CN204522320U - Liquid vacuum enrichment facility - Google Patents
Liquid vacuum enrichment facility Download PDFInfo
- Publication number
- CN204522320U CN204522320U CN201520189202.5U CN201520189202U CN204522320U CN 204522320 U CN204522320 U CN 204522320U CN 201520189202 U CN201520189202 U CN 201520189202U CN 204522320 U CN204522320 U CN 204522320U
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- liquid
- enrichment facility
- chamber
- vaporization chamber
- condenser
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- 239000007788 liquid Substances 0.000 title claims abstract description 161
- 238000009834 vaporization Methods 0.000 claims abstract description 75
- 230000008016 vaporization Effects 0.000 claims abstract description 75
- 238000000926 separation method Methods 0.000 claims abstract description 74
- 239000006260 foam Substances 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 239000012530 fluid Substances 0.000 claims abstract description 7
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 4
- 230000008020 evaporation Effects 0.000 claims description 4
- 239000000203 mixture Substances 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000003814 drug Substances 0.000 description 12
- 239000000284 extract Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 8
- 239000004615 ingredient Substances 0.000 description 7
- 238000009835 boiling Methods 0.000 description 5
- 239000012141 concentrate Substances 0.000 description 3
- 230000008030 elimination Effects 0.000 description 3
- 238000003379 elimination reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 1
- 229930182490 saponin Natural products 0.000 description 1
- 150000007949 saponins Chemical class 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a kind of liquid vacuum enrichment facility.Liquid vacuum enrichment facility comprises: casing, has inner space; Vaporization chamber, have liquid inlet and liquid outlet, liquid enters into vaporization chamber by liquid inlet, is heated in vaporization chamber, and final concentrated liquid is discharged into outside by liquid outlet; Separation chamber, is communicated with vaporization chamber fluid, and liquid and the foam produced by heating due to liquid enter from vaporization chamber to be stated separation chamber, gas-liquid separation in separation chamber, and the liquid after gas-liquid separation flow back into vaporization chamber from separation chamber; Condenser, the gas after gas-liquid separation enters into condenser and is condensed into condensed water within the condenser from described separation chamber; Vavuum pump, makes vaporization chamber, separation chamber and condenser be in vacuum state.The original composition of liquid can be kept not run off according to liquid vacuum enrichment facility of the present utility model, and energy consumption is low.
Description
Technical field
The utility model relates to a kind of liquid vacuum enrichment facility, specifically, relates to and a kind ofly the original composition of liquid can be made not run off and the low liquid vacuum enrichment facility of energy consumption.
Background technology
Liquid is placed in container and heats by existing liquid concentration method, makes container internal pressure reduce simultaneously, thus liquid is evaporated.Specifically, existing liquid concentration method utilizes heating under reduced pressure that volatile ingredient is evaporated, and the steam of volatile ingredient is cooled in rear end/collects, and the non-volatile component after concentrated is stayed in container.
The concentrated of Chinese medicine extract has following characteristics: one, because Chinese medicine extract is usually containing materials such as sugar, protein, starch, saponin components, so stickiness is larger; Two, because some Chinese medicine extracts contain heat-sensitive ingredients, so also require low temperature, concentrate rapidly.Therefore, when using existing liquid concentration method to carry out concentrated to Chinese medicine extract, Chinese medicine extract easy bumping and run material in concentrator, and be difficult to the property of medicine of guarantee heat-sensitive ingredients, thus affect the quality of Chinese medicine extract, loss late is larger.
Utility model content
The utility model proposes a kind of liquid vacuum enrichment facility, to solve the problem that existing liquid concentrating device easily makes the original ingredients from lossing of liquid.
The utility model provides a kind of liquid vacuum enrichment facility, and liquid vacuum enrichment facility comprises: casing, has inner space; Vaporization chamber, is arranged on the top of described casing, has liquid inlet and liquid outlet, and liquid enters into described vaporization chamber by described liquid inlet, and is heated in described vaporization chamber, and final concentrated liquid is discharged into outside by described liquid outlet; Separation chamber, be arranged on the top of described casing and be communicated with described vaporization chamber fluid, described liquid and the foam produced by heating due to described liquid can enter into described separation chamber from described vaporization chamber, thus gas-liquid separation in described separation chamber, and the liquid after gas-liquid separation can flow back into described vaporization chamber from described separation chamber; Condenser, is arranged in described inner space, and the gas after gas-liquid separation can enter into described condenser from described separation chamber and be condensed into condensed water at described condenser; Vavuum pump, to be arranged in described inner space and to be communicated with described condenser fluid with described vaporization chamber, described separation chamber, being in vacuum state to make described vaporization chamber, described separation chamber and described condenser.
According to embodiment of the present utility model, described liquid vacuum enrichment facility also can comprise: blowdown piping, is arranged on the top of described vaporization chamber; Foam sensor, is arranged on the top of described separation chamber, for sensing the foam of inside, described separation chamber, wherein, when the foam of inside, described separation chamber exceedes predeterminated level, described blowdown piping is automatically opened, to make the pressure increase of foam, thus force bubble collapse.
According to embodiment of the present utility model, described blowdown piping can be provided with the first magnetic valve, with the inside enabling extraneous air optionally enter into described vaporization chamber.
According to embodiment of the present utility model, described vaporization chamber can comprise heater for heating liquid and the temperature sensor for the temperature that senses described evaporation chamber, wherein, when the temperature of described evaporation chamber reaches predetermined temperature, described vavuum pump brings into operation.
According to embodiment of the present utility model, described condenser can comprise the liquid level sensor of the liquid level for sensing described condenser inside and the temperature sensor for the temperature that senses described condenser inside, wherein, when the temperature of described condenser inside reaches predetermined temperature, automatically open inlet pipeline, enter in described condenser to allow external water stream.
According to embodiment of the present utility model, described liquid vacuum enrichment facility also can comprise vacuum buffer tank, described vacuum buffer tank is for storing the condensed water from described condenser, and described vacuum buffer tank comprises the liquid level sensor for sensing liquid level wherein, wherein, when the liquid level of described vacuum buffer tank inside is higher than predeterminated level, automatically open discharge pipe, flow out to outside to allow the condensed water in described vacuum buffer tank.
According to embodiment of the present utility model, described liquid vacuum enrichment facility also can comprise the separator between described vavuum pump and described condenser, for the described vavuum pump of protection.
According to embodiment of the present utility model, described liquid vacuum enrichment facility also can comprise Teat pipette, goes out Teat pipette and be discharged into outside described in the final concentrated liquid in described vaporization chamber passes through.
According to embodiment of the present utility model, described liquid vacuum enrichment facility also can comprise the cleaning channels for clean described vaporization chamber and described separation chamber.
According to embodiment of the present utility model, described liquid vacuum enrichment facility also can comprise be arranged on described casing top for controlling the control panel of the whole operation of described liquid vacuum enrichment facility.
Have the following advantages according to liquid vacuum enrichment facility of the present utility model: liquid boiling temperature is low, the heat-sensitive ingredients in Chinese medicine extract can not be destroyed; The foam produced in vaporization chamber is by the pressure differential automatic pulverizing between vaporization chamber and separation chamber, and the composition of Chinese medicine extract is without loss; The concentrated of variable concentrations can be carried out, to meet the different concentrated demand of various liquid to various liquid; Keep original components unchanged of liquid, improve the quality of concentrate, and reduce concentrated cost; Simple and reasonable for structure, achieve Automated condtrol, simple to operate.
Accompanying drawing explanation
By the detailed description carried out below in conjunction with accompanying drawing, above and other aspect of the present utility model, feature and other advantages will clearly be understood, wherein:
Fig. 1 is the structural representation of the liquid vacuum enrichment facility according to exemplary embodiment of the present utility model;
Fig. 2 is the schematic block diagram of the liquid vacuum enrichment facility according to exemplary embodiment of the present utility model.
Detailed description of the invention
Be described in detail exemplary embodiment of the present utility model now with reference to accompanying drawing, its sample table shows in the accompanying drawings, for the sake of clarity, may exaggerate the size of parts, and identical label represents same or analogous element all the time.
Fig. 1 is the structural representation of the liquid vacuum enrichment facility according to exemplary embodiment of the present utility model, and Fig. 2 is the schematic block diagram of the liquid vacuum enrichment facility according to exemplary embodiment of the present utility model.
See figures.1.and.2, the liquid vacuum enrichment facility according to exemplary embodiment of the present utility model comprises: casing 15, has inner space; Vaporization chamber 1, is arranged on the top of casing 15, and have liquid inlet 17 and liquid outlet 18, liquid enters into vaporization chamber 1 by liquid inlet 17, and is heated in vaporization chamber 1, and final concentrated liquid is discharged into outside by liquid outlet 18; Separation chamber 7, be arranged on the top of casing 15, and be communicated with vaporization chamber 1 fluid by top connecting pipeline 3, liquid and the foam produced by heating due to liquid can enter into separation chamber 7 by top connecting pipeline 3 from vaporization chamber 1, thus gas-liquid separation in separation chamber 7, and the liquid after gas-liquid separation can flow back into vaporization chamber 1 by bottom connecting pipeline 8 from separation chamber 7; Condenser 9, is arranged in described inner space, and the gas after gas-liquid separation enters into condenser 9 by pipeline 4 from separation chamber 7 and is condensed into condensed water at condenser 9; Vavuum pump 12, to be arranged in described inner space and to be communicated with condenser 9 fluid with vaporization chamber 1, separation chamber 7, being in vacuum state (such as, vacuum is for-0.08Mpa) to make vaporization chamber 1, separation chamber 7 and condenser 9.
Vaporization chamber 1 also can comprise: heater (such as, heating ring or heating plate), is arranged on bottom or the bottom of vaporization chamber 1, for heating liquid; Temperature sensor 161, is arranged in vaporization chamber 1, and for sensing the temperature of vaporization chamber 1 inside, when the temperature of vaporization chamber 1 inside reaches predetermined temperature (such as, 55 DEG C), vavuum pump 12 brings into operation; Blowdown piping 2, is arranged on the top of vaporization chamber 1; Blowdown piping 2 is provided with the first magnetic valve, with the inside making extraneous air optionally enter into vaporization chamber 1; Liquid level sensor 103, is arranged on the bottom of vaporization chamber 1, for sensing the liquid level of vaporization chamber 1 inside, when the liquid level of vaporization chamber 1 inside is lower than predeterminated level, closes heater to stop heating.
Separation chamber 7 also can comprise: foam sensor 5, is arranged on the top of separation chamber 7, for sensing the foam of inside, separation chamber 7, when the foam of inside, separation chamber 7 exceedes predeterminated level, open blowdown piping 2, to make the pressure increase of foam, thus force bubble collapse; Vacuum meter, for measuring and showing the pressure (vacuum) of inside, separation chamber 7; Liquid outlet, the liquid after the gas-liquid separation in separation chamber 7 is flow back in evaporimeter 1 by described liquid outlet.
Alternatively, the top of vaporization chamber 1 and separation chamber 7 can be made up of transparent high-boron-silicon glass, and are provided with scale on the transparent part of vaporization chamber 1 and the outer wall of separation chamber 7.
Condenser 9 can comprise: liquid level sensor 101, for sensing the liquid level of condenser 9 inside; Temperature sensor 162, for sensing the temperature of condenser 9 inside, the temperature when condenser 9 inside reaches predetermined temperature (such as, 36 DEG C), opens inlet pipeline 20, enters in condenser 9 to allow external water stream; Stop when the liquid level of condenser 9 inside reaches predeterminated level.Enter on pipeline 20 and be provided with the second magnetic valve, enter into condenser 9 optionally to allow outside water.
Alternatively, liquid vacuum enrichment facility according to exemplary embodiment of the present utility model also can comprise vacuum buffer tank 11, vacuum buffer tank 11 is for storing the condensed water of condenser 9, and vacuum buffer tank 11 comprises the liquid level sensor 102 for sensing liquid level wherein, when the liquid level of vacuum buffer tank 11 inside is higher than predeterminated level, open discharge pipe 22, to allow the condensed water elimination in vacuum buffer tank 11 to outside.Discharge pipe 22 is provided with the 3rd magnetic valve, optionally to allow the condensed water elimination in vacuum buffer tank 11 to outside.
Alternatively, also can comprise the separator 13 between vavuum pump 12 and vacuum buffer tank 11 according to the liquid vacuum enrichment facility of exemplary embodiment of the present utility model, for protection vavuum pump 12.
Alternatively, the liquid vacuum enrichment facility according to exemplary embodiment of the present utility model also can comprise Teat pipette 14, and the final concentrated liquid in vaporization chamber 1 passes through Teat pipette 14 and is discharged into outside.
Alternatively, the cleaning channels 19 of clean vaporization chamber 1 and separation chamber 7 is also can be used for according to the liquid vacuum enrichment facility of exemplary embodiment of the present utility model, vaporization chamber 1 and separation chamber 7 is entered into by cleaning channels to allow outside water, clean vaporization chamber 1 and separation chamber 7, the sewage after clean also passes through Teat pipette 14 and is discharged into outside.
Alternatively, also can comprise according to the liquid vacuum enrichment facility of exemplary embodiment of the present utility model be arranged on casing 15 top for controlling the control panel of the whole operation of liquid vacuum enrichment facility.
Referring to Fig. 1 and Fig. 2, the method for concentration according to the liquid vacuum enrichment facility of exemplary embodiment of the present utility model is described.
Liquid to be concentrated is placed in vaporization chamber 1, by heater, described liquid is heated, sense the temperature in vaporization chamber 1 by temperature sensor 161 simultaneously, when the temperature in vaporization chamber 1 reaches predetermined value (such as, 55 DEG C) time, open vavuum pump 12, with to vaporization chamber 1, separation chamber 7 and condenser 9 carry out vacuumizing (such as, vacuum can be-0.08Mpa), make liquid boiling, and produce steam, steam and liquid form foam, foam is full of vaporization chamber 1 fast, and increase the pressure of vaporization chamber 1 inside, thus pressure reduction is formed between vaporization chamber 1 and separation chamber 7, liquid bottom vaporization chamber 1 enters separation chamber 7 in the effect lower part of above-mentioned pressure reduction, and make to reach pressure balance rapidly between vaporization chamber 1 and separation chamber 7.Along with heater continuous heating, the foam in vaporization chamber 1 enters separation chamber 7 by top connecting pipeline 3, broken under the effect of the pressure reduction between vaporization chamber 1 and separation chamber 7, thus realizes gas-liquid separation.The reason running vavuum pump 12 when temperature in vaporization chamber 1 reaches 55 DEG C is: vacuum is little, boiling point is low, and now, the boiling point of Chinese medicine extract to be concentrated is approximately 60 DEG C, that is, run vavuum pump 12 in advance.Gas after gas-liquid separation enters into condenser 9 from separation chamber 7 and is condensed into condensed water at condenser 9, and the liquid after gas-liquid separation is flow back into vaporization chamber 1 by bottom connecting pipeline 8 from separation chamber 7 and continues to be heated until be concentrated into the concentration of requirement.
In the process that liquid is concentrated, the foam of inside, separation chamber 7 is sensed by foam sensor 5, when the foam of inside, separation chamber 7 exceedes predeterminated level, control panel carries out operating and automatically opening the first magnetic valve on blowdown piping 2, vaporization chamber 1 is entered into allow extraneous air, to make the pressure increase of foam, thus force bubble collapse.
In the process that liquid is concentrated, the liquid level of condenser 9 inside is sensed by liquid level sensor 101, and the temperature of condenser 9 inside is sensed by temperature sensor 162, when the temperature of condenser 9 inside reaches predetermined temperature, control panel carries out operating and automatically opening the second magnetic valve on inlet pipeline 20, allows external water stream to enter in condenser 9.Stop when the liquid level of condenser 9 inside reaches predeterminated level.
In the process that liquid is concentrated, the liquid level being sent to the condensed water vacuum buffer tank 11 from condenser 9 is sensed by liquid level sensor 102, when the liquid level in vacuum buffer tank 11 is higher than predeterminated level, control panel carries out operating and automatically opening the 3rd magnetic valve on discharge pipe 22, to allow the condensed water elimination in vacuum buffer tank 11 to outside.
The method for concentration concentrated according to liquid vacuum of the present utility model has the following advantages: liquid boiling temperature is low, can not destroy the heat-sensitive ingredients in Chinese medicine extract; The foam produced in vaporization chamber is by the pressure differential automatic pulverizing between vaporization chamber and separation chamber, and the composition of Chinese medicine extract is without loss; The concentrated of variable concentrations can be carried out, to meet the different concentrated demand of various liquid to various liquid; Keep original components unchanged of liquid, improve the quality of concentrate, and reduce concentrated cost.In addition to the advantages described above, also have the following advantages according to liquid vacuum enrichment facility of the present utility model: simple and reasonable for structure, achieve Automated condtrol, simple to operate.
Although describe and illustrated above-described embodiment of the present utility model, it should be appreciated by those skilled in the art that when not departing from the spirit and scope of the present utility model be defined by the claims, the various changes of form and details can have been carried out it.
Claims (10)
1. a liquid vacuum enrichment facility, is characterized in that comprising:
Casing, has inner space;
Vaporization chamber, is arranged on the top of described casing, has liquid inlet and liquid outlet, and liquid enters into described vaporization chamber by described liquid inlet, and is heated in described vaporization chamber, and final concentrated liquid is discharged into outside by described liquid outlet;
Separation chamber, be arranged on the top of described casing and be communicated with described vaporization chamber fluid, described liquid and the foam produced by heating due to described liquid can enter into described separation chamber from described vaporization chamber, thus gas-liquid separation in described separation chamber, and the liquid after gas-liquid separation can flow back into described vaporization chamber from described separation chamber;
Condenser, is arranged in described inner space, and the gas after gas-liquid separation can enter into described condenser from described separation chamber and be condensed into condensed water at described condenser;
Vavuum pump, to be arranged in described inner space and to be communicated with described condenser fluid with described vaporization chamber, described separation chamber, being in vacuum state to make described vaporization chamber, described separation chamber and described condenser.
2. liquid vacuum enrichment facility as claimed in claim 1, it is characterized in that, described liquid vacuum enrichment facility also comprises:
Blowdown piping, is arranged on the top of described vaporization chamber;
Foam sensor, is arranged on the top of described separation chamber, for sensing the foam of inside, described separation chamber,
Wherein, when the foam of inside, described separation chamber exceedes predeterminated level, automatically open described blowdown piping, to make the pressure increase of foam, thus force bubble collapse.
3. liquid vacuum enrichment facility as claimed in claim 2, is characterized in that, described blowdown piping is provided with the first magnetic valve, with the inside enabling extraneous air optionally enter into described vaporization chamber.
4. liquid vacuum enrichment facility as claimed in claim 1, it is characterized in that, described vaporization chamber comprises heater for heating liquid and the temperature sensor for the temperature that senses described evaporation chamber, wherein, when the temperature of described evaporation chamber reaches predetermined temperature, described vavuum pump brings into operation.
5. liquid vacuum enrichment facility as claimed in claim 1, it is characterized in that, described condenser comprises the liquid level sensor of the liquid level for sensing described condenser inside and the temperature sensor for the temperature that senses described condenser inside, wherein, when the temperature of described condenser inside reaches predetermined temperature, automatically open inlet pipeline, enter in described condenser to allow external water stream.
6. liquid vacuum enrichment facility as claimed in claim 1, it is characterized in that, described liquid vacuum enrichment facility also comprises vacuum buffer tank, described vacuum buffer tank is for storing the condensed water from described condenser, and described vacuum buffer tank comprises the liquid level sensor for sensing liquid level wherein, wherein, when the liquid level of described vacuum buffer tank inside is higher than predeterminated level, automatically open discharge pipe, flow out to outside to allow the condensed water in described vacuum buffer tank.
7. liquid vacuum enrichment facility as claimed in claim 1, it is characterized in that, described liquid vacuum enrichment facility also comprises the separator between described vavuum pump and described condenser, for the described vavuum pump of protection.
8. liquid vacuum enrichment facility as claimed in claim 1, it is characterized in that, described liquid vacuum enrichment facility also comprises Teat pipette, goes out Teat pipette and be discharged into outside described in the final concentrated liquid in described vaporization chamber passes through.
9. liquid vacuum enrichment facility as claimed in claim 1, is characterized in that, described liquid vacuum enrichment facility also comprises the cleaning channels for clean described vaporization chamber and described separation chamber.
10. liquid vacuum enrichment facility as claimed in claim 1, is characterized in that, described liquid vacuum enrichment facility also comprise be arranged on described casing top for controlling the control panel of the whole operation of described liquid vacuum enrichment facility.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520189202.5U CN204522320U (en) | 2015-03-31 | 2015-03-31 | Liquid vacuum enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520189202.5U CN204522320U (en) | 2015-03-31 | 2015-03-31 | Liquid vacuum enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204522320U true CN204522320U (en) | 2015-08-05 |
Family
ID=53736376
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520189202.5U Expired - Fee Related CN204522320U (en) | 2015-03-31 | 2015-03-31 | Liquid vacuum enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204522320U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106139622A (en) * | 2015-03-31 | 2016-11-23 | 北京东华原医疗设备有限责任公司 | Liquid vacuum enrichment facility and method for concentration thereof |
| CN116104760A (en) * | 2023-04-13 | 2023-05-12 | 沈阳凯世比泵阀有限公司 | Box vacuum system |
-
2015
- 2015-03-31 CN CN201520189202.5U patent/CN204522320U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106139622A (en) * | 2015-03-31 | 2016-11-23 | 北京东华原医疗设备有限责任公司 | Liquid vacuum enrichment facility and method for concentration thereof |
| CN106139622B (en) * | 2015-03-31 | 2018-01-30 | 北京东华原医疗设备有限责任公司 | Liquid vacuum enrichment facility and its method for concentration |
| CN116104760A (en) * | 2023-04-13 | 2023-05-12 | 沈阳凯世比泵阀有限公司 | Box vacuum system |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150805 Termination date: 20190331 |