CN220404829U - Concentrating and paste collecting device for animal and plant material extract - Google Patents
Concentrating and paste collecting device for animal and plant material extract Download PDFInfo
- Publication number
- CN220404829U CN220404829U CN202321431401.3U CN202321431401U CN220404829U CN 220404829 U CN220404829 U CN 220404829U CN 202321431401 U CN202321431401 U CN 202321431401U CN 220404829 U CN220404829 U CN 220404829U
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- Prior art keywords
- heat exchange
- exchange tube
- collecting
- cooling
- evaporation chamber
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- 239000000284 extract Substances 0.000 title claims abstract description 35
- 239000000463 material Substances 0.000 title claims abstract description 23
- 238000001704 evaporation Methods 0.000 claims abstract description 68
- 230000008020 evaporation Effects 0.000 claims abstract description 67
- 238000001816 cooling Methods 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 30
- 239000000498 cooling water Substances 0.000 claims description 27
- 239000011229 interlayer Substances 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 230000000007 visual effect Effects 0.000 claims description 4
- 238000011084 recovery Methods 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 6
- 238000009833 condensation Methods 0.000 description 11
- 230000005494 condensation Effects 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 4
- 230000008878 coupling Effects 0.000 description 3
- 238000010168 coupling process Methods 0.000 description 3
- 238000005859 coupling reaction Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000419 plant extract Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a device for concentrating and collecting animal and plant material extract, which is characterized by comprising the following components: the storage tank is communicated with the concentrator, and a vacuum pump is arranged on the concentrator; the concentrator comprises an evaporation module and a cooling module which are communicated with each other; the evaporation module comprises an evaporator and an evaporation chamber, wherein the evaporator is communicated with the storage tank and the evaporation chamber, and the evaporation chamber is connected with a paste collecting assembly; the cooling module comprises a heat exchange tube group, wherein the heat exchange tube group comprises a pre-cooling heat exchange tube and a condensing heat exchange tube, the pre-cooling heat exchange tube is connected with an evaporation chamber and the condensing heat exchange tube through a steam pipeline, the condensing heat exchange tube is connected with a collecting tank, an extracting solution is heated in the evaporation module to evaporate steam, part of the steam firstly enters the pre-cooling heat exchange tube to be cooled into a liquid state in advance, the rest of the steam is totally condensed into the liquid state through the condensing heat exchange tube, and the heat exchange tube group is utilized to enable the steam to complete total cooling, so that the negative pressure state inside the concentrator is kept, and the concentration effect is improved.
Description
Technical Field
The utility model relates to concentrating equipment, in particular to a concentrating and paste collecting device for animal and plant material extract.
Background
The traditional concentrating and paste collecting device utilizes a concentrator with a negative pressure state inside, the boiling point of an extraction liquid is reduced in the negative pressure state, the extraction liquid can be boiled to generate steam only by a lower heating temperature, the concentration treatment process is to heat the extraction liquid in an evaporation chamber to generate steam, evaporated gas is cooled into a liquid state through a tube array heat exchanger, and finally the liquid cooled by the steam is collected by a collecting tank.
Disclosure of Invention
The utility model provides a concentrating and paste collecting device for animal and plant material extract, which is used for solving the problem that partial steam cannot be cooled into liquid state so as to influence the negative pressure environment in the whole concentrator to cause poor concentrating effect in the prior art, and comprises the following steps: the storage tank is communicated with the concentrator, and a vacuum pump is arranged on the concentrator;
the concentrator comprises an evaporation module and a cooling module which are communicated with each other;
the evaporation module comprises an evaporator and an evaporation chamber, wherein the evaporator is communicated with the storage tank and the evaporation chamber, and the evaporation chamber is connected with a paste collecting assembly;
the cooling module comprises a heat exchange tube group, wherein the heat exchange tube group comprises a pre-cooling heat exchange tube and a condensing heat exchange tube, the pre-cooling heat exchange tube is connected with an evaporation chamber and the condensing heat exchange tube through a steam pipeline, and the condensing heat exchange tube is connected with a collecting tank.
In the structure, a safety valve, a feed inlet, a water inlet, a storage tank liquid level meter and a manhole are arranged on the storage tank.
In the above structure, the evaporator is connected to the storage tank through a pipe provided with a pipe pump, and the evaporator communicates with the evaporation chamber through a nozzle pipe and a circulation pipe.
In the structure, the evaporator is provided with a steam interlayer, and a steam inlet and a condensate outlet are arranged on the steam interlayer.
In the above structure, the paste collecting assembly comprises a paste collecting pipeline and a paste collecting pump.
In the above structure, the evaporation chamber is provided with a manhole, a visual mirror and a vacuum control assembly.
In the above structure, the vacuum control assembly comprises a vacuum control pipeline, a vacuum control valve and a vacuum gauge, wherein the vacuum control pipeline is communicated with the evaporation chamber, and the vacuum control valve and the vacuum gauge are arranged on the vacuum control pipeline.
In the structure, a vacuum interface is arranged at the joint of the condensation heat exchange tube and the collecting tank, and the vacuum interface is connected with a vacuum pump.
In the above structure, the collection tank is provided with a visual mirror, a collection tank level gauge and a recovery liquid outlet.
In the structure, the pre-cooling heat exchange tube and the condensation heat exchange tube are both provided with cooling water interlayers, the cooling water interlayers of the pre-cooling heat exchange tube and the condensation heat exchange tube are communicated through cooling water pipelines, and the cooling water interlayers are connected with a cooling tower.
The beneficial effects of the utility model are as follows: the cooling module comprises a heat exchange tube group, wherein the heat exchange tube group comprises a pre-cooling heat exchange tube and a condensing heat exchange tube, the pre-cooling heat exchange tube is connected with an evaporation chamber and the condensing heat exchange tube through a steam pipeline, the condensing heat exchange tube is connected with a collecting tank, an extracting solution is heated in the evaporation module to evaporate steam, part of the steam firstly enters the pre-cooling heat exchange tube to be cooled into a liquid state in advance, the rest of the steam is totally condensed into the liquid state through the condensing heat exchange tube, and the heat exchange tube group is utilized to enable the steam to complete total cooling, so that the negative pressure state inside the concentrator is kept, and the concentration effect is improved.
Drawings
The utility model will be further described with reference to the drawings and examples.
FIG. 1 is a schematic view of the assembly of the present utility model;
fig. 2 is a schematic diagram of the assembly of the concentrator of the present utility model.
Detailed Description
The conception, specific structure, and technical effects produced by the present utility model will be clearly and completely described below with reference to the embodiments and the drawings to fully understand the objects, features, and effects of the present utility model. It is apparent that the described embodiments are only some embodiments of the present utility model, but not all embodiments, and that other embodiments obtained by those skilled in the art without inventive effort are within the scope of the present utility model based on the embodiments of the present utility model. In addition, all the coupling/connection relationships referred to in the patent are not direct connection of the single-finger members, but rather, it means that a better coupling structure can be formed by adding or subtracting coupling aids depending on the specific implementation. The technical features in the utility model can be interactively combined on the premise of no contradiction and conflict.
The present utility model provides an embodiment:
as shown in fig. 1, an animal and plant material extract concentrating and paste collecting device comprises: the device comprises a storage tank 1 and a concentrator 2, wherein the storage tank 1 is communicated with the concentrator 2, and a vacuum pump 3 is arranged on the concentrator 2; the storage tank 1 is used for storing animal and plant material extract liquid, the concentrator 2 is used for concentrating and collecting paste of the animal and plant material extract liquid transferred from the storage tank 1, and the vacuum pump 3 is used for extracting gas in the concentrator to enable the concentrator 2 to be in a negative pressure state.
The concentrator 2 comprises an evaporation module 21 and a cooling module 22 which are mutually communicated, wherein the evaporation module 21 is used for heating and evaporating the extract, and the cooling module 22 is used for cooling and recycling the steam generated after evaporation.
The evaporation module 21 comprises an evaporator 211 and an evaporation chamber 212, wherein the evaporator 211 is communicated with the storage tank 1 and the evaporation chamber 212, and the evaporation chamber 212 is connected with the paste collecting assembly 4;
the evaporator 211 receives the animal and plant extract transferred from the storage tank 1, the evaporator 1 heats the animal and plant material extract, the animal and plant material extract is boiled and then is sprayed into the evaporation chamber 212, the boiled animal and plant material extract is evaporated into steam in the evaporation chamber 212, the bottom of the evaporation chamber 212 is connected with the paste receiving component 4, and the paste receiving component 4 is used for carrying out paste receiving treatment on the animal and plant extract concentrated and received by evaporation.
The cooling module 22 comprises a heat exchange tube set 221, the heat exchange tube set 221 is used for cooling steam, the heat exchange tube set 221 comprises a pre-cooling heat exchange tube 221a and a condensing heat exchange tube 221b, the pre-cooling heat exchange tube 221a is connected with an evaporation chamber 212 and the condensing heat exchange tube 221b through a steam pipeline, one end of the pre-cooling heat exchange tube 221a is connected with the evaporation chamber 212 through the steam pipeline, the other end of the pre-cooling heat exchange tube is connected with the condensing heat exchange tube 221b through the steam pipeline, steam generated by evaporation of the evaporation chamber 212 firstly enters the pre-cooling heat exchange tube to be pre-cooled, then enters the condensing heat exchange tube 221b to enable the steam to be completely cooled into a liquid state, the condensing heat exchange tube 221b is connected with a collecting tank 222, and the collecting tank 222 is used for collecting the cooled liquid.
On the basis of the above embodiment, the following scheme is preferable:
preferably, the storage tank 1 is provided with a safety valve 11, a feed inlet 12, a water inlet 13, a storage tank liquid level meter 14 and a manhole, the safety valve 11 is used for controlling the safety air pressure in the storage tank 1, the feed inlet 12 is used for pouring animal and plant material extract, the water inlet 13 is used for introducing water, a cleaning ball is arranged below the further water inlet 13 and used for dispersing the water introduced from the water inlet 13 out and used for cleaning the inner surface of the storage tank 1, the storage tank liquid level meter 14 is used for monitoring the liquid level in the storage tank, and personnel for manhole use enter the detection device.
Preferably, the evaporator 211 is connected to the storage tank 1 through a pipeline provided with a pipeline pump, the pipeline pump is used for pumping the animal and plant material extract in the storage tank 1 into the evaporator 211, the evaporator 211 is communicated with the circulating pipe 2112 through the spraying pipe 2111 to form an evaporation chamber 212, the spraying pipe 2111 is arranged above the evaporator 211, the extract liquid boiled in the evaporator 211 is sprayed into the evaporation chamber 212 from the spraying pipe 2111, the extract liquid is evaporated into steam in the evaporation chamber 212, the circulating pipe 2112 is arranged at the bottom of the evaporator 211, the circulating pipe 2112 is communicated with the bottom of the evaporation chamber 211, and the extract liquid enters the evaporator 211 again through the circulating pipe 2112 to be heated and boiled in the evaporation chamber 211 so as to realize the circular heating evaporation in the evaporator 211 and the evaporation chamber 212 until the extract liquid reaches the concentration meeting the standard.
Preferably, the evaporator 211 is provided with a steam interlayer 2113, a steam inlet 2114 and a condensate outlet 2115 are arranged on the steam interlayer 2113, high-temperature and high-pressure steam enters the steam interlayer 2113 from the steam inlet 2114 to heat the evaporator 211, and the condensate outlet 2115 is used for discharging condensate water formed by liquefying the steam due to temperature change in the steam interlayer 2113.
Preferably, the evaporation chamber 212 is provided with a paste collecting pipe 2121, the paste collecting pipe 2121 is arranged at the bottom of the evaporation chamber 212 and is used for transferring the concentrated extract liquid in the evaporation chamber 212, the paste collecting pipe 2121 is provided with a paste collecting pump 2122, and the paste collecting pump 2122 is used for extracting the concentrated extract liquid in the evaporation chamber 212.
Preferably, the evaporation chamber 212 is provided with a manhole for personnel to enter the evaporation chamber 212 for detection, a visual mirror for observing the condition in the evaporation chamber 212, and a vacuum control assembly 2123 for controlling the vacuum degree in the evaporation chamber 212.
Preferably, the vacuum control assembly 2123 includes a vacuum control conduit 2124, a vacuum control valve 2125, and a vacuum gauge 2126, the vacuum control conduit 2124 being in communication with the evaporation chamber 212, the vacuum control valve 2125 being disposed on the vacuum control conduit 2124 with the vacuum gauge 2126, the vacuum control conduit 2124 being configured to communicate with the evaporation chamber 212 so that the vacuum control valve 2125 regulates the vacuum level inside the evaporation chamber 212 and so that the vacuum gauge 2126 monitors the vacuum level inside the evaporation chamber 212.
Preferably, a vacuum interface 31 is arranged at the connection part of the condensation heat exchange tube 221a and the collection tank 222, the vacuum interface 31 is connected with a vacuum pump 3, and the vacuum pump 3 draws air from the vacuum interface 31 to form a negative pressure state in the concentrator 2.
Preferably, the collection tank 222 is provided with a sight glass for observing the condition in the collection tank 222, a collection tank level gauge for observing the liquid level in the collection pipe, and a recovery liquid discharge port for discharging the collected steam condensate.
Preferably, the pre-cooling heat exchange tube 221a and the condensation heat exchange tube 221b are provided with a cooling water interlayer 223, the pre-cooling heat exchange tube 221a is communicated with the cooling water interlayer 223 of the condensation heat exchange tube 221b through a cooling water pipeline, the cooling water interlayer is connected with a cooling tower, the condensation heat exchange tube 221b is provided with a cooling water inlet, the pre-cooling heat exchange tube 221a is provided with a cooling water outlet, the cooling water inlet and the cooling water outlet are connected with the cooling tower through the cooling water pipeline, cooling water enters the cooling water interlayer 223 of the condensation heat exchange tube 221b from the cooling water inlet, then enters the cooling water interlayer of the pre-cooling heat exchange tube 221a through the cooling water pipeline between the cooling water interlayer of the pre-cooling heat exchange tube 221a and the cooling water interlayer 223 of the condensation heat exchange tube 221b, and returns to the cooling tower from the cooling water outlet of the cooling water interlayer 223 of the pre-cooling heat exchange tube 221a, so that cooling water circulation is realized for refrigerating the pre-cooling heat exchange tube 221a and the condensation heat exchange tube 221 b.
When the embodiment is implemented, animal and plant material extract is pumped into an evaporator from a storage tank to be heated, the extract is heated and boiled and then is sprayed into an evaporation chamber through a spray pipe, the extract is evaporated in the evaporation chamber to form steam, the steam firstly enters a pre-cooling heat exchange tube to be pre-cooled through a steam pipeline, then is totally condensed into a liquid state through a condensation heat exchange tube, the steam is completely cooled through a heat exchange tube group, the negative pressure state in the concentrator is favorably maintained, the concentration effect is improved, the extract reserved in the evaporation chamber after evaporation reaches the calibrated concentration to stop heating, finally the concentrated extract in the evaporation chamber is pumped through a paste collecting pump of a paste collecting pipeline, and the concentrated extract is collected after pumping.
While the preferred embodiment of the present utility model has been described in detail, the present utility model is not limited to the embodiments, and those skilled in the art can make various equivalent modifications or substitutions without departing from the spirit of the present utility model, and these equivalent modifications or substitutions are included in the scope of the present utility model as defined in the appended claims.
Claims (10)
1. An animal and plant material extract concentrating and paste collecting device, which is characterized by comprising: the storage tank is communicated with the concentrator, and a vacuum pump is arranged on the concentrator; the concentrator comprises an evaporation module and a cooling module which are communicated with each other;
the evaporation module comprises an evaporator and an evaporation chamber, wherein the evaporator is communicated with the storage tank and the evaporation chamber, and the evaporation chamber is connected with a paste collecting assembly;
the cooling module comprises a heat exchange tube group, wherein the heat exchange tube group comprises a pre-cooling heat exchange tube and a condensing heat exchange tube, the pre-cooling heat exchange tube is connected with an evaporation chamber and the condensing heat exchange tube through a steam pipeline, and the condensing heat exchange tube is connected with a collecting tank.
2. The animal and plant material extract concentrating and paste collecting device according to claim 1, wherein the storage tank is provided with a safety valve, a feed inlet, a water inlet, a storage tank liquid level gauge and a manhole.
3. The device for concentrating and collecting animal and plant material extract according to claim 1, wherein the evaporator is connected with the storage tank through a pipeline provided with a pipeline pump, and the evaporator is communicated with the evaporation chamber through a spray pipe and a circulating pipe.
4. The animal and plant material extract concentrating and paste collecting device according to claim 1, wherein the evaporator is provided with a steam interlayer, and a steam inlet and a condensate outlet are arranged on the steam interlayer.
5. The device for concentrating and collecting animal and plant material extract according to claim 1, wherein the collecting assembly comprises a collecting pipe and a collecting pump.
6. The animal and plant material extract concentrating and paste collecting device according to claim 1, wherein a manhole, a visual mirror and a vacuum control assembly are arranged on the evaporation chamber.
7. The device of claim 6, wherein the vacuum control assembly comprises a vacuum control pipe, a vacuum control valve and a vacuum gauge, the vacuum control pipe is communicated with the evaporation chamber, and the vacuum control valve and the vacuum gauge are arranged on the vacuum control pipe.
8. The animal and plant material extract concentrating and paste collecting device according to claim 1, wherein a vacuum interface is arranged at the joint of the condensing heat exchange tube and the collecting tank, and the vacuum interface is connected with a vacuum pump.
9. The plant and animal material extract concentrating and paste collecting apparatus according to claim 1, wherein the collecting tank is provided with a sight glass, a collecting tank level gauge and a recovery liquid outlet.
10. The device for concentrating and collecting the extract of the animal and plant materials according to claim 1, wherein the pre-cooling heat exchange tube and the condensing heat exchange tube are both provided with a cooling water interlayer, the cooling water interlayer of the pre-cooling heat exchange tube and the condensing heat exchange tube is communicated with each other through a cooling water pipeline, and the cooling water interlayer is connected with a cooling tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321431401.3U CN220404829U (en) | 2023-06-06 | 2023-06-06 | Concentrating and paste collecting device for animal and plant material extract |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321431401.3U CN220404829U (en) | 2023-06-06 | 2023-06-06 | Concentrating and paste collecting device for animal and plant material extract |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220404829U true CN220404829U (en) | 2024-01-30 |
Family
ID=89659744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321431401.3U Active CN220404829U (en) | 2023-06-06 | 2023-06-06 | Concentrating and paste collecting device for animal and plant material extract |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220404829U (en) |
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2023
- 2023-06-06 CN CN202321431401.3U patent/CN220404829U/en active Active
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