CN109173809A - A kind of multifunctional efficient emulsifying device heat-exchange system - Google Patents
A kind of multifunctional efficient emulsifying device heat-exchange system Download PDFInfo
- Publication number
- CN109173809A CN109173809A CN201811145027.4A CN201811145027A CN109173809A CN 109173809 A CN109173809 A CN 109173809A CN 201811145027 A CN201811145027 A CN 201811145027A CN 109173809 A CN109173809 A CN 109173809A
- Authority
- CN
- China
- Prior art keywords
- emulsion tank
- heat exchange
- exchange coil
- heat
- tank
- 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.)
- Pending
Links
- 230000001804 emulsifying effect Effects 0.000 title claims abstract description 17
- 239000000839 emulsion Substances 0.000 claims abstract description 65
- 239000000463 material Substances 0.000 claims abstract description 41
- 230000008676 import Effects 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims description 16
- 238000004945 emulsification Methods 0.000 claims description 8
- 238000010992 reflux Methods 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 5
- 238000005498 polishing Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 239000006071 cream Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000003292 glue Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/271—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator
- B01F27/2711—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed radially between the surfaces of the rotor and the stator provided with intermeshing elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/51—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
- B01F35/92—Heating or cooling systems for heating the outside of the receptacle, e.g. heated jackets or burners
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Accessories For Mixers (AREA)
Abstract
The present invention relates to a kind of multifunctional efficient emulsifying device heat-exchange systems, including emulsion tank (1), collet (2), heat exchange coil (3) and pump (4), in which: collet (2) is sheathed on emulsion tank (1) outside；Heat exchange coil (3) is set in collet (2), one end of heat exchange coil (3) is connected to as Matter Transfer import with emulsion tank (1) bottom, and the other end of heat exchange coil (3) is exported as Matter Transfer and is connected at the top of emulsion tank (1)；(4) are pumped for the circulation conveying by material between emulsion tank (1) and heat exchange coil (3).Compared with prior art, the present invention substantially increases the heat exchange efficiency of heating, cooling, improves product processing quality, and enhances the deaeration ability of equipment.
Description
Technical field
The present invention relates to technical field of heat exchange, more particularly, to a kind of multifunctional efficient emulsifying device heat-exchange system.
Background technique
The emulsifying device of daily use chemicals industry at present, generallys use jacket for heat exchange, i.e., heat transferring medium is passed through on the outside of kettle tank, and (industry is steamed
Vapour or chilled water), and when emulsification tank volume is excessive, heat exchange area is extremely limited, this causes heat exchange efficiency very low.And whole
In a production process, being heated or cooled is exactly most to influence two key factors of efficiency to directly affect product quality, also shadow
It rings and arrives production efficiency.How to be rapidly cooled at low cost to the material in emulsifying device is that those skilled in the art need to solve
Certainly the technical issues of.
Summary of the invention
It is an object of the present invention to overcome the above-mentioned drawbacks of the prior art and provide a kind of multifunctional efficient creams
Change equipment heat-exchange system.
The purpose of the present invention can be achieved through the following technical solutions:
A kind of multifunctional efficient emulsifying device heat-exchange system, including emulsion tank, further includes:
Collet is sheathed on outside emulsion tank,
Heat exchange coil is set in collet, and one end of heat exchange coil is connected to as Matter Transfer import with emulsification pot bottom,
The other end of heat exchange coil is exported as Matter Transfer and is connected at the top of emulsion tank,
Pump, for the circulation conveying by material between emulsion tank and heat exchange coil.
Collet, heat exchange coil and pump of the invention constitutes external circulation heat exchanging unit, and external circulation heat exchanging unit of the invention can
To be improved on existing, additional heat exchange equipment is not increased, application cost is not high.Outer circulation pump is relied primarily on to carry out
Conveying, material is delivered in collet from tank base, in the form of spiral coil, is passed through collet, then enter cream from tank body upper end
Change tank, forms circulation.Part in collet but really considerably increases heat exchange area not with media contact in collet, heat exchange effect
Rate increase by 40% or more (containing heating and cooling process all can).
External circulation heat exchanging unit of the invention can also bring an additional benefit.Material in reality in emulsion tank is to want
It carries out while stirring deaeration operation (such as vacuumizing de-bubble), and upper layer bubble can be imported to bottom in whipping process, in this way
Deaeration can be made to become more difficult.And the application is by importeding into emulsification by heat exchange coil circulation for the material for emulsifying pot bottom
Tank upper layer, to be more conducive to the deaeration of material.External circulation heat exchanging unit also enhances de- while improving heat transfer effect
Bubble ability.
Preferably, the heat exchange coil is spiral heat exchange coil, is arranged on the outside of emulsion tank in the shape of a spiral.
Preferably, the Matter Transfer import of heat exchange coil is connected to by bottom discharge pipeline with emulsification pot bottom, heat exchange plate
The Matter Transfer outlet of pipe at the top of top feed pipeline and emulsion tank by being connected to.
Preferably, the pump is impeller pump or diaphragm pump, is set on bottom discharge pipeline.
The circulation of material rely primarily on external pump conveyed (the solution of the present invention there are certain requirements the viscosity of material,
It is recommended that dynamic viscosity is not more than 50000cps), material is exchanged heat in collet by heat exchange coil, is recycled back into emulsion tank
Portion.Form complete closed loop cycle.Meanwhile the material inside emulsion tank, also simultaneously carried out that control is heated or cooled with collet.
Preferably, reflux pipeline section, the material on reflux the pipeline section top and heat exchange coil are equipped in the emulsion tank
Loop exit connection, bottom end are bent to emulsion tank inner sidewall.
Deaeration is carried out by defoaming device since emulsion tank is typically necessary, avoids the generation of bubble, the present invention passes through back
The deaeration material for flowing back into emulsion tank is guided to emulsification pot sidewall, is allowed to slowly flow down along side wall, avoid by flow tube road
It since material directly falls causes to blister again in reflux course.
Preferably, the material of the heat exchange coil use SUS316 stainless steel material, heat exchange coil inner wall polishing degree Ra <
0.8。
Preferably, the emulsion tank is vertical emulsion tank, is equipped with center agitating paddle and edge agitating paddle, institute in emulsion tank
The center agitating paddle stated is by the central stirring shaft that is arranged along vertical emulsion tank central axis and is distributed in more in central stirring shaft
A center blade composition, the top of the central stirring shaft, which passes through, to be connect at the top of emulsion tank with motor drive；The edge
Agitating paddle is by multiple edge supports bars for being set to the terminal pad of central stirring shaft bottom end, stretching out from terminal pad and is set to
Multiple edge blades composition on each edge supports bar, the edge blade are staggeredly set in emulsion tank axial direction with center blade
It sets.
The present invention can also further pass through setting center agitating paddle and edge agitating paddle, being capable of effectively improving material stirring
Efficiency strengthens the Flow of Goods and Materials inside emulsion tank, to enhance heat transfer effect.
Compared with prior art, the invention has the following advantages:
1. substantially increasing the heat exchange efficiency of heating, cooling, since the two steps are in entire technical process, the time is accounted for
Than highest, so that the present invention can greatly improve working efficiency (improving efficiency about 40%).
2. part soap base or foundation cream class formula, have very high requirement to cooling efficiency, not only the influence of efficiency, quickly
Cooling can also make material have good appearance, and quality is more stable, improves product processing quality.
3. external circulation heat exchanging unit also enhances deaeration ability while improving heat transfer effect, double at one stroke.
4. center agitating paddle and edge agitating paddle strengthen the Flow of Goods and Materials in emulsion tank, and external circulation heat exchanging unit matching,
Further enhance heat transfer effect.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is that (arrow direction is material in figure for the flow schematic diagram of material in heat exchange coil in Fig. 1 at Section A-A
Flow direction).
In figure, 1 is emulsion tank, and 2 be collet, and 3 be heat exchange coil, and 4 be pump, and 5 be bottom discharge pipeline, and 6 be top feed
Pipeline, 71 be center agitating shaft, and 72 be center blade, and 81 be terminal pad, and 82 be edge supports bar, and 83 be edge blade, and 9 are back
Flow tube section.
Specific embodiment
The present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Embodiment 1
A kind of multifunctional efficient emulsifying device heat-exchange system, as shown in Fig. 1~2, including emulsion tank 1, further includes:
Collet 2 is sheathed on outside emulsion tank 1,
Heat exchange coil 3 is set in collet 2, and one end of heat exchange coil 3 is as Matter Transfer import and 1 bottom of emulsion tank
The other end of connection, heat exchange coil 3 is exported as Matter Transfer and is connected at the top of emulsion tank 1,
Pump 4, for the circulation conveying by material between emulsion tank 1 and heat exchange coil 3.
Collet, heat exchange coil and pump of the invention constitutes external circulation heat exchanging unit, and external circulation heat exchanging unit of the invention can
To be improved on existing, additional heat exchange equipment is not increased, application cost is not high.Outer circulation pump is relied primarily on to carry out
Conveying, material is delivered in collet from tank base, in the form of spiral coil, is passed through collet, then enter cream from tank body upper end
Change tank, forms circulation.Part in collet but really considerably increases heat exchange area not with media contact in collet, heat exchange effect
Rate increase by 40% or more (containing heating and cooling process all can).
External circulation heat exchanging unit of the invention can also bring an additional benefit.Material in reality in emulsion tank is to want
It carries out while stirring deaeration operation (such as vacuumizing de-bubble), and upper layer bubble can be imported to bottom in whipping process, in this way
Deaeration can be made to become more difficult.And the application is by importeding into emulsification by heat exchange coil circulation for the material for emulsifying pot bottom
Tank upper layer, to be more conducive to the deaeration of material.External circulation heat exchanging unit also enhances de- while improving heat transfer effect
Bubble ability.
In the present invention, heat exchange coil 3 is spiral heat exchange coil, is arranged on the outside of emulsion tank 1 in the shape of a spiral.Material is from cream
Change the heat transferring medium after pot bottom flows out in spiral heat exchange coil in spiral, with collet sufficiently to exchange heat, cooling efficiency
It is high.The Matter Transfer import of heat exchange coil 3 is connected to by bottom discharge pipeline 5 with 1 bottom of emulsion tank, the material of heat exchange coil 3
Loop exit at the top of top feed pipeline 6 and emulsion tank 1 by being connected to.Pump 4 can choose as impeller pump or diaphragm pump, be set to
On bottom discharge pipeline 5.The conveying power of material relies primarily on external pump and is conveyed that (the solution of the present invention glues material
Degree there are certain requirements, it is proposed that dynamic viscosity is not more than 50000cps), material is exchanged heat in collet by coil pipe, is recycled back into
Inside emulsion tank.Form complete closed loop cycle.Meanwhile the Material inside emulsion tank, also simultaneously with collet carry out heating or it is cold
But it controls.The material of heat exchange coil 3 uses SUS316 stainless steel material, 3 inner wall polishing degree Ra < 0.8 of heat exchange coil.Coil diameter
It is set according to the size of equipment, the coil pipe nominal diameter for presetting 1000L emulsion pot is not less than 1 cun, to be not easy to result in blockage
The corner or spot as yet untouched by a clean-up campaign and.
Reflux pipeline section 9 is equipped in the present embodiment, in emulsion tank 1, the Matter Transfer on flow back pipeline section 9 top and heat exchange coil 3
Outlet connection, bottom end are bent to 1 inner sidewall of emulsion tank.It is taken off this is because emulsion tank is typically necessary by defoaming device
Bubble, avoids the generation of bubble, and the present invention is guided the deaeration material for flowing back into emulsion tank to emulsion tank side by reflux line
It on wall, is allowed to slowly flow down along side wall, avoids in reflux course and cause to blister again since material directly falls.
In this implementation, emulsion tank 1 is vertical emulsion tank, is equipped with center agitating paddle and edge agitating paddle, center in emulsion tank 1
Agitating paddle is by along the central stirring shaft 71 that vertical 1 central axis of emulsion tank is arranged and being distributed in multiple in central stirring shaft 71
Heart blade 72 forms, and the top of central stirring shaft 71 passes through 1 top of emulsion tank and connect with motor drive；Edge agitating paddle is by being arranged
In the terminal pad 81 of 71 bottom end of central stirring shaft, the multiple edge supports bars 82 stretched out from terminal pad 81 and it is set to each side
Multiple edge blades 83 composition on edge support rod 82, edge blade 83 are staggeredly set in 1 axial direction of emulsion tank with center blade 72
It sets.By setting center agitating paddle and edge agitating paddle, can effective improving material stirring efficiency, strengthen the object inside emulsion tank
Stream is dynamic, to enhance heat transfer effect.
The above-mentioned description to embodiment is for ease of ordinary skill in the art to understand and use the invention.It is ripe
The personnel for knowing art technology obviously easily can make various modifications to these embodiments, and general original described herein
It ought to use in other embodiments without having to go through creative labor.Therefore, the present invention is not limited to the above embodiments, this field
Technical staff's announcement according to the present invention, improvement and modification made without departing from the scope of the present invention all should be in guarantors of the invention
Within the scope of shield.
Claims (7)
1. a kind of multifunctional efficient emulsifying device heat-exchange system, including emulsion tank (1), which is characterized in that further include:
Collet (2) is sheathed on emulsion tank (1) outside,
Heat exchange coil (3) is set in collet (2), and one end of heat exchange coil (3) is as Matter Transfer import and emulsion tank (1)
The other end of bottom connection, heat exchange coil (3) is exported as Matter Transfer and is connected at the top of emulsion tank (1),
It pumps (4), for the circulation conveying by material between emulsion tank (1) and heat exchange coil (3).
2. a kind of multifunctional efficient emulsifying device heat-exchange system according to claim 1, which is characterized in that the heat exchange
Coil pipe (3) is spiral heat exchange coil, is arranged on the outside of emulsion tank (1) in the shape of a spiral.
3. a kind of multifunctional efficient emulsifying device heat-exchange system according to claim 1, which is characterized in that heat exchange coil
(3) Matter Transfer import is connected to by bottom discharge pipeline (5) with emulsion tank (1) bottom, the Matter Transfer of heat exchange coil (3)
Outlet at the top of top feed pipeline (6) and emulsion tank (1) by being connected to.
4. a kind of multifunctional efficient emulsifying device heat-exchange system according to claim 3, which is characterized in that the pump
(4) it is impeller pump or diaphragm pump, is set on bottom discharge pipeline (5).
5. a kind of multifunctional efficient emulsifying device heat-exchange system according to claim 1, which is characterized in that the emulsification
Reflux pipeline section (9) is equipped in tank (1), the Matter Transfer outlet of reflux pipeline section (9) top and heat exchange coil (3) connects,
Bottom end is bent to emulsion tank (1) inner sidewall.
6. a kind of multifunctional efficient emulsifying device heat-exchange system according to claim 1, which is characterized in that the heat exchange
The material of coil pipe (3) uses SUS316 stainless steel material, heat exchange coil (3) inner wall polishing degree Ra < 0.8.
7. a kind of multifunctional efficient emulsifying device heat-exchange system according to claim 1, which is characterized in that the emulsification
Tank (1) is vertical emulsion tank, is equipped with center agitating paddle and edge agitating paddle in emulsion tank (1), the center agitating paddle is by edge
The central stirring shaft (71) of vertical emulsion tank (1) central axis setting and the multiple center paddles being distributed on central stirring shaft (71)
Leaf (72) composition, the top of the central stirring shaft (71), which passes through, to be connect at the top of emulsion tank (1) with motor drive；The side
Edge agitating paddle is by multiple edge branch for being set to the terminal pad (81) of central stirring shaft (71) bottom end, stretching out from terminal pad (81)
Strut (82) and the multiple edge blades (83) being set on each edge supports bar (82) composition, the edge blade (83)
It is staggered in emulsion tank (1) axial direction with center blade (72).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811145027.4A CN109173809A (en) | 2018-09-29 | 2018-09-29 | A kind of multifunctional efficient emulsifying device heat-exchange system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811145027.4A CN109173809A (en) | 2018-09-29 | 2018-09-29 | A kind of multifunctional efficient emulsifying device heat-exchange system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109173809A true CN109173809A (en) | 2019-01-11 |
Family
ID=64907867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811145027.4A Pending CN109173809A (en) | 2018-09-29 | 2018-09-29 | A kind of multifunctional efficient emulsifying device heat-exchange system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109173809A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621876A (en) * | 2019-01-24 | 2019-04-16 | 江西立德传动设备有限公司 | A kind of liquid material combination cooling device |
| CN112774530A (en) * | 2020-12-17 | 2021-05-11 | 江西省华宝孔雀食品科技发展有限公司 | Emulsification tank suitable for production of a small amount of essence |
| CN113797791A (en) * | 2021-09-01 | 2021-12-17 | 联业织染(珠海)有限公司 | High-uniformity compound blending device and blending method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1157437A (en) * | 1997-08-26 | 1999-03-02 | Lion Corp | Manufacturing of emulsified liquid |
| CN102563845A (en) * | 2012-02-03 | 2012-07-11 | 美的集团有限公司 | Composite quick-heating heat exchanger |
| CN105363381A (en) * | 2015-12-09 | 2016-03-02 | 唐盛元成（天津）健康科技有限公司 | Homogenizing and emulsifying machine |
| CN205340598U (en) * | 2016-01-07 | 2016-06-29 | 宿迁市万尚新材料科技有限公司 | Vacuum emulsification reation kettle |
| CN209254571U (en) * | 2018-09-29 | 2019-08-16 | 上海百雀羚生物科技有限公司 | A kind of multifunctional efficient emulsifying device heat-exchange system |
-
2018
- 2018-09-29 CN CN201811145027.4A patent/CN109173809A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1157437A (en) * | 1997-08-26 | 1999-03-02 | Lion Corp | Manufacturing of emulsified liquid |
| CN102563845A (en) * | 2012-02-03 | 2012-07-11 | 美的集团有限公司 | Composite quick-heating heat exchanger |
| CN105363381A (en) * | 2015-12-09 | 2016-03-02 | 唐盛元成（天津）健康科技有限公司 | Homogenizing and emulsifying machine |
| CN205340598U (en) * | 2016-01-07 | 2016-06-29 | 宿迁市万尚新材料科技有限公司 | Vacuum emulsification reation kettle |
| CN209254571U (en) * | 2018-09-29 | 2019-08-16 | 上海百雀羚生物科技有限公司 | A kind of multifunctional efficient emulsifying device heat-exchange system |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621876A (en) * | 2019-01-24 | 2019-04-16 | 江西立德传动设备有限公司 | A kind of liquid material combination cooling device |
| CN112774530A (en) * | 2020-12-17 | 2021-05-11 | 江西省华宝孔雀食品科技发展有限公司 | Emulsification tank suitable for production of a small amount of essence |
| CN113797791A (en) * | 2021-09-01 | 2021-12-17 | 联业织染(珠海)有限公司 | High-uniformity compound blending device and blending method |
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