CN218056731U - A ejection of compact cooling system for emulsifier - Google Patents
A ejection of compact cooling system for emulsifier Download PDFInfo
- Publication number
- CN218056731U CN218056731U CN202222344139.0U CN202222344139U CN218056731U CN 218056731 U CN218056731 U CN 218056731U CN 202222344139 U CN202222344139 U CN 202222344139U CN 218056731 U CN218056731 U CN 218056731U
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- Prior art keywords
- emulsifier
- stirring
- pipe
- stirring tank
- interlayer
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- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 89
- 238000001816 cooling Methods 0.000 title claims abstract description 44
- 238000003756 stirring Methods 0.000 claims abstract description 115
- 239000011229 interlayer Substances 0.000 claims abstract description 27
- 238000004321 preservation Methods 0.000 claims abstract description 20
- 239000002826 coolant Substances 0.000 claims abstract description 14
- 239000010410 layer Substances 0.000 claims abstract description 7
- 238000012544 monitoring process Methods 0.000 claims abstract description 3
- 238000002156 mixing Methods 0.000 claims description 15
- 238000000926 separation method Methods 0.000 claims description 9
- 238000009413 insulation Methods 0.000 claims description 7
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000001154 acute effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000110 cooling liquid Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
Abstract
The application relates to a discharge cooling system for an emulsifier, which comprises a stirring tank, a cooling pipe, a heat preservation pipe and a temperature monitor, wherein the stirring tank is a double-layer stirring tank and is provided with an interlayer; the cooling pipe is communicated with the interlayer and used for guiding a cooling medium to the interlayer, and a first valve is arranged on the periphery of the cooling pipe; the heat preservation pipe is communicated with the interlayer and used for guiding a heat preservation medium to the interlayer, and a second valve is arranged on the periphery of the heat preservation pipe; the temperature monitor is used for monitoring the temperature of the emulsifier. This application has the effect that carries out temperature adjustment and maintenance to the emulsifier that is about to fill fast.
Description
Technical Field
The application relates to the field of emulsifier production equipment, in particular to a discharge cooling system for an emulsifier.
Background
The emulsifier is a substance capable of forming a stable emulsion from a mixture of two or more immiscible components. The emulsifier is applied to various industries, wherein the emulsifier has wide application in food processing industry and cosmetic industry.
After the emulsifier is stirred in the stirring tank, the emulsifier needs to be cooled to a specific temperature and then conveyed to a filling machine for filling, however, in the process of conveying the emulsifier in the stirring tank to the filling machine, the temperature of the emulsifier required during filling needs to be kept stable and lower than that of the emulsifier in the stirring tank, so that the filling effect and efficiency can be ensured, and therefore, a cooling system is needed to quickly adjust and maintain the temperature of the emulsifier to be filled.
SUMMERY OF THE UTILITY MODEL
In order to quickly adjust and maintain the temperature of the emulsifier to be filled, the application provides a discharge cooling system for the emulsifier.
The application provides a ejection of compact cooling system for emulsifier adopts following technical scheme:
a discharging cooling system for an emulsifier comprises a stirring tank, a cooling pipe, a heat preservation pipe and a temperature monitor, wherein the stirring tank is a double-layer stirring tank and is provided with an interlayer; the cooling pipe is communicated with the interlayer, the cooling pipe is used for guiding a cooling medium to the interlayer, and a first valve is arranged on the periphery of the cooling pipe; the heat-insulating pipe is communicated with the interlayer, the heat-insulating pipe is used for guiding a heat-insulating medium to the interlayer, and a second valve is arranged on the periphery of the heat-insulating pipe; the temperature monitor is used for monitoring the temperature of the emulsifier.
By adopting the technical scheme, after the emulsifier is stirred in the stirring tank, the first valve is opened, the cooling medium is introduced into the interlayer through the cooling pipe, so that the emulsifier is cooled to a specific temperature, and then the cooling medium in the interlayer is discharged. Then close first valve, open the second valve, let in the heat preservation medium through the insulating tube in to the intermediate layer, keep warm to the emulsifier in the agitator tank, reduce the further refrigerated risk of emulsifier to the realization is carried out the effect of temperature adjustment and maintenance to the emulsifier that is about to fill fast.
Optionally, the heat insulation pipe further comprises a header pipe, the inner cavity of the cooling pipe and the inner cavity of the heat insulation pipe are both communicated with the inner cavity of the header pipe, and the inner cavity of the header pipe is communicated with the interlayer.
Through adopting above-mentioned technical scheme, utilize the house steward with the inner chamber of intermediate layer and cooling tube, intermediate layer and the inner chamber intercommunication of insulating tube, need not to set up two openings that are used for connecting cooling tube and insulating tube respectively at the jar wall of agitator tank this moment, reduce the manufacturing procedure of agitator tank, also reduce the maintenance cost of agitator tank simultaneously.
Optionally, the header pipe is connected to the lower end of the agitator tank.
By adopting the technical scheme, the emulsifier positioned at the bottom of the stirring tank is subjected to the pressure of the emulsifier from the upper part, and the heat is not easy to dissipate. When the main pipe is connected to the lower end of the stirring tank, and the cooling medium is introduced into the interlayer, the temperature rises after the cooling medium exchanges heat with the emulsifier at the bottom of the stirring tank, and the cooling medium flows upwards, so that the subsequently introduced cooling medium with lower temperature continuously exchanges heat with the emulsifier at the bottom of the stirring tank, and the emulsifier at the bottom of the stirring tank exchanges heat with the upper part of the emulsifier, namely the emulsifier in the middle of the stirring tank, and the uniformity of temperature distribution at each position inside the stirring tank is improved.
Optionally, the discharge port of the stirring tank is located at the lower end of the stirring tank, and the lower end of the stirring tank is conical.
By adopting the technical scheme, the emulsifier finishes discharging from the discharge hole, and because the lower end of the stirring tank is conical, the emulsifier slides to the discharge hole along the inclined plane of the lower end of the stirring tank under the action of gravity, so that the risk that the emulsifier is attached to the bottom of the stirring tank is reduced; in addition, the funnel-shaped lower end has a larger tank wall area, so that the emulsifier can be more sufficiently contacted with the tank wall, thereby further improving the uniformity of temperature distribution and simultaneously improving cooling efficiency.
Optionally, a stirring shaft is arranged inside the stirring tank, and the stirring tank is provided with a motor for driving the stirring shaft to rotate; at least one connecting rod is arranged on the periphery of the stirring shaft, and a scraper is arranged at one end of the connecting rod, which is far away from the stirring shaft; the side butt of scraper blade in the inner wall of agitator tank, the scraper blade is followed the direction of height extension setting of agitator tank, the scraper blade is close to the one side slope setting of the inner wall of agitator tank.
By adopting the technical scheme, when the emulsifier in the stirring tank is cooled and insulated, the stirring shaft can continue to rotate for uniform temperature. When the stirring shaft rotates, under the action of centrifugal force, the emulsifier flows radially and flows to the inner wall of the stirring tank, and the scraper is separated from the emulsifier attached to the tank wall. When the included angle between the axis of the connecting rod and the tangent plane of the scraper is an acute angle, the scraper has a diversion effect on the emulsifier, the emulsifier close to the inner wall of the stirring tank is promoted to exchange with the emulsifier in the middle of the stirring tank, and therefore the uniformity of the temperature distribution of all parts in the stirring tank is further promoted.
Optionally, the week side of (mixing) shaft is provided with helical blade, helical blade keeps away from the edge of (mixing) shaft is provided with at a distance from the separation blade, it follows to separate the separation blade helical blade's edge direction extends the setting, separate the surface of separation blade with the axis of (mixing) shaft is parallel.
By adopting the technical scheme, the stirring shaft drives the spiral blades to rotate in the rotating process, the emulsifier axially flows under the action of the spiral blades, so that the emulsifier in the stirring tank is exchanged up and down in the vertical direction, the separation baffle forms certain separation baffle for the emulsifier which moves along the radial direction under the action of centrifugal force, the exchange efficiency of the emulsifier up and down is improved, and the uniformity of the temperature distribution of each part in the stirring tank is promoted.
Optionally, the side wall of the helical blade far away from the stirring shaft is provided with a plurality of stirring blades, the stirring blades are arranged at intervals, and the surfaces of the stirring blades are coplanar with the surfaces of the helical blade.
Through adopting above-mentioned technical scheme, stirring vane is located between scraper blade and the helical blade, and it is rotatory to drive stirring vane when the (mixing) shaft is rotatory, and stirring vane cuts the emulsifier, because stirring vane's surface and helical blade's surface coplane, therefore stirring vane slope sets up, and stirring vane cuts the in-process of emulsifier and also has the water conservancy diversion effect to the emulsifier, promotes the upper and lower exchange of emulsifier on vertical direction, further promotes each part temperature distribution's homogeneity in the agitator tank.
Optionally, a first spoiler is arranged on the surface of the stirring blade, the surface of the first spoiler is perpendicular to the surface of the spiral blade, and a plurality of through holes are formed in the surface of the first spoiler in a penetrating manner and used for allowing an emulsifier to pass through.
Through adopting above-mentioned technical scheme, first spoiler further promotes each part temperature distribution's in the agitator tank homogeneity, and when the (mixing) shaft passed through stirring vane and drives first spoiler and rotate, partial emulsifier passed the through-hole to reduce the rotatory resistance of (mixing) shaft.
In summary, the present application includes at least one of the following beneficial technical effects:
1. by arranging the heat preservation pipe, after the emulsifier in the stirring tank is cooled, the heat preservation medium is guided to the interlayer to preserve heat of the emulsifier, so that the effect of quickly adjusting and maintaining the temperature of the emulsifier to be filled is realized;
2. the scraper is arranged in the stirring tank, so that the emulsifier attached to the inner wall of the stirring tank is separated from the inner wall of the stirring tank, and the risk that the emulsifier is attached to the inner wall of the stirring tank is further reduced;
3. the helical blades are arranged on the peripheral side of the stirring shaft, so that the up-and-down exchange of the emulsifier in the stirring tank is promoted, and the uniformity of the temperature distribution at each position in the stirring tank is promoted.
Drawings
Fig. 1 is a schematic view showing the overall structure of embodiment 1 of the present application.
FIG. 2 is a schematic view showing the structure of a stirring shaft in example 1 of the present application.
Fig. 3 is a schematic view of the overall structure for showing embodiment 2 of the present application.
Fig. 4 is an enlarged schematic view of a portion a of fig. 3.
Fig. 5 is a schematic structural view for showing a helical blade in embodiment 2 of the present application.
Fig. 6 is an enlarged schematic view of fig. 5 at a portion B.
Description of reference numerals: 1. a stirring tank; 11. a feed inlet; 12. a discharge port; 13. an interlayer; 14. a motor; 15. a stirring shaft; 151. a connecting rod; 152. a second spoiler; 16. a squeegee; 17. a helical blade; 171. separating sheets; 172. a stirring blade; 173. a first spoiler; 174. a through hole; 2. a header pipe; 3. a cooling tube; 31. a first valve; 4. a heat-insulating pipe; 41. a second valve; 5. and a temperature monitor.
Detailed Description
The present application is described in further detail below with reference to figures 1-6.
The embodiment of the application discloses an ejection of compact cooling system for emulsifier.
Example 1
Referring to fig. 1 and 2, a discharging cooling system for an emulsifier comprises an agitator tank 1, a header pipe 2, a cooling pipe 3, a heat preservation pipe 4 and a temperature monitor 5, wherein the agitator tank 1 is a double-layer agitator tank, the lower end of the agitator tank 1 is set to be in a conical structure, a feeding port 11 and a discharging port 12 are respectively arranged at the upper end and the lower end of the agitator tank 1, and the agitator tank 1 is provided with an interlayer 13. One end of the main pipe 2 is closed, the other end of the main pipe is fixed at the lower end of the stirring tank 1, and the inner cavity of the main pipe 2 is communicated with the interlayer 13.
Referring to fig. 1 and 2, the inner cavity of the cooling pipe 3 is communicated with the inner cavity of the main pipe 2, the cooling pipe 3 is used for guiding a cooling medium to the main pipe 2, the cooling medium may be cooling liquid or cold water, the cooling medium may be pumped by an external delivery pump or may be introduced by gravity through a height difference of a cooling tower, and a first valve 31 is fixed on the circumferential side of the cooling pipe 3. The inner cavity of the heat preservation pipe 4 is communicated with the inner cavity of the main pipe 2, the heat preservation pipe 4 is used for guiding heat preservation media to the main pipe 2, the heat preservation media can be hot oil or hot water, the preferred temperature is 75 ℃, the pumping principle of the heat preservation media can be the same as that of cooling media, and a second valve 41 is fixed on the periphery of the heat preservation pipe 4. The temperature monitor 5 is used to monitor the temperature of the emulsifier.
Referring to fig. 1 and 2, a motor 14 is fixed at the center of the top of the stirring tank 1, a stirring shaft 15 is arranged inside the stirring tank 1, the stirring shaft 15 is coaxially fixed on the rotating shaft of the motor 14, and the stirring shaft 15 is rotatably connected to the top wall of the stirring tank 1.
Referring to fig. 1 and 2, two scrapers 16 having an arc-shaped structure are disposed inside the stirring tank 1, the two scrapers 16 are disposed opposite to each other, and the plate surface of the scraper 16 is used for abutting against the inner wall of the stirring tank 1. Two scraper blades 16 all with be provided with many connecting rods 151 between the (mixing) shaft 15, the axis of connecting rod 151 is perpendicular with the axis of (mixing) shaft 15, many connecting rods 151 along the setting of arranging of (mixing) shaft 15's length direction equidistance interval, the both ends of connecting rod 151 respectively with (mixing) shaft 15 and scraper blade 16 towards the face fixed connection of (mixing) shaft 15. The middle of the connecting rod 151 is fixed with a second spoiler 152, and the second spoiler 152 is vertically disposed.
The implementation principle of the embodiment 1 is as follows: after the emulsifier is stirred in the stirring tank 1, opening the first valve 31, introducing a cooling medium into the interlayer 13 through the cooling pipe 3, cooling the emulsifier, and discharging the cooling medium in the interlayer 13 after the emulsifier is cooled to a specific temperature; then, the first valve 31 is closed, the second valve 41 is opened, a heat insulation medium is introduced into the interlayer 13 through the heat insulation pipe 4, the heat insulation of the emulsifier is carried out, and the effect of quickly adjusting and maintaining the temperature of the emulsifier to be filled is achieved. Meanwhile, the stirring shaft 15 continuously stirs the emulsifier to promote the uniformity of the temperature distribution of each part in the stirring tank 1.
Example 2
Referring to fig. 3 and 4, the present embodiment is different from embodiment 1 in that one end of the connecting rod 151 away from the stirring shaft 15 is fixedly connected to a side wall of the scraper 16, and the scraper 16 is obliquely disposed away from the side wall of the stirring shaft 15 and is provided with a chamfer.
Referring to fig. 5 and 6, a helical blade 17 is fixed on the circumferential side of the stirring shaft 15, a baffle 171 is integrally formed on the edge of the helical blade 17 away from the stirring shaft 15, the baffle 171 extends along the edge direction of the helical blade 17, and the surface of the baffle 171 is perpendicular to the axis of the stirring shaft 15. The rotation of the stirring shaft 15 drives the helical blades 17 to rotate, the emulsifier flows axially under the action of the helical blades 17, so that the emulsifier in the stirring tank 1 is exchanged up and down in the vertical direction, the separating and blocking piece 171 forms a certain separation and blocking for the emulsifier which moves along the radial direction under the action of centrifugal force, the up-and-down exchange efficiency of the emulsifier is improved, and the uniformity of temperature distribution of all parts in the stirring tank 1 is promoted
Referring to fig. 5 and 6, the side wall of the helical blade 17 away from the stirring shaft 15 is provided with a plurality of stirring blades 172, the stirring blades 172 are coplanar with the helical blade 17, and the plurality of stirring blades 172 are arranged at equal intervals along the edge direction of the helical blade 17. The stirring shaft 15 drives the stirring blade 172 to rotate when rotating, the stirring blade 172 shears the emulsifier, the surface of the stirring blade 172 is coplanar with the surface of the helical blade 17, so that the stirring blade 172 is obliquely arranged, the emulsifier is guided by the stirring blade 172 in the process of shearing the emulsifier, the vertical exchange of the emulsifier is promoted, and the uniformity of the temperature distribution of each part in the stirring tank 1 is further promoted
Referring to fig. 5 and 6, a first spoiler 173 is fixed to a surface of the agitating blade 172, and the surface of the first spoiler 173 is perpendicular to the surface of the agitating blade 172. The surface of the first spoiler 173 is formed with a plurality of through holes 174, and the through holes 174 are uniformly distributed on the surface of the first spoiler 173. When the stirring shaft 15 drives the first spoiler 173 to rotate, the emulsifier is cut at the edge of the through hole 174 to promote the flow of the emulsifier, and meanwhile, part of the emulsifier passes through the through hole 174 to reduce the rotation resistance of the stirring shaft 15.
The above embodiments are preferred embodiments of the present application, and the protection scope of the present application is not limited by the above embodiments, so: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.
Claims (8)
1. A ejection of compact cooling system for emulsifier which characterized in that: the device comprises a stirring tank (1), a cooling pipe (3), a heat preservation pipe (4) and a temperature monitor (5), wherein the stirring tank (1) is a double-layer stirring tank, and the stirring tank (1) is provided with an interlayer (13); the cooling pipe (3) is communicated with the interlayer (13), the cooling pipe (3) is used for guiding a cooling medium to the interlayer (13), and a first valve (31) is arranged on the periphery of the cooling pipe (3); the heat preservation pipe (4) is communicated with the interlayer (13), the heat preservation pipe (4) is used for guiding a heat preservation medium to the interlayer (13), and a second valve (41) is arranged on the periphery of the heat preservation pipe (4); the temperature monitor (5) is used for monitoring the temperature of the emulsifier.
2. The discharge cooling system for emulsifier according to claim 1, wherein: the heat-insulation pipe is characterized by further comprising a header pipe (2), the inner cavity of the cooling pipe (3) and the inner cavity of the heat-insulation pipe (4) are communicated with the inner cavity of the header pipe (2), and the inner cavity of the header pipe (2) is communicated with the interlayer (13).
3. The discharge cooling system for emulsifier according to claim 2, characterized in that: one end of the main pipe (2) is connected with the lower end of the stirring tank (1).
4. The discharge cooling system for emulsifier according to any one of claims 1 to 3, characterized in that: the discharge hole (12) of the stirring tank (1) is positioned at the lower end of the stirring tank (1), and the lower end of the stirring tank (1) is of a conical structure.
5. The discharge cooling system for emulsifier according to any one of claims 1 to 3, characterized in that: a stirring shaft (15) is arranged in the stirring tank (1), a motor (18) is arranged in the stirring tank (1), and the motor (18) is used for driving the stirring shaft (15) to rotate; at least one connecting rod (151) is arranged on the periphery of the stirring shaft (15), and a scraper (16) is arranged at one end, far away from the stirring shaft (15), of the connecting rod (151); the side butt of scraper blade (16) in the inner wall of agitator tank (1), scraper blade (16) are followed the direction of height of agitator tank (1) extends the setting, the slope of one side of the inner wall that is close to agitator tank (1) of scraper blade (16) sets up.
6. The discharge cooling system for emulsifier according to claim 5, wherein: the week side of (mixing) shaft (15) is provided with helical blade (17), helical blade (17) are kept away from the edge of (mixing) shaft (15) is provided with at a distance from separation blade (171), separate separation blade (171) and follow the edge direction of helical blade (17) extends the setting, separate the surface of separation blade (171) with the axis of (mixing) shaft (15) is parallel.
7. The discharge cooling system for emulsifier according to claim 6, wherein: the side wall of helical blade (17) keeping away from (mixing) shaft (15) is provided with a plurality of stirring vane (172), and a plurality of stirring vane (172) interval arrange the setting, the surface of stirring vane (172) with helical blade (17)'s surface coplane.
8. The discharge cooling system for emulsifier according to claim 7, wherein: the surface of the stirring blade (172) is provided with a first spoiler (173), the surface of the first spoiler (173) is perpendicular to the surface of the spiral blade (17), the surface of the first spoiler (173) is provided with a plurality of through holes (174) in a penetrating manner, and the through holes (174) are used for emulsifier to pass through.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222344139.0U CN218056731U (en) | 2022-09-03 | 2022-09-03 | A ejection of compact cooling system for emulsifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222344139.0U CN218056731U (en) | 2022-09-03 | 2022-09-03 | A ejection of compact cooling system for emulsifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218056731U true CN218056731U (en) | 2022-12-16 |
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ID=84409447
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222344139.0U Active CN218056731U (en) | 2022-09-03 | 2022-09-03 | A ejection of compact cooling system for emulsifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218056731U (en) |
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2022
- 2022-09-03 CN CN202222344139.0U patent/CN218056731U/en active Active
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