacket (6) is surrounded on cylindrical shell (11) outside, and is connected with the side seal of cylindrical shell (11).
7. horizontal solid-liquid mixing apparatus as claimed in claim 1, it is characterized in that: the lower end of described liquid inlet opening (5) is fixedly connected with liquid distribution trough (12), described liquid distribution trough (12) be arranged in parallel with the bus of cylindrical shell (11).
8. horizontal solid-liquid mixing apparatus as claimed in claim 1, it is characterized in that: described shaft (9) is upper arranges one group of stirring colter (10) every 300-500mm, every group is provided with 3～5 stirring colters (10), and described stirring colter (10) is evenly distributed and makes progress in the week of shaft (9).
9. horizontal solid-liquid mixing apparatus as claimed in claim 1, is characterized in that: the outer surface of described stirring colter (10) is through Wear-resistant Treatment, and surface treatment thickness is 0.1mm～0.5mm.
10. horizontal solid-liquid mixing apparatus as claimed in claim 1, is characterized in that: the valve of described discharge port (8) is selected manually-operated gate, operated pneumatic valve or electrically operated valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420390329.9U CN204017699U (en) | 2014-07-15 | 2014-07-15 | A kind of horizontal solid-liquid mixing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420390329.9U CN204017699U (en) | 2014-07-15 | 2014-07-15 | A kind of horizontal solid-liquid mixing apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN204017699U true CN204017699U (en) | 2014-12-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420390329.9U Expired - Fee Related CN204017699U (en) | 2014-07-15 | 2014-07-15 | A kind of horizontal solid-liquid mixing apparatus |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104725289A (en) * | 2015-03-20 | 2015-06-24 | 周建康 | Preparation device of calcium 2-hydroxy-4-methylthio-butyrate |
| CN104923098A (en) * | 2015-06-09 | 2015-09-23 | 施婷婷 | All-in-one machine integrating foodstuff cutting and stirring |
| CN106076149A (en) * | 2016-08-01 | 2016-11-09 | 美科机械有限公司 | A kind of horizontal wave colter mixer being applicable to solid-liquid mixing |
| CN106422849A (en) * | 2016-10-10 | 2017-02-22 | 芜湖瑞德机械科技有限公司 | Heating and stirring device for coating, and operating method thereof |
| CN108041110A (en) * | 2018-01-23 | 2018-05-18 | 佛山市雅路斯工业设备有限公司 | A kind of material inflation method and device with pellet |
| CN111375341A (en) * | 2018-12-29 | 2020-07-07 | 上海数郜机电有限公司 | Horizontal mixing tank |
| CN112915944A (en) * | 2021-01-22 | 2021-06-08 | 周口师范学院 | Preparation equipment of nano-scale titanium dioxide photocatalytic environment purification material |
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2014
- 2014-07-15 CN CN201420390329.9U patent/CN204017699U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104725289A (en) * | 2015-03-20 | 2015-06-24 | 周建康 | Preparation device of calcium 2-hydroxy-4-methylthio-butyrate |
| CN104725289B (en) * | 2015-03-20 | 2017-03-15 | 周建康 | The preparation facilitiess of 2 hydroxyl, 4 methylthio calcium butyrate |
| CN104923098A (en) * | 2015-06-09 | 2015-09-23 | 施婷婷 | All-in-one machine integrating foodstuff cutting and stirring |
| CN104923098B (en) * | 2015-06-09 | 2017-04-12 | 施婷婷 | All-in-one machine integrating foodstuff cutting and stirring |
| CN106076149A (en) * | 2016-08-01 | 2016-11-09 | 美科机械有限公司 | A kind of horizontal wave colter mixer being applicable to solid-liquid mixing |
| CN106422849A (en) * | 2016-10-10 | 2017-02-22 | 芜湖瑞德机械科技有限公司 | Heating and stirring device for coating, and operating method thereof |
| CN108041110A (en) * | 2018-01-23 | 2018-05-18 | 佛山市雅路斯工业设备有限公司 | A kind of material inflation method and device with pellet |
| CN111375341A (en) * | 2018-12-29 | 2020-07-07 | 上海数郜机电有限公司 | Horizontal mixing tank |
| CN112915944A (en) * | 2021-01-22 | 2021-06-08 | 周口师范学院 | Preparation equipment of nano-scale titanium dioxide photocatalytic environment purification material |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141217 Termination date: 20150715 |
|
| EXPY | Termination of patent right or utility model |