CN206853596U - Decoction continuous homogenizing system - Google Patents
Decoction continuous homogenizing system Download PDFInfo
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- CN206853596U CN206853596U CN201720389154.3U CN201720389154U CN206853596U CN 206853596 U CN206853596 U CN 206853596U CN 201720389154 U CN201720389154 U CN 201720389154U CN 206853596 U CN206853596 U CN 206853596U
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- tank
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- surge tank
- decoction
- connecting pipeline
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Abstract
It the utility model is related to a kind of decoction continuous homogenizing system, including emulsion tank, high pressure Microfluidizer, the connecting pipeline I between emulsion tank and high pressure Microfluidizer, it is characterised in that：Multiple non-conservation tanks and surge tank are separately sequentially provided with connecting pipeline I, the side wall upper part of surge tank is provided with inlet, lower sidewall is provided with liquid outlet, it is provided with the top of surge tank and is used to keep the pressure balanced respirator of tank body, the cleaning spray ball for realizing on-line cleaning and the bubble elimination device for defoaming, the bottom of surge tank to be provided with the blowoff line for being used for discharging rinse water and condensed water in on-line cleaning and sterilization process.Its is rational in infrastructure, using reliable, greatly reduces liquor residue amount, while ensure that the decoction saturation into homogenizer, will not cause the infringement to homogenizer.
Description
Technical field
It the utility model is related to a kind of decoction continuous homogenizing system.
Background technology
The production technology of existing decoction homogeneous system is：Decoction passes through pipeline to high pressure Microfluidizer through emulsion tank
It is repeated a number of times, but the problem of liquor residue is big, loss is more, caused foam is more is present, it is average about to be wasted per batch
10000ml decoctions, the yield of product is directly affected, and foam is more caused by pipeline in production process, the easy shape of homogenizer
Into unsaturated running status, the infringement to homogenizer is larger.
The content of the invention
The purpose of this utility model is to provide for a kind of decoction continuous homogenizing system for overcoming above mentioned problem, and structure is closed
Reason, using reliable, greatly reduce liquor residue amount, while ensure that the decoction saturation into homogenizer, will not cause pair
The infringement of homogenizer.
The technical solution of the utility model is：
A kind of decoction continuous homogenizing system, including emulsion tank, high pressure Microfluidizer, penetrate located at emulsion tank and high pressure are micro-
Flow the connecting pipeline I between homogenizer, it is characterised in that：Multiple non-conservation tanks and buffering are separately sequentially provided with the connecting pipeline I
Tank, the side wall upper part of the surge tank are provided with liquid outlet provided with inlet, lower sidewall, are provided with the top of the surge tank and are used to protect
Hold the pressure balanced respirator of tank body, cleaning spray ball and the dress of the removal of foam for defoaming for realizing on-line cleaning
Put, the bottom of the surge tank is provided with the blow-off pipe for being used for that rinse water and condensed water to be discharged in on-line cleaning and sterilization process
Road.
Above-mentioned decoction continuous homogenizing system, the bubble elimination device disappears foam device for stirring paddle, to be hit using machinery
Hit power and crush foam.
Above-mentioned decoction continuous homogenizing system, the charging aperture of the non-conservation tank connect with the liquid outlet of high pressure Microfluidizer
Lead to and be provided with control valve I in gating location, the discharging opening of the non-conservation tank is connected with connecting pipeline I and set in discharging opening position
There is control valve II.
Above-mentioned decoction continuous homogenizing system, the liquid outlet of the high pressure Microfluidizer using connecting pipeline II with into
Product tank connects and is respectively equipped with control valve III and control valve IV at the liquid inlet and outlet end of connecting pipeline II.
Above-mentioned decoction continuous homogenizing system, the outlet of the emulsion tank, the liquid outlet of high pressure Microfluidizer ease up
Rush and valve is respectively equipped with the blowoff line of tank.
The beneficial effects of the utility model are：
Due to setting up surge tank, the total residue of pipeline reduces about 2/5 after improvement, has significantly saved production cost；Together
When enter surge tank after caused foam simply float over decoction surface, and tank body has bubble elimination device in itself, will effectively can steep
Foam removes, and can ensure the decoction saturation into homogenizer, will not cause the infringement to homogenizer, enhance the guarantor to equipment
Shield.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
In figure：1. finished pot, 2. control valves IV, 3. connecting pipelines II, 4. non-conservation tanks, 5. control valves III, 6. control valves I,
7. control valve II, 8. emulsion tanks, 9. valves, 10. connecting pipelines I, 11. surge tanks, 12. respirators, 13. bubble elimination devices,
14. cleaning spray ball, 15. blowoff lines, 16. valves, 17. valves, 18. high pressure Microfluidizers.
Embodiment
As shown in figure 1, the decoction continuous homogenizing system, including emulsion tank 8, high pressure Microfluidizer 18, located at emulsification
Connecting pipeline I 10 between tank 8 and high pressure Microfluidizer 18, multiple turnovers are separately sequentially provided with the connecting pipeline I 10
Tank 4 and surge tank 11, the side wall upper part of the surge tank 11 are provided with liquid outlet, the surge tank provided with inlet, lower sidewall
11 tops, which are provided with, to be used to keep the pressure balanced respirator 12 of tank body, the cleaning for realizing on-line cleaning to spray ball 14 and be used for
The bubble elimination device 13 to defoam, the bottom of the surge tank 11, which is provided with, to be used to discharge in on-line cleaning and sterilization process
The blowoff line 15 of rinse water and condensed water.
In the present embodiment, the bubble elimination device 13 disappears foam device for stirring paddle, to crush bubble using mechanical impact
Foam.The quantity of non-conservation tank 4 is two, and the charging aperture of each non-conservation tank 4 connects simultaneously with the liquid outlet of high pressure Microfluidizer 18
Control valve I 6 is provided with gating location, the discharging opening of each non-conservation tank 4 is connected with connecting pipeline I 10 and set in discharging opening position
There is control valve II 7.The liquid outlet of the high pressure Microfluidizer 18 is connected with finished pot 1 using connecting pipeline II 3 and even
The liquid inlet and outlet end of adapter line II 3 is respectively equipped with control valve III 5 and control valve IV 2.The outlet of the emulsion tank 8, high pressure microjet
Valve 9,17,16 is respectively equipped with the liquid outlet of homogenizer 18 and the blowoff line 15 of surge tank 11.In the present embodiment, surge tank
11 volume is 5L, total residual about 6000ml after improvement, and about 4000ml decoctions are reduced compared with being remained than former technique.
Claims (5)
1. a kind of decoction continuous homogenizing system, including emulsion tank, high pressure Microfluidizer, located at emulsion tank and high pressure microjet
Connecting pipeline I between homogenizer, it is characterised in that：Multiple non-conservation tanks and surge tank are separately sequentially provided with the connecting pipeline I,
The side wall upper part of the surge tank is provided with inlet, lower sidewall is provided with liquid outlet, is provided with the top of the surge tank and is used to keep
The pressure balanced respirator of tank body, cleaning spray ball and the dress of the removal of foam for defoaming for realizing on-line cleaning
Put, the bottom of the surge tank is provided with the blow-off pipe for being used for that rinse water and condensed water to be discharged in on-line cleaning and sterilization process
Road.
2. decoction continuous homogenizing system according to claim 1, it is characterised in that：The bubble elimination device is agitating paddle
Formula disappears foam device.
3. decoction continuous homogenizing system according to claim 1, it is characterised in that：The charging aperture and high pressure of the non-conservation tank
The liquid outlet of Microfluidizer connects and is provided with control valve I, the discharging opening and connecting tube of the non-conservation tank in gating location
Line I connects and is provided with control valve II in discharging opening position.
4. decoction continuous homogenizing system according to claim 1, it is characterised in that：The high pressure Microfluidizer goes out
Liquid mouth is connected with finished pot using connecting pipeline II and control valve III is respectively equipped with the liquid inlet and outlet end of connecting pipeline II and is controlled
Valve IV.
5. decoction continuous homogenizing system according to claim 1, it is characterised in that：The outlet of the emulsion tank, high pressure are micro-
Valve is respectively equipped with the liquid outlet of jet homogenizer and the blowoff line of surge tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720389154.3U CN206853596U (en) | 2017-04-14 | 2017-04-14 | Decoction continuous homogenizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720389154.3U CN206853596U (en) | 2017-04-14 | 2017-04-14 | Decoction continuous homogenizing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206853596U true CN206853596U (en) | 2018-01-09 |
Family
ID=60817568
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720389154.3U Active CN206853596U (en) | 2017-04-14 | 2017-04-14 | Decoction continuous homogenizing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206853596U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109550455A (en) * | 2018-12-11 | 2019-04-02 | 黄冈华杰窑炉设备有限公司 | A kind of mixing arrangement of industrial tail gas cleanser |
| CN110624457A (en) * | 2018-06-21 | 2019-12-31 | 中国石油天然气股份有限公司 | Mobile liquid preparation system |
-
2017
- 2017-04-14 CN CN201720389154.3U patent/CN206853596U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110624457A (en) * | 2018-06-21 | 2019-12-31 | 中国石油天然气股份有限公司 | Mobile liquid preparation system |
| CN109550455A (en) * | 2018-12-11 | 2019-04-02 | 黄冈华杰窑炉设备有限公司 | A kind of mixing arrangement of industrial tail gas cleanser |
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